[0001] The present invention relates to a chronotherapeutic dosage form containing a therapeutically
effective amount of a drug. The present invention is further related to methods of
preparing such formulations, and to methods of treatment utilizing such formulations.
[0002] Coordinating biological rhythms (chronobiology) with medical treatment is called
chronotherapy. Chronotherapy takes into consideration a person's biological rhythms
in determining the timing - and sometimes the amount - of medication to optimize desired
effects of a drug(s) and minimize the undesired effects. The synchronization of medication
levels to the biological rhythms of disease activity is playing an increasing role
in the management of common cardiovascular conditions such as hypertension, elevated
cholesterol, angina, stroke and ischemic heart disease, according to experts in this
new and ever-expanding field. For example, in humans, at 1am post-surgical death is
most likely; at 2am peptic ulcers flare up; at 3am blood pressure bottoms out; at
4am asthma is at its worst. When one wakes up, hay fever is at its most tormenting,
and in the morning hours, as ones blood pressure rises to meet the day, one is most
likely to suffer a heart attack or stroke. Rheumatoid arthritis improves through the
day, but osteoarthritis grows worse. Alcohol is least toxic to the body at around
5pm: cocktail hour.
[0003] The first application of chronotherapy, in the 1960s, was a synthetic corticosteroid
tablet (Medrol, Upjohn). Clinicians found that when used in the morning, the drug
was more effective and caused fewer adverse reactions. Another example of a commercial
product employing chronotherapy is the bronchodilator, Uniphyl®, a long-acting theophylline
preparation manufactured by Purdue Frederick (approved by the FDA in 1989). Taken
once a day at dinner to control night-time asthma symptoms. Uniphyl
® causes theophylline blood levels to reach their peak and improve lung function during
the difficult morning hours.
[0004] Oral controlled release delivery systems may also be capable of passing over the
entire tract of the small intestine, including the duodenum, jejunum, and ileum, so
that the active ingredients can be released directly in the colon, if such site specific
delivery is desired. One means of accomplishing this is by providing a coating surrounding
the active pharmaceutical formulation core so as to preserve the integrity of the
formulation while it is passing through the gastric tract. The high acidity of the
gastric tract and presence of proteolytic and other enzymes therein generates a highly
digestive environment that readily disintegrates pharmaceutical formulations that
do not possess some type of gastro-resistance protection. This disintegration would
typically have a detrimental effect upon the sustained release of the active agent.
Such coated pharmaceutical formulations, in addition to slowing the release rate of
the active agent contained within the core of the tablet, can also effectuate a delay
in the release of the active ingredient for a desired period of time such that the
dissolution of the active drug core can be delayed. Examples of coated pharmaceutical
delivery systems for delayed release can be found in
U.S. Patents Nos. 4,863,742 (Panoz et al.) and
5,891,474 (Busetti et al.), as well as in European Patent Applications Nos.
366 621,
572 942 and
629 398. In the delayed release tablets described in each of these references, the therapeutically
active drug core is coated with at least one and potentially several layers of coating,
wherein the layers of coating have a direct effect upon the timed release of the active
drug within the tablet core into the system of the patient.
[0005] EP 519 099 A1 is purportedly directed to a stable, directly compressible pharmaceutical composition
comprising cyclophosphamide and a partially or fully pregelatinized starch.
[0006] US 4,933.186 B1 is purportedly directed to a dihydropyridine formulation with a rapid release core
and a delayed release compression coating.
[0007] EP 526 862 A1 is purportedly directed to a pharmaceutical composition which contains high density
organics, bioadhesives, an active agent and ether materials.
[0008] It is considered desirable by those skilled in the art to provide an oral controlled
release delivery system that is adaptable to deliver a drug(s) such that release rates
and drug plasma profiles can be matched to physiological and chronotherapeutic requirements.
[0009] It is an object of the present invention to provide an oral pharmaceutical dosage
form that releases a drug(s) into the body of a patient at a predetermined time after
oral ingestion of the dosage form by the patient.
[0010] It is a further object of the present invention to provide an oral pharmaceutical
dosage form that provides a delayed release of a drug(s) into the gastrointestinal
tract of a patient at a predetermined time after oral ingestion of the dosage form.
[0011] It is a further object of certain embodiments of the present invention to provide
an oral pharmaceutical dosage form having a core containing drug, the core being compression
coated with a coating that provides a delayed release of the drug from the dosage
form after the dosage form is orally administered to a patient.
[0012] It is a further object of certain embodiments of the present invention to provide
an oral pharmaceutical dosage form having a drug-containing core that is compression
coated with a coating which provides a delayed release of the drug when the dosage
form is orally administered to a patient.
[0013] It is a further object of certain embodiments of the present invention to provide
a dosage form which allows time-specific dosing for a wide variety of diseases.
[0014] It is a further object of certain embodiments of the present invention to provide
a dosage form which allows time-specific dosing for diseases such as arthritis, high
blood pressure, or asthma which are typically more symptomatic in the early morning
corresponding to circadian rhythms.
[0015] It is a further object of certain embodiments of the present invention to provide
a dosage form which provides a delayed release of drug from the dosage form, followed
by a sustained release of the drug thereafter as the dosage form travels through the
gastrointestinal tract.
[0016] It is a further object of certain embodiments of the present invention to provide
a compression coated dosage form having an immediate release layer of a drug(s) overcoating
a compression coated core which provides a delayed release of the same or different
drug(s) from the dosage form; the core optionally providing a sustained release of
the drug thereafter as the dosage form travels through the gastrointestinal tract.
[0017] It is a further object of certain embodiments of the present invention to provide
an oral dosage form which provides site-specific delivery of drug (e.g., to the colon).
[0018] It is a further object of certain embodiments of the present invention to develop
an oral dosage form which provides programmed release of drug.
[0019] It is a further object of certain embodiments of the present invention to develop
an oral dosage form which provides pulsatile release of drug.
[0020] Subject of the invention is a delayed release oral solid dosage form, comprising
a core comprising a therapeutically effective amount of a drug, and a delayed release
material compression coated onto said core, said delayed release material comprising
a heteropolysaccharide gum and a homopolysaccharide gum, said compression coating
delaying the release of said drug from said dosage form until after a period of time
from 2 to 18 hours after exposure of the dosage form to an aqueous solution.
[0021] In certain preferred embodiments, the compression coating comprises a mixture (e.g.,
matrix) of xanthan gum, locust bean gum, and a pharmaceutically acceptable saccharide,
e.g., a monosaccharide, a disaccharide, a polyhydric alcohol, or a combination of
any of the foregoing. In certain preferred embodiments, the core is an immediate release
core comprising the drug together with one or more pharmaceutically acceptable excipients.
[0022] The invention is further directed in part to a delayed release oral solid dosage
form comprising a core comprising a therapeutically effective amount of a drug(s),
and an agglomerated delayed release material compression coated onto the core, the
agglomerated delayed release material comprising a gum selected from, e.g., a homopolysaccharide,
a heteropolysaccharide, and a mixture of a homopolysaccharide and a heteropolysaccharide,
together with a pharmaceutically acceptable excipient, the compression coating delaying
the release of the drug from the dosage form for a predetermined period of time after
exposure of the dosage form to an aqueous solution.
[0023] The invention is further directed in part to a delayed release oral solid dosage
form comprising a core comprising a therapeutically effective amount of a drug(s)
and a disintegrant, and a delayed release material compression coated onto the core,
said delayed release material comprising one or more natural or synthetic gums, said
compression coating delaying the release of the drug from the dosage form for a predetermined
period of time after exposure of the dosage form to an aqueous solution, the disintegrant
being included in the core in an amount effective to cause the release of at least
50 percent of the drug into said aqueous solution within one hour after said predetermined
period of time.
[0024] The invention is further directed in part to a delayed release oral solid tablet,
comprising a tablet core comprising a therapeutically effective amount of a drug,
and a delayed release material compression coated onto the core, the delayed release
material comprising one or more natural or synthetic gums, the gums comprising from
6.5 percent to 83 percent of the tablet by weight, the compression coating delaying
the release of the drug from the dosage form for a period of time from 2 to 18 hours
after exposure of the dosage form to an aqueous solution.
[0025] The invention is further directed to a chronotherapeutic, delayed release oral solid
dosage form for low dose drugs, comprising a core comprising from 0.01 mg to 40 mg
of a drug(s), and a delayed release material compression coated onto the core, the
delayed release material comprising one or more natural or synthetic gums, the compression
coating comprising from 75 to 94 percent by weight of the oral solid dosage form,
and the ratio of the core to gum in the compression coating being from 1:0.37 to 1:5,
by weight, the compression coating delaying the release of the drug from the dosage
form for a period of time from 2 to 18 hours after exposure of the dosage form to
an aqueous solution.
[0026] The invention is further directed in part to a chronotherapeutic, delayed release
oral solid dosage form for a relatively high dose drug, comprising a core comprising
from 41 mg to 300 mg of a drug, and a delayed release material compression coated
onto the core, the delayed release material comprising one or more natural or synthetic
gums, the ratio of the core to gum in the compression coating being from 1:0.3 to
1:3, by weight, the total weight of the oral solid dosage form being from 500 mg to
1500 mg, the compression coating delaying the release of the drug from the dosage
form for a period of time from 2 to 18 hours after exposure of the dosage form to
an aqueous solution.
[0027] The invention is further directed in part to a method of preparing a chronotherapeutic
oral solid dosage form of a drug, comprising preparing a core comprising a therapeutically
effective amount of a drug(s) and from 5 to 20% disintegrant, by weight of the core,
preparing a granulate of a delayed release material comprising one or more natural
or synthetic gums, compression coating the granulate onto said core, the compression
coating delaying the release of the drug from the dosage form until after a period
of time from 2 to 18 hours after exposure of the dosage form to an aqueous solution.
In certain preferred embodiments, the method further comprises preparing the granulate
of delayed release material by wet granulating one or more natural or synthetic gums
together with at least one pharmaceutically acceptable excipient, and drying the resultant
granulate to obtain agglomerated particles of the delayed release material. In certain
embodiments the method further comprises granulating the glucocorticosteroid, the
disintegrant, and a pharmaceutically acceptable inert diluent prior to the compression
coating step.
[0028] In certain preferred embodiments, the disintegrant is a superdisintegrant incorporated
in the core in an amount effective to cause the release of at least 50 percent of
the drug(s) into the aqueous solution within one hour upon completion of the time
period for delayed release.
[0029] The invention is further directed to methods of treatment utilizing the formulations
disclosed herein.
[0030] In certain embodiments, the oral dosage form provides a lag time (delayed release
of drug) from 2 to 18 hours, after oral administration to, e.g., a human subject or
patient.
[0031] In certain preferred embodiments, the oral dosage form releases at least 50 percent
of the drug(s) contained in the core within about one hour, and preferably at least
80 percent of the drug(s) contained in the core within about one or two hours, after
the end of the lag time provided by the compression coating.
[0032] In certain embodiments, the oral dosage form of the invention provides a lag time
from 5 to 8 hours with a full release by 8 to 12 hours, after oral administration,
e.g., to a human patient.
[0033] In certain preferred embodiments, the oral dosage form provides a lag time of 6 to
7 hours with full release by 8 to 9 hours, after oral administration of the dosage
form.
[0034] In certain other preferred embodiments, the oral dosage form provides a lag time
of 6 to 7 hours, followed by full release of the drug by 7 to 8 hours after oral administration.
[0035] In yet other embodiments, the formulation provides a lag time from 9 to 12 hours,
with full release by 11 to 13 hours after oral administration, preferably a lag time
of 10 to 11 hours followed by full release at 11 to 12 hours after oral administration
of the dosage form.
[0036] In yet other embodiments, the formulation provides a lag time of, e.g., 3 to 12 hours,
with full release of the drug from the dosage form within about 24 hours, or (alternatively)
after 24 hours.
[0037] By "delayed release" it is meant for purposes of the present invention that the release
of the drug is delayed and the drug contained in the dosage form is not substantially
released from the formulation until after a certain period of time, e.g., such that
the drug is not released into the bloodstream of the patient immediately upon ingestion
by the patient of the tablet but rather only after a specific period of time, e.g.,
a 4 hour to a 9 hour delay. For purposes of the present invention, delayed release
is synonymous with "timed delay" or a release of drug after a lag time, or a programmed
release.
[0038] By "sustained release" it is meant for purposes of the present invention that, once
the drug is released from the formulation, it is released at a controlled rate such
that therapeutically beneficial blood levels (but below toxic levels) of the medicament
are maintained over an extended period of time from the start of drug release, e.g.,
providing a release over a time period, e.g., from 4 to 24 hours from the point of
drug release after the lag time, onward.
[0039] The term "environmental fluid" is meant for purposes of the present invention to
encompass, e.g., an aqueous solution (e.g., an in-vitro dissolution bath) or gastrointestinal
fluid.
[0040] The term USP apparatus type III used herein is described e.g., in the United States
Pharmacopeia XXV (2002).
DETAILED DESCRIPTION OF THE INVENTION
[0041] The present invention may be employed to achieve the time-delayed release of a pharmaceutically
active agent and in certain embodiments to provide a controlled-release pharmaceutical
formulation for pharmaceutically active agents that are desirously delivered over
a predetermined period of time. The formulations of the present invention provide
the time-delayed release of a pharmaceutically active agent and may be useful for
the treatment of conditions that are desirously treated through time-delayed pharmaceutical
agent delivery mechanisms. For example, the formulations of the present invention
are useful for the treatment of morning pathologies, i.e., conditions, diseases or
other illnesses, such as arthritis, hypertension and asthma, the symptoms of which
are generally more acute in the morning as the patient awakens from sleep. These conditions
may be treated by administering the time-delayed release formulation according to
the present invention to the patient prior to sleeping, such that the delivery of
the pharmaceutically active agent is achieved at about the time the patient awakens,
or preferably the pharmaceutically active agent has been delivered from the dosage
form (and absorbed from the gastrointestinal tract) to an extent that it has achieved
a therapeutic effect, thereby alleviating the symptoms of the morning pathology.
[0042] The formulations of the present invention comprise a core comprising an active agent
and a compression coating over the core that comprises one or more natural or synthetic
pharmaceutically acceptable gums. In certain especially preferred embodiments, the
compression coating comprises a combination of a heteropolysaccharide gum (e.g., xanthan
gum) and a homopolysaccharide gum (e.g., locust bean gum), together with a pharmaceutically
acceptable saccharide (e.g., lactose, dextrose, mannitol, etc.). In certain preferred
embodiments, the gum(s) are wet granulated together with the optional saccharide(s)
to form agglomerated particles comprising a mixture of, e.g., xanthan gum, locust
bean gum and dextrose.
[0043] The goal of the compression coating of the present invention is to delay the release
of the active agent, for a predetermined period of time, referred to in the art as
a "lag time." In certain embodiments, the release of the active agent is delayed for,
or has a lag time of, 2 to 18 hours after administration of the dosage form.
[0044] The core comprising the active agent can be formulated for either immediate release
or sustained release of the active agent. Formulations for both immediate release
and sustained release of active agents are well known to those skilled in the art.
[0045] In the present invention, when the core comprising the active agent is formulated
for immediate release, the core can be prepared by any suitable tableting technique
known to those skilled in the art. For example, the pharmaceutically active agent
may be admixed with excipient(s) and formed into a tablet core using a conventional
tableting press or using conventional wet granulation techniques. According certain
preferred embodiments of the present invention, ingredients for the core are dry blended
in a V-blender and compressed on a rotary tablet press into tablet cores. Alternatively,
in certain embodiments, the ingredients for the core can be wet granulated, dried
and thereafter compressed into tablet cores. Preferably, the core should be compressed
to a degree of hardness such that they do not chip or come apart during further processing,
such as during the coating process. In certain embodiments, the cores can be compressed
to 50 mg weight and 2 to 8, preferably 4 to 8, most preferably 4-5 kP hardness. In
addition, tablet core size should range from ⅛ inch to ⅝ inch, preferably from ⅛ inch
to ½ inch, more preferably from 3/16 inch to ¼ inch.
[0046] In certain embodiments, wherein the core is manufactured without a wet granulation
step, and the final mixture is to be compressed into a tablet core, all or part of
the excipient in the core may comprise a pre-manufactured direct compression diluent.
Examples of such pre-manufactured direct compression diluents include Emcocel
® (microcrystalline cellulose, N.F.), Emdex
® (dextrates, N.F.), and Tab-Fini
® (a number of direct-compression sugars including sucrose, fructose and dextrose),
all of which are commercially available from Penwest Pharmaceuticals Co., Patterson,
New York). Other direct compression diluents include anhydrous lactose (Lactose N.F.,
anhydrous direct tableting) from Sheffield Chemical, Union, N.J. 07083; Elcems
® G-250 (powdered cellulose), N.F.) from Degussa, D-600 Frankfurt (Main) Germany; Fast-Flo
Lactose
® (Lactose, N.F., spray dried) from Foremost Whey Products, Banaboo, WI 53913; Maltrin
® (Agglomerated maltodextrin) from Grain Processing Corp., Muscatine, IA 52761; Neosorb
60
® (Sorbitol, N.F., direct-compression from Roquet Corp., 645 5th Ave., New York, N.Y.
10022; Nu-Tab
® (Compressible sugar, N.F.) from Ingredient Technology, Inc., Pennsauken, N.J. 08110;
Polyplasdone XL
® (Crospovidone, N.F., cross-linked polyvinylpyrrolidone) from GAF Corp., New York,
N.Y. 10020; Primojel
® (Sodium starch glycolate, N.F., carboxymethyl starch) from Generichem Corp., Little
Falls, N.J. 07424; Solka Floc
® (Cellulose floc) from Penwest Pharmaceuticals Co., Patterson, N.Y. 10512; Spray-dried
lactose
® (Lactose N.F., spray dried) from Foremost Whey Products, Baraboo, WI 53913 and DMV
Corp., Vehgel, Holland; and Sta-Rx 1500
® (Starch 1500) (Pregelatinized starch, N.F., compressible) from Colorcon, Inc., West
Point, PA 19486. In certain embodiments of the present invention, the directly compressible
inert diluent which is used in the core of the present invention is an augmented microcrystalline
cellulose as disclosed in
U.S. Patent No 5,585,115, issued December 17, 1996, and entitled "PHARMACEUTICAL EXCIPIENT HAVING IMPROVED COMPRESSIBILITY", hereby
incorporated by reference in its entirety. The augmented microcrystalline cellulose
described therein is commercially available under the tradename Prosolv® from Penwest
Pharmaceuticals Co. PROSOLV SMCC 50 is a silicified microcrystalline cellulose. This
particular grade has a median particle size (by sieve analysis) in the region of 50
µm. PROSOLV SMCC 90 is a silicified microcrystalline cellulose. This grade has a median
particle size (by sieve analysis) in the region of 90 µm.
[0047] Alternatively, in certain embodiments, the core comprising the active agent can be
formulated as a sustained release core for the sustained release of the active agent.
When the core comprising the active agent is formulated for sustained release, the
core can be prepared in a number of ways known in the art. For example, the active
agent can be incorporated in a sustained release matrix and thereafter compressed
into a core, or a sustained release material can be coated onto the immediate release
core to provide for the sustained release of the active agent, or a combination of
the compressed sustained release matrix and sustained release coating on the core
can be used. Additionally, spheroids comprising the active agent, or multiparticulates
with sustained release coatings and comprising the active agent, may be compressed
with optional binders and other excipients into a sustained release core.
[0048] When the core of the present invention comprises a sustained release matrix, the
matrix formulations are generally prepared using standard techniques well known in
the art. Typically, they are prepared by dry blending a sustained release material,
diluent, active agent, and optional other excipients followed by granulating the mixture
until proper granulation is obtained. The granulation is done by methods known in
the art. Typically with a wet granulation, the wet granules are dried in a fluid bed
dryer, sifted and ground to appropriate size. Lubricating agents are mixed with the
dried granulation to obtain the final core formulation.
[0049] In our
U.S. Patent Nos. 4,994,276;
5,128,143;
5,135,757;
5,455,046;
5,512,297;
5,554,387;
5,667,801;
5,846,563;
5,773,025;
6,048,548;
5,662,933;
5,958,456;
5,472,711;
5,670,168; and
6,039,980, all of which are hereby incorporated by reference, we reported that a controlled
release excipient that is comprised of a gelling agent such as synergistic heterodisperse
polysaccharides (e.g., a heteropolysaccharide such as xanthan gum) preferably in combination
with a polysaccharide gum capable of cross-linking with the heteropolysaccharide (e.g.,
locust bean gum) is capable of processing into oral solid dosage forms using either
direct compression, following addition of drug and lubricant powder, conventional
wet granulation, or a combination of the two. These systems (controlled release excipients)
are commercially available under the trade name TIMERx
® from Penwest Pharmaceuticals Co., Patterson, N.Y., which is the assignee of the present
invention.
[0050] In certain embodiments of the present invention, wherein the core provides for the
sustained release of the active agent, the core comprises a sustained release matrix
such as those disclosed in our foregoing patents. For example, in certain embodiments
of the present invention, in addition to the active agent, the core comprises a sustained
release excipient comprising a gelling agent comprising a heteropolysaccharide gum
and a homopolysaccharide gum capable of cross-linking said heteropolysaccharide gum
when exposed to an environmental fluid, and an inert pharmaceutical diluent. Preferably,
the ratio of the heteropolysaccharide gum to the homopolysaccharide gum is from 1:3
to 3:1, and the ratio of active agent to gelling agent is preferably from 1:3 to 1:8.
The resulting core preferably provides a therapeutically effective blood level of
the active agent for at least about 4 hours, and in certain preferred embodiments,
for 24 hours. In certain preferred embodiments, the sustained release excipient further
comprises an effective amount of a pharmaceutically acceptable ionizable gel strength
enhancing agent, such as those described hereinafter, to provide a sustained release
of the active when the core is exposed to an environmental fluid. The sustained release
excipient (with or without the optional ionizable gel strength enhancing agent) may
be further modified by incorporation of a hydrophobic material which slows the hydration
of the gums without disrupting the hydrophilic matrix. In addition, in certain embodiments,
the sustained release excipient can be modified to provide for bi- or multi-phasic
release profiles of the active agent by the inclusion of a pharmaceutically acceptable
surfactant or wetting agent in the core. Alternatively, the sustained release-excipient
comprises only one of the aforementioned gums. In yet other embodiments, the sustained
release excipient comprises a different pharmaceutically acceptable gum.
[0051] In addition to the above, other sustained release materials may be used for the sustained
release matrix cores of the inventive formulations. A nonlimiting list of suitable
sustained-release materials which may be included in a sustained-release matrix according
to the present invention include hydrophilic and/or hydrophobic materials, such as
sustained release polymers gums, acrylic resins, protein derived materials, waxes,
shellac, and oils such as hydrogenated castor oil, hydrogenated vegetable oil. Preferred
sustained-release polymers include alkylcelluloses such as ethylcellulose, acrylic
and methacrylic acid polymers and copolymers; and cellulose ethers, especially hydroxyalkylcelluloses
(especially hydroxypropylmethylcellulose) and carboxyalkylcelluloses. Preferred waxes
include for example natural and synthetic waxes, fatty acids, fatty alcohols, and
mixtures of the same (e.g., beeswax, carnauba wax, stearic acid and stearyl alcohol).
Certain embodiments utilize mixtures of any of the foregoing sustained release materials
in the matrix of the core. However, any pharmaceutically acceptable hydrophobic or
hydrophilic sustained-release material which is capable of imparting sustained-release
of the active agent may be used in accordance with the present invention.
[0052] Alternatively, in certain embodiments of the present invention, the core may be formulated
to provide for the sustained release of the active agent through the use of an immediate
release core (as previously described) with a sufficient amount of a hydrophobic coating
to provide for the sustained release of the active agent from the immediate release
core. The hydrophobic coating may be applied to the core using methods and techniques
known to those skilled in the art. Examples of suitable coating devices include fluid
bed coaters, pan coaters, etc. Examples of hydrophobic materials which may be used
in such hydrophobic coatings include for example, alkylcelluloses (e.g., ethylcellulose),
copolymers of acrylic and methacrylic acid esters, waxes, shellac, zein, hydrogenated
vegetable oil, mixtures thereof, and the like.
[0053] Additionally, the cores may be formulated for sustained release of the active agent
by using a combination of the sustained release matrix and sustained release coating.
The sustained release cores (e.g, sustained release matrix, sustained release coated,
or combination thereof), and the immediate release cores, may also contain suitable
quantities of additional excipients, e.g., lubricants, binders, granulating aids,
diluents, colorants, flavorants and glidants which are conventional in the pharmaceutical
art.
[0055] In certain preferred embodiments, the oral dosage form includes one or more disintegrants
preferably incorporated in the core. When such an agent is included in the core, the
rate of release of drug (after the initial delay caused by the compression coating)
is an immediate pulse effect. In certain embodiments, when no disintegrant is present,
a controlled profile may be produced. Suitable disintegrants are known to those skilled
in the art, and include for example sodium starch glycolate (commercially available
as Explotab® from Penwest Pharmaceuticals Co.).
[0056] The mechanism of disintegration is based on swelling, wicking, and deformation of
the disintegrants. When a compressed tablet is placed in aqueous solution, water can
be quickly absorbed, and the swelling of the disintegrant breaks apart tablets quickly.
In one embodiment in which the therapeutic active drug is formulated for immediate
release, when a disintegrant is present in the core of the tablet, the rate of release
of the active agent is an immediate pulse effect. In certain embodiments in which
the therapeutic active drug is formulated for immediate release, when no disintegrant
is present, a controlled profile may be produced.
[0057] Examples of such disintegrants for use in the present invention include, for example,
starch, veegum, crospovidone, cellulose, kaolin, microcrystalline cellulose (e.g.,
Avicel PH101 & PH102), crosslinked polyvinyl pyrrolidone (e.g., Kollidon CL), and
mixtures thereof. In certain preferred embodiments, the disintegrant is a superdisintegrant,
such as, for example, croscarmellose sodium, crospovidone, crosslinked carboxy methyl
cellulose, sodium starch glycolate, and mixtures thereof. Superdisintegrants can be
incorporated at lower levels than regular disintegrants to increase the water content.
Some brand named superdisintegrants for use in the present invention include, Ac-Di-Sol
®, Primojel
®, Explotab
®, and Crospovidone
®.
[0058] In certain embodiments, the core of the present invention includes a wicking agent
in addition to or as an alternative to a disintegrant. Wicking agents such as those
materials already mentioned as disintegrants (e.g. microcrystalline cellulose) may
be included if necessary to enhance the speed of water uptake. Other materials suitable
for acting as wicking agents include, but are not limited to, colloidal silicon dioxide,
kaolin, titanium dioxide, fumed silicon dioxide, alumina, niacinamide, sodium lauryl
sulfate, low molecular weight polyvinyl pyrrolidone, m-pyrol, bentonite, magnesium
aluminum silicate, polyester, polyethylene, mixtures thereof, and the like.
[0059] In certain embodiments, the one or more disintegrant(s) in the core is included in
an amount from 5 to 20 percent, preferably from 6 to 10 percent, most preferably 8
percent by weight of the core. In terms of whole tablet weight (e.g., core plus compression
coating), the one or more disintegrant(s) in the core are included in an amount from
0.1 to 5 percent, preferably from 0.3 to 2 percent, by weight of the tablet (entire
formulation).
[0060] According to the present invention, the core containing active drug is completely
surrounded or substantially surrounded by a compression coating. The compression coating
preferably delays the release of the pharmaceutically active agent for a predetermined
period of time, which time is dependent upon the formulation of the coating and the
thickness of the coating layer. The appropriate time period for the release of the
active ingredient can be determined prior to the preparation of the formulation, and
the formulation can be designed by applying the appropriate thickness and composition
of the coating to achieve the desired time delay prior to release of the active ingredient
and the desired release rate of the active ingredient following the time delay.
[0061] Preferably, the compression coating comprises a natural or synthetic gum which can
function as a gelling agent, causing the core to be surrounded by the gel when the
compression coated tablet is exposed to an environmental fluid (e.g., water or gastrointestinal
fluid) and thereby causing the drug to be released after diffusion of the environmental
fluid through the compression coating, the dissolution of the drug into the environmental
fluid, and the egress of the dissolved drug into the fluid surrounding the compression
coated tablet.
[0062] In certain embodiments, gums for use in the compression coating include, for example
and without limitation, heteropolysaccharides such as xanthan gum(s), homopolysaccharides
such as locust bean gum, galactans, mannans, vegetable gums such as alginates, gum
karaya, pectin, agar, tragacanth, accacia, carrageenan, tragacanth, chitosan, agar,
alginic acid, other polysaccharide gums (e.g. hydrocolloids), and mixtures of any
of the foregoing. Further examples of specific gums which may be useful in the compression
coatings of the invention include but are not limited to acacia catechu, salai guggal,
indian bodellum, copaiba gum, asafetida, cambi gum, Enterolobium cyclocarpum, mastic
gum, benzoin gum, sandarac, gambier gum, butea frondosa (Flame of Forest Gum), myrrh,
konjak mannan, guar gum, welan gum, gellan gum, tara gum, locust bean gum, carageenan
gum, glucomannan, galactan gum, sodium alginate, tragacanth, chitosan, xanthan gum,
deacetylated xanthan gum, pectin, sodium polypectate, gluten, karaya gum, tamarind
gum, ghatti gum, Accaroid/Yacca/Red gum, dammar gum, juniper gum, ester gum, ipil-ipil
seed gum, gum talha (acacia seyal), and cultured plant cell gums including those of
the plants of the genera: acacia, actinidia, aptenia, carbobrotus, chickorium, cucumis,
glycine, hibiscus, hordeum, letuca, lycopersicon, malus, medicago, mesembryanthemum,
oryza, panicum, phalaris, phleum, poliathus, polycarbophil, sida, solanum, trifolium,
trigonella, Afzelia africana seed gum, Treculia africana gum, detarium gum, cassia
gum, carob gum, Prosopis africana gum, Colocassia esulenta gum, Hakea gibbosa gum,
khaya gum, scleroglucan, zea, mixtures of any of the foregoing, and the like.
[0063] In certain especially preferred embodiments, the compression coating comprises a
heteropolysaccharide such as xanthan gum, a homopolysaccharide such as locust bean
gum, or a mixture of one or more hetero- and one or more homopolysaccharide(s). Heterodisperse
excipients, previously disclosed as a sustained release tablet matrix in our
U.S. Patents Nos. 4,994,276,
5,128,143, and
5,135,757, may be utilized in the compression coatings of the present invention. For example,
in certain embodiments of the present invention, a gelling agent of both hetero- and
homo- polysaccharides which exhibit synergism, e.g., the combination of two or more
polysaccharide gums producing a higher viscosity and faster hydration than that which
would be expected by either of the gums alone, the resultant gel being faster-forming
and more rigid, may be used in the compression coatings of the present invention.
[0064] The term "heteropolysaccharide" as used in the present invention is defined as a
water-soluble polysaccharide containing two or more kinds of sugar units, the heteropoly-saccharide
having a branched or helical configuration, and having excellent water-wicking properties
and immense thickening properties.
[0065] An especially preferred heteropolysaccharide is xanthan gum, which is a high molecular
weight (>10
6) heteropolysaccharide. Other preferred heteropolysaccharides include derivatives
of xanthan gum, such as deacylated xanthan gum, the carboxymethyl ether, and the propylene
glycol ester.
[0066] The homopolysaccharide materials used in the present invention that are capable of
cross-linking with the heteropolysaccharide include the galactomannans, i.e., polysaccharides
that are composed solely of mannose and galactose. A possible mechanism for the interaction
between the galactomannan and the heteropolysaccharide involves the interaction between
the helical regions of the heteropolysaccharide and the unsubstituted mannose regions
of the galactomannan. Galactomannans that have higher proportions of unsubstituted
mannose regions have been found to achieve more interaction with the heteropolysaccharide.
Hence, locust bean gum, which has a higher ratio of mannose to galactose, is especially
preferred as compared to other galactomannans, such as guar and hydroxypropyl guar.
[0067] In certain preferred embodiments, the heteropolysaccharide comprises from 1 to 50
percent and the homopolysaccharide material comprises from 50 to 1 percent by weight
of the compression coating. In certain preferred embodiments, the ratio of heteropolysaccharide
to homopolysaccharide material is from 1:3 to 3:1, preferably from 2:3 to 3:2, or
1:1.
[0068] In a certain preferred embodiment, the compression coating comprises from 5 to 70
percent or more by weight of a hydrophilic material (e.g., gums). In certain preferred
embodiments of the present invention, the higher the percentage of gums in the compression
coating, the longer the delay of the release or "lag time" of the active agent.
[0069] In certain embodiments, the percent of gums in the compression coating corresponds
to a delayed release of the active agent which is independent of pH. For example,
in certain preferred embodiments, when the compression coating is less than 25% gums,
preferably comprising 5 to 15% gums, the delayed release is more independent of pH
than a compression coating comprising greater than 25% gums (e.g., 30, 40, or 50%
gums).
[0070] In certain preferred embodiments, the compression coating also includes pharmaceutically
acceptable excipients, for example, a saccharide such as a monosaccharide, a disaccharide
or a polyhydric alcohol, and/or mixtures of any of the foregoing, or microcrystalline
cellulose or a starch. Examples of suitable such excipients include sucrose, dextrose,
lactose, fructose, xylitol, sorbitol, Mannitol, starches, mixtures thereof and the
like. In certain embodiments, it is preferred that a soluble pharmaceutical excipient
such as lactose, dextrose, sucrose, mannitol, or mixtures thereof is included in the
materials to be used in the compression coating. In certain preferred embodiments,
the gum(s) is wet granulated with the pharmaceutically acceptable excipient prior
to its use as a compression coating on the surface of the inner cores of the invention.
The compression coating may comprise, e.g., up to 95% pharmaceutically acceptable
excipient(s), by weight.
[0071] In certain embodiments, the amount of gum(s) contained in the compression coating
is from 1 percent to 90 percent by weight, preferably from 6.5 percent to 83 percent
of the total tablet, by weight.
[0072] In certain embodiments, it is possible to dry mix the ingredients of the compression
(delayed release) coating without utilizing a wet granulation step. If the mixture
is to be manufactured without a wet granulation step, and the final mixture is to
be compression coated onto a pre-formed tablet core, it is preferred that all or part
of the pharmaceutically acceptable excipient(s) should impart sufficient compressibility
to provide a pharmaceutically acceptable product. The properties and characteristics
of a specific excipient system prepared according to the present invention may be
dependent in part on the individual characteristics, e.g., of the homo- and heteropolysaccharide
constituents, in terms of polymer solubility, glass transition temperatures etc.,
as well as on the synergism both between different homo- and heteropolysaccharides
and between the homo- and heteropolysaccharides and the inert saccharide constituent(s)
in modifying dissolution fluid-excipient interactions.
[0073] In certain embodiments of the invention where the compression coating comprises a
heteropolysaccharide, a homopolysaccharide, or both, a release-modifying agent as
described in our previous patents directed to the use of these materials in sustained
release matrices can also be utilized in the compression coating. Such release-modifying
agents and pre-manufactured excipients disclosed in our
U.S. Patent Nos. 5,455,046;
5,512,297;
5,554,387;
5,667,801;
5,846,563;
5,773,025;
6,048,548;
5,662,933;
5,958,456;
5,472,711;
5,670,168; and
6,039,980 may be utilized in the compression coatings of the present invention.
[0074] Thus, for example, the release-modifying agent may comprise an ionizable gel-strength
enhancing agent. The ionizable gel strength-enhancing agent that is optionally used
in conjunction with the present invention may be monovalent or multivalent metal cations.
The preferred salts are the inorganic salts, including various alkali metal and/or
alkaline earth metal sulfates, chlorides, borates, bromides, citrates, acetates, lactates,
etc. Specific examples of suitable ionizable gel strength enhancing agent include
calcium sulfate, sodium chloride, potassium sulfate, sodium carbonate, lithium chloride,
tripotassium phosphate, sodium borate, potassium bromide, potassium fluoride, sodium
bicarbonate, calcium chloride, magnesium chloride, sodium citrate, sodium acetate,
calcium lactate, magnesium sulfate and sodium fluoride. Multivalent metal cations
may also be utilized. However, the preferred ionizable gel strength-enhancing agents
are bivalent. Particularly preferred salts are calcium sulfate and sodium chloride.
The ionizable gel strength enhancing agents of the present invention are added in
an amount effective to obtain a desirable increased gel strength due to the cross-linking
of the gelling agent (e.g., the heteropolysaccharide and homopolysaccharide gums).
In alternate embodiments, the ionizable gel strength-enhancing agent is included in
the delayed release excipient of the present invention in an amount from 1 to 20%
by weight of the delayed release excipient, and in an amount 0.5% to 16% by weight
of the final dosage form. In certain embodiments, the inclusion of an ionizable gel
strength-enhancing agent not only delays the release of the active, but also provides
for a sustained release of the active agent.
[0075] In certain embodiments of the present invention, the (delayed release) compression
coating coated onto the core comprises from 1 to 90 percent by weight of a gelling
agent comprising a heteropolysaccharide gum and a homopolysaccharide gum, from 0 to
20 percent by weight of an ionizable gel strength enhancing agent, and from 10 to
95 percent by weight of an pharmaceutically acceptable excipient. In other embodiments,
the compression coating material comprises from 5 to 75 percent gelling agent (gum),
from 0 to 15 percent ionizable gel strength enhancing agent, and from 30 to 95 percent
pharmaceutically acceptable excipient (e.g., an inert diluent). In yet other embodiments,
the compression coating material comprises from 7.5 to 50 percent gelling agent, from
0 to 10 percent ionizable gel strength enhancing agent, and from 30 to 95 percent
pharmaceutically acceptable excipient.
[0076] Surfactants that may be used in the present invention generally include pharmaceutically
acceptable anionic surfactants, cationic surfactants, amphoteric (amphipathic/ amphophilic)
surfactants, and non-ionic surfactants. Suitable pharmaceutically acceptable anionic
surfactants include, for example, monovalent alkyl carboxylates, acyl lactylates,
alkyl ether carboxylates, N-acyl sarcosinates, polyvalent alkyl carbonates, N-acyl
glutamates, fatty acid-polypeptide condensates, sulfuric acid esters, alkyl sulfates
(including sodium lauryl sulfate (SLS)), ethoxylated alkyl sulfates, ester linked
sulfonates (including docusate sodium or dioctyl sodium succinate (DSS)), alpha olefin
sulfonates, and phosphated ethoxylated alcohols.
[0077] Suitable pharmaceutically acceptable cationic surfactants include, for example, monoalkyl
quaternary ammonium salts, dialkyl quaternary ammonium compounds, amidoamines, and
aminimides.
[0078] Suitable pharmaceutically acceptable amphoteric (amphipathic/amphophitic) surfactants,
include, for example, N-substituted alkyl amides, N-alkyl betaines, sulfobetaines,
and N-alkyl ?-aminoproprionates.
[0079] Other suitable surfactants for use in conjunction with the present invention include
polyethyleneglycols as esters or ethers. Examples include polyethoxylated castor oil,
polyethoxylated hydrogenated castor oil, or polyethoxylated fatty acid from castor
oil or polyethoxylated fatty acid from hydrogenated castor oil. Commercially available
surfactants that can be used are known under trade names Cremophor, Myrj, Polyoxyl
40 stearate, Emerest 2675, Lipal 395 and PEG 3350.
[0080] Other release-modifying pharmaceutically acceptable agents that may be added in appropriate
quantities for their particular ability to modify dissolution rates include, for example:
stearic acid, metallic stearates, stearyl alcohol, hydrogenated cotton seed oil, sodium
chloride and certain disintegrants that are described below.
[0081] The quantity of such release-modifying agent employed depends on the release characteristics
required and the nature of the agent. For a delayed release formulation according
to the invention, the level of release-modifying agents used may be from 0.1 to 25%,
preferably from 0.5 to 10% by weight of the total composition.
[0082] In certain other embodiments of the invention, the compression coating includes a
pH-modifying agent. The pH-modifying agent may be present in the compression coating
from 1 % to 10% by weight of the final dosage form. In preferred embodiments, the
pH-modifying agent is an organic acid such as citric acid, succinic acid, fumaric
acid, malic acid, maleic acid, glutaric acid or lactic acid.
[0083] In certain preferred embodiments, the release of drug occurs when aqueous environmental
fluid (e.g., water or gastrointestinal fluid, etc. surrounding the dosage form) diffuses
through the compression coating of the dosage form, resulting in hydration of the
core and dissolving the drug, which then can pass into the fluid surrounding the core.
[0084] In certain preferred embodiments, the delayed release of the drug (lag time) is varied
by increasing the thickness of the compression coating (increased lag time) or by
decreasing the thickness of the compressing coating (decreased lag time). The delayed
release may also be varied, e.g., by changing the gum(s) included in the delayed release
compression coating, selecting a particular combination of gums, by including or not
including a pharmaceutically acceptable excipient, such as a saccharide (including
polysaccharides) or a combination of saccharide(s) (or polysaccharides) in the compression
coating, by changing or by adding additional agents to the compression coating which
cause the compression coating to further delay the diffusion of water (or gastrointestinal
fluid) through the compression coating (e.g., matrix) into the inner core (thereby
allowing hydration of the inner core). In addition, the compression force used to
apply the compression coating may be used to alter the release rate of the active
ingredient. Also, release can be modified via the use of an extragranular excipient
addition to the compression coating. Such ingredients may comprise, for example, microcrystalline
cellulose, polyvinylpyrrolidone, polyethylene glycol, and the like.
[0085] The delayed release of the drug may further be varied by utilizing a further coating
(i) between the core and the compression coating; (ii) over the compression coating;
or (iii) both between the core and the compression coating and over the compression
coating. Such coatings may comprise, for example a hydrophilic polymer (such as hydroxypropylmethylcellulose)
and/or a hydrophobic polymer (such as an acrylic polymer, a copolymer of acrylic and
methacrylic acid esters, an alkylcellulose such as ethylcellulose, etc.). In such
circumstances, the release of drug from the dosage form may not only be occurring
as fluid diffuses through the compression coating; erosion of the further coatings
described in this paragraph may also delay the release of drug.
[0086] The dissolution rates of the present invention (with or without the optional release
modifying agents mentioned above) may be further modified by incorporation of a hydrophobic
material in the compression coating, which slows the hydration of the gums without
disrupting the hydrophilic matrix. This is accomplished in alternate embodiments of
the present invention by granulating the delayed release excipient with a solution
or dispersion of a hydrophobic material prior to the compression coating of the core.
The hydrophobic polymer may be selected from an alkylcellulose such as ethylcellulose,
other hydrophobic cellulosic materials, polymers or copolymers derived from acrylic
or methacrylic acid esters, copolymers of acrylic and methacrylic acid esters, zein,
waxes, shellac, hydrogenated vegetable oils, and any other pharmaceutically acceptable
hydrophobic material known to those skilled in the art. The solvent for the hydrophobic
material may be an aqueous or organic solvent, or mixtures thereof. The amount of
hydrophobic material incorporated into the delayed release excipient is that which
is effective to slow the hydration of the gums without disrupting the hydrophilic
matrix formed upon exposure to an environmental fluid. In certain preferred embodiments
of the present invention, the hydrophobic material is included in the compression
coating in an amount from 1 to 20 percent by weight.
[0087] The compression coating may also contain suitable quantities of, e.g., lubricants,
binders, granulating aids, diluents, colorants, flavorants and glidants which are
described hereinafter and are which are conventional in the pharmaceutical art.
[0088] In preferred embodiments where the materials to be included in the compression coating
are pre-manufactured, the combination of the gum gelling agent (e.g., a mixture of
xanthan gum and locust bean gum) with the pharmaceutical excipient(s), with or without
a release modifying agent, provides a ready-to-use compression coating product in
which a formulator need only apply the material onto the core by compression coating
to provide the desired chronotherapeutic dosage forms. The compression coating may
comprise a physical admix of the gums along with a soluble excipient such as compressible
sucrose, lactose, dextrose, etc., although it is preferred to granulate or agglomerate
the gums with a plain pharmaceutically acceptable excipient (i.e., crystalline) sucrose,
lactose, dextrose, mannitol, etc., to form a delayed release excipient for use in
the compression coating. The granulate form has certain advantages including the fact
that it can be optimized for flow and compressibility.
[0089] The gums and optional pharmaceutical excipients used in the compression coating are
preferably prepared according to any agglomeration technique to yield an acceptable
excipient product. In wet granulation techniques, the desired amounts of the hydrophilic
material (e.g., heteropolysaccharide gum and/or the homopolysaccharide gum) and the
inert diluent are mixed together and thereafter a moistening agent such as water,
propylene glycol, glycerol, alcohol or the like is added to prepare a moistened mass.
Next, the moistened mass is dried. The dried mass is then milled with conventional
equipment into granules. Thereafter, the excipient product is ready to use.
[0090] The (preferably) pre-manufactured delayed release excipient is preferably free-flowing
and directly compressible. Accordingly, the excipient may be directly compressed onto
a pre-formed inner core of a therapeutically active medicament to form coated tablets.
The delayed release coating mixture, in an amount sufficient to make a uniform coating
onto a pre-formed tablet core, is subjected to tableting in a conventional production
scale tableting machine at normal compression pressure, i.e., 2000-1600 lbs/sq in.
However, the mixture should not be compressed to such a degree that there is subsequent
difficulty in its hydration when exposed to gastric fluid.
[0091] The average particle size of the granulated delayed release excipient of the present
invention ranges from 50 microns to 400 microns and preferably from 185 microns to
265 microns. The particle size of the granulation is not narrowly critical, the important
parameter being that the average particle size of the granules must permit the formation
of a directly compressible excipient which forms a coating over pharmaceutically active
tablet cores. The desired tap and bulk densities of the granulation of the present
invention are normally between from 0.3 to 0.8 g/ml, with an average density of from
0.5 to 0.7 g/ml.
[0092] The compression coatings of the present invention preferably have uniform packing
characteristics over a range of different particle size distributions and are capable
of processing onto the pre-formed tablet core using direct compression, following
the addition of a lubricant.
[0093] In addition to being (optionally) used in the tablet core, in certain embodiments
it is preferred that one or more pharmaceutically acceptable lubricants be added to
the compression coating materials (preferably pre-agglomerated) prior to the mixture
being compression coated onto the surface of the core. Examples of suitable lubricants
for use in the core and compression coating of the invention include, for example
and without limitation, talc, stearic acid, vegetable oil, calcium stearate, zinc
stearate, magnesium stearate, etc. Preferably, an effective amount of any generally
accepted pharmaceutical lubricant, including calcium or magnesium soaps is preferably
added to the mixture of ingredients prior to compression of the mixture onto the solid
pre-formed tablet core. An especially preferred lubricant is sodium stearyl fumarate,
NF, commercially available under the trade name Pruv
® from Penwest Pharmaceuticals Co.
[0094] In certain embodiments, the present invention is further directed towards a method
of manufacturing the delayed release solid oral dosage forms (e.g., tablets) of the
present invention. In certain preferred embodiments, the steps for preparation of
a delayed release oral solid dosage form of the present invention may include the
following:
[0095] Preparation of inner core formulation:
- 1.
- (A) Wet granulate active ingredient (e.g., drug) together with optional excipients,
followed by drying and milling as necessary to obtain a granulate; or
- (B) Dry blend the active together with optional excipients using geometric dilution
as necessary to obtain a granulate;
- 2. Optionally, extragranularly add excipients to the material prepared in Step 1 with
appropriate blending;
- 3. Preferably, lubricate powder blend prepared in Step 1 or 2:
- 4. Compress core using powder blend prepared in Step 3 with an appropriate press.
- 5. Optionally, applying a functional film coating onto the tablet cores prepared in
Step 4;
[0096] Preparation of delayed release (compression) coating may be accomplished, e.g., as
follows:
6.
- (A) Wet granulate a gum(s) (e.g., a heteropolysaccharide gum and a homopolysaccharide
gum) together with optional excipients to form a delayed release material (agglomerated
particles), and then dry the delayed release material; or
- (B) Dry blend a gum(s) together with optional excipients to form a delayed release
material (granulate);
7. Preferably, mill the delayed release material prepared in Step 6;
8. Preferably, lubricate the delayed release material prepared in Step 6 or 7;
[0097] Coating of inner core:
9. Compression coat the delayed release material prepared in Steps 6-8 over the tablet
cores prepared in Step 1-5;
10. Optionally, film coat the final dosage form (if desired).
[0098] In certain embodiments, steps 4 & 10 are combined in a single unit operation when
using e.g., a Dry-Cota Press as described hereinafter. A functional coating of the
tablet cores may be possible using the Dry-Cota Press if a modification is made to
the press to add a core tablet feeder system.
[0099] A Manesty Dry-Cota press press consists of two side by side interconnected tablet
presses where the core is made on one press then mechanically transferred to the next
press for compression coating. Each "press" has an independent powder feed mechanism
so that core blend is loaded on one machine and coating blend on the other. Mechanical
transfer arms rotate between the machines to remove cores from one press and transfer
them to the coating press. Other and more modern types of presses which may be used
(e.g. Elizabeth Hata HT-AP44-MSU-C, Killian RUD, Fette PT 4090) have a dual feed system
for coating blend and pre-made cores. This configuration is more flexible, in that
cores can be pan coated with a functional or cosmetic coating before compression coating.
In addition, this allows multiple compression coating layers to be achieved by recycling
tablets that have already been compression coated. Both types of presses have mechanisms
to center the tablet within the coating both vertically and radially. One of ordinary
skill would understand that other tablet presses may be used to provide for the final
dosage forms of the present invention.
[0100] Although typically the compression coating surrounds the entire core, in certain
embodiments of the present invention, the compression coating substantially surrounds,
but does not entirely surround the tablet core. In such instances, the release of
drug from the tablet core will occur first from that portion of the inner core to
which the compression is not applied. In other embodiments of the invention, compression
coating is not applied to the same thickness around the entire inner core, thereby
creating areas of the compressed dosage form that release drug earlier (and later)
than other areas. This may be accomplished, e.g, by having the core to which the compression
coating is applied not being centered in the press.
[0101] For best results, the tablets formed from the compression coating of the core are
from 4 to 25 kP, preferably 5 to 15 kP, most preferably 8 to 9 kP hardness. In certain
preferred embodiments, for round compression coated tablets the diameter may be up
to ⅝ inch or greater, and for caplet shaped compression coated tablets the diameter
may be up to % inch or greater. The average flow of the (non-compression) coatings
prepared in accordance with the present invention is from 25 to 40 g/sec.
[0102] In certain embodiments of the present invention, the compression coated tablet may
then be further overcoated with an enteric coating material or a hydrophobic material.
Examples of suitable enteric polymers include cellulose acetate phthalate, hydroxypropyl-methylcellulose
phthalate, polyvinylacetate phthalate, methacrylic acid copolymer, shellac, hydroxypropylmethylcellulose
succinate, cellulose acetate trimellitate, and mixtures of any of the foregoing. An
example of a suitable commercially available enteric material is available under the
trade name Eudragit® L30D55.
[0103] In further embodiments, the dosage form may be coating with a hydrophilic coating
in addition to or instead of the above-mentioned enteric coating or hydrophobic coating.
An example of a suitable material that may be used for such a hydrophilic coating
is hydroxypropylmethylcellulose (e.g., Opadry
®, commercially available from Colorcon, West Point, Pennsylvania).
[0104] In still further embodiments, the optional enteric and/or hydrophobic and/or hydrophilic
coatings may be alternatively or additionally applied as an intermediate layer(s)
between the core and the compression coating.
[0105] The optional enteric and/or hydrophobic and/or hydrophilic coatings may be applied
in any pharmaceutically acceptable manner known to those skilled in the art. For example,
in one embodiment, the coating is applied via a fluidized bed or in a coating pan.
For example, the coated tablets may be dried, e.g., at 60 to 70° C for 3 to 4 hours
in a coating pan. The solvent for the hydrophobic polymer or enteric coating may be
organic, aqueous, or a mixture of an organic and an aqueous solvent. The organic solvents
may be, e.g., isopropyl alcohol, ethanol, and the like, with or without water.
[0106] In additional embodiments of the present invention, a support platform is applied
to the tablets manufactured in accordance with the present invention. Suitable support
platforms are well known to those skilled in the art. An example of suitable support
platforms is set forth, e.g., in
U.S. Patent No. 4,839,177, hereby incorporated by reference. In that patent, the support platform partially
coats the tablet, and consists of a polymeric material insoluble in aqueous liquids.
The support platform may, for example, be designed to maintain its impermeability
characteristics during the transfer of the therapeutically active medicament. The
support platform may be applied to the tablets, e.g., via compression coating onto
part of the tablet surface, by spray coating the polymeric materials comprising the
support platform onto all or part of the tablet surface, or by immersing the tablets
in a solution of the polymeric materials.
[0107] The support platform may have a thickness of, e.g., 2 mm if applied by compression,
and 10 i if applied via spray-coating or immersion-coating. Generally, in embodiments
of the invention wherein a hydrophobic polymer or enteric coating is applied to the
tablets over the delayed release coating, the tablets are coated to a weight gain
from 1 to 20%, and in certain embodiments preferably from 5% to 10%.
[0108] Materials useful in the hydrophobic coatings and support platforms of the present
invention include derivatives of acrylic acid (such as esters of acrylic acid, methacrylic
acid, and copolymers thereof) celluloses and derivatives thereof (such as ethylcellulose),
polyvinylalcohols, and the like.
[0109] As mentioned above, the cores and/or compression coatings may also contain suitable
quantities of, e.g., lubricants, binders, granulating aids, diluents, colorants, flavorants
and glidants which are conventional in the pharmaceutical art.
[0110] Examples of suitable binders for use in the present invention include for example
and without limitation, povidone, polyvinylpyrrolidone, xanthan gum, cellulose gums
such as carboxymethylcellulose, methyl cellulose, hydroxypropylmethylcellulose, hydroxycellulose,
gelatin, starch, and pregelatinized starch.
[0111] Examples of suitable glidants for use in the present invention include talc, silicon
dioxide, and cornstarch.
[0112] In certain embodiments of the present invention, the tablet core includes an additional
dose of the drug (or a therapeutically effective dose of a different drug) included
in either the (optional) hydrophobic or enteric coating, or in an additional (optional)
overcoating coated on the outer surface of the tablet core (without the hydrophobic
or enteric coating) or as an additional coating layer coated on the surface of the
base coating(s) comprising the compression coating and, if applicable, hydrophobic
and/or enteric coating material. This may be desired when, for example, a loading
dose of the drug is needed to provide therapeutically effective blood levels of the
active agent when the formulation is first exposed to gastric fluid. The loading dose
of drug included in the coating layer may be, e.g., from 10% to 40% of the total amount
of drug included in the formulation.
[0113] Examples of drugs that are suitable for incorporation in the present invention include:
- antihistamines (e.g., azatadine maleate, brompheniramine maleate, carbinoxamine maleate,
chlorpheniramine maleate, dexchlorpheniramine maleate, diphenhydramine hydrochloride,
doxylamine succinate, methdilazine hydrochloride, promethazine, trimeprazine tartrate,
tripelennamine citrate, tripelennamine hydrochloride and triprolidine hydrochloride);
- antibiotics (e.g., penicillin V potassium, cloxacillin sodium, dicloxacillin sodium,
nafcillin sodium, oxacillin sodium, carbenicillin indanyl sodium, oxytetracycline
hydrochloride, tetracycline hydrochloride, clindamycin phosphate, clindamycin hydrochloride,
clindamycin palmitate HCL, lincomycin HCL, novobiocin sodium, nitrofurantoin sodium,
metronidazole hydrochloride): antituberculosis agents (e.g., isoniazid);
- cholinergic agents (e.g., ambenonium chloride, bethanecol chloride, neostigmine bromide,
pyridostigmine bromide);
- antimuscarinics (e.g., anisotropine methylbromide, clidinium bromide, dicyclomine
hydrochloride, glycopyrrolate, hexocyclium methylsulfate, homatropine methylbromide,
hyoscyamine sulfate, methantheline bromide, hyoscine hydrobromide, oxyphenonium bromide,
propantheline bromide, tridihexethyl chloride);
- sympathomimetics (e.g., bitolterol mesylate, ephedrine, ephedrine hydrochloride, ephedrine
sulphate, orciprenaline sulphate, phenylpropanolamine hydrochloride, pseudoephedrine
hydrochloride, ritodrine hydrochloride, salbutamol sulphate, terbutaline sulphate);
- sympatholytic agents (e.g., phenoxybenzamine hydrochloride); miscellaneous autonomic
drugs (e.g., nicotine);
- iron preparations (e.g., ferrous gluconate, ferrous sulphate);
- haemostatics (e.g., aminocaproic acid);
- cardiac drugs (e.g., acebutolol hydrochloride, disopyramide phosphate, flecainide
acetate, procainamide hydrochloride, propranolol hydrochloride, quinidine gluconate,
timolol maleate, tocainide hydrochloride, verapamil hydrochloride);
- antihypertensive agents (e.g., captopril, clonidine hydrochloride, hydralazine hydrochloride,
mecamylamine hydrochloride, metoprolol tartrate); vasodilators (e.g., papaverine hydrochloride);
- non-steroidal anti-inflammatory agents (e.g., choline salicylate, ibuprofen, ketoprofen,
magnesium salicylate, meclofenamate sodium, naproxen sodium, tolmetin sodium);
- opiate agonists (e.g., codeine hydrochloride, codeine phosphate, codeine sulphate,
dextromoramide tartrate, hydrocodone bitartrate, hydromorphone hydrochloride, pethidine
hydrochloride, methadone hydrochloride, morphine sulphate, morphine acetate, morphine
lactate, morphine meconate, morphine nitrate, morphine monobasic phosphate, morphine
tartrate, morphine valerate, morphine hydrobromide, morphine hydrochloride; propoxyphene
hydrochloride);
- anticonvulsants (e.g., phenobarbital sodium, phenytoin sodium, troxidone, ethosuximide,
valproate sodium);
- tranquilizers (e.g., acetophenazine maleate, chlorpromazine hydrochloride, fluphenazine
hydrochloride, prochlorperazine edisylate, promethazine hydrochloride, thioridazine
hydrochloride, trifluoroperazine hydrochloride, lithium citrate, molindone hydrochloride,
thiothixine hydrochloride);
- chemotherapeutic agents (e.g., doxorubicin, cisplatin, floxuridine, methotrexate,
combinations thereof, etc.);
- lipid lowering agents (e.g., gemfibrozil, clofibrate, HMG-CoA reductase inhibitors,
such as for example, atorvastatin, cerivastatin, fluvastatin, lovastatin, pravastatin,
simvastatin, etc.);
- H2-antagonists (e.g., cimetidine, famotidine, nizatidine, ranitidine HCl, etc.);
- anti-coagulant and anti-platelet agents (e.g., warfarin, cipyridamole, ticlopidine,
etc.);
- bronchodilators (e.g., albuterol, isoproterenol, metaproterenol, terbutaline, etc.);
- stimulants (e.g., benzamphetamine hydrochloride, dextroamphetamine sulphate, dextroamphetamine
phosphate, diethylpropion hydrochloride, fenfluramine hydrochloride, methamphetamine
hydrochloride, methylphenidate hydrochloride, phendimetrazine tartrate, phenmetrazine
hydrochloride, caffeine citrate);
- barbiturates (e.g., amylobarbital sodium, butabarbital sodium, secobarbital sodium);
- sedatives (e.g., hydroxyzine hydrochloride, methprylon); expectorants (e.g., potassium
iodide);
- antiemetics (e.g., benzaquinamide hydrochloride, metoclopropamide hydrochloride, trimethobenzamide
hydrochloride);
- gastro-intestinal drugs (e.g., ranitidine hydrochloride); heavy metal antagonists
(e.g., penicillamine, penicillamine hydrochloride);
- antithyroid agents (e.g., methimazole);
- genitourinary smooth muscle relaxants (e.g., flavoxate hydrochloride, oxybutynin hydrochloride);
- vitamins (e.g., thiamine hydrochloride, ascorbic acid);
- unclassified agents (e.g., amantadine hydrochloride, colchicine, etidronate disodium,
leucovorin calcium, methylene blue, potassium chloride, pralidoxime chloride.
- steroids, particularly glucocorticoids (e.g., prednisolone, prednisone, cortisone,
hydrocortisone, methylprednisolone, betamethasone, dexamethasone, triamcinolone).
[0114] The drugs may be in their base for, or a pharmaceutically acceptable salt or complex
may be used. The list of possible therapeutic classes and particular drugs listed
above are representative only, and are not meant to limit the scope of the invention
in any way.
[0115] The chronotherapeutic formulations of the present invention may be utilized to treat
any condition known (or which become known) to those skilled in the art which would
benefit from such therapy. These therapies include, but are not limited to allergic
rhinitis, attention deficit disorder, asthma, arthritis, cancer therapy, cardiovascular
disease, high cholesterol, hypertension, and ulcers.
[0116] With respect to allergic rhinitis, major symptoms of sneezing, runny nose and stuffy
nose are typically worse upon rising than during the middle of the activity span of
a given day. The chronotherapeutic approach of the present invention could also help
offset the sneezing, nasal congestion and runny nose and eyes that come with allergies.
For instance, hay fever symptoms peak in the morning. Some studies show taking an
antihistamine in the evening, rather than during the day, helps block symptoms before
a patient gets out of bed, rather than waiting for symptoms to begin. Thus, it would
be greatly desirable to provide a chronotherapeutic oral formulation of, for e.g.,
an antihistamine, which would be taken at a convenient time and which would have release
the dose at a time point such that the maximal effect of the dosage form is reached
in the morning.
[0117] With respect to asthma, normal lung function undergoes circadian changes and reaches
a low point in the early morning hours. This dip particularly pronounced in people
with asthma. Chronotherapy for asthma is aimed at getting maximal effect from bronchodilator
medications during the early morning hours. It has been proferred that the key to
managing asthma cases is chronotherapy, and that treatment to improve nighttime asthma
will allow for improvement of daytime manifestations of asthma. Certainly dosage and
timing are related for asthma patients, whose number has doubled since 1975 in America
alone. The majority of asthma patients suffer most at night, possibly because that
is when cortisol, the body's natural anti-inflammatory, is at its lowest level. The
most common time for an attack is 4 a.m., so the agony of the asthma itself is often
compounded by the further strain of sleeplessness. Thus, it would be greatly desirable
to provide a chronotherapeutic oral formulation of, e.g., an antihistamine, which
would be taken at a convenient time and which would release the dose at, e.g., just
before 4 a.m., such that the maximal effect of the dosage form is reached at that
time. The chronotherapeutic formulations of the invention may also be used to treat
arthritis. Glucocorticosteroids have a very favourable effect on the symptoms of rheumatoid
arthritis, e.g. morning stiffness, joint pain and joint swelling. With respect to
arthritis, chronobiological patterns have been observed with arthritis pain. People
with osteoarthritis (the most common form of arthritis) tend to have less pain in
the morning and more at night. But for people with rheumatoid arthritis, the pain
usually peaks in the morning and decreases as the day wears on. Recent animal studies
showing that joint inflammation in rats fluctuates over a 24-hour period support these
observations by both patients and physicians. Potential drug candidates in this therapeutic
area include (for all forms of arthritis) standard treatment, NSAIDs and corticosteroids,
etc. Preferably, the dosages should be timed to ensure that the highest blood levels
of the drug coincide with peak pain. For osteoarthritis - the optimal time for an
NSAID (ibuprofen, etc.) would be around noon or mid-afternoon. For rheumatoid arthritis
- the optimal time for an NSAID to be taken is after the evening meal.
[0118] With respect to attention deficit disorder, it has been observed that peak plasma
concentrations of the drug are lower when sustained release formulations are used,
and in some instances, sustained release formulations of methylphenidate have been
shown to have lower efficacy than conventional dosage forms. A dosage form which provides
for a delay in release of maximally effective amount of an agent to treat attention
deficit disorder could be useful, particularly if the dosage form provides in one
administration, and initial release of the active agent, followed by a predictable
delay and then a second release of the active agent. Potential drug candidates include
stimulants such as for example methylphenidate and pharmaceutically acceptable salts
thereof.
[0119] With respect to cancer therapy, animal studies suggest that chemotherapy may be more
effective and less toxic if cancer drugs are administered at carefully selected times.
The studies currently suggest that there may be different chronobiological cycles
for normal cells and tumor cells. If this is true, the goal would be to time the administration
of cancer drugs to the chronobiological cycles of tumor cells, making them more effective
against the cancer and less toxic to normal tissues. Potential drug candidates include,
e.g., injectables such as doxorubicin and cisplatin (combination) and floxuridine.
[0120] Chronotherapeutics are not entirely new in the treatment of cardiovascular disease.
Since 1986, people with angina have been treated with nitroglycerin patches that are
attached to their chest or shoulder in the morning and are removed in the evening.
This is considered to be "side door" chronotherapy because it is not based on the
recognition that a disease gets worse at a certain time of the day, and therefore
should be treated at that time of the day. Rather, it arose out of the recognition
that nitroglycerin is not effective when it is continuously administered. Based on
the fact that cardiologic diseases have a 24-hour pattern, the use of the chronotherapeutic
formulations of the present invention would be greatly desirable. It has been thought
by those skilled in the art that heart attacks, sudden death, angina and stroke all
seem to peak in the morning hours. Thus, it would be greatly desirable to provide
a chronotherapeutic oral formulation which would be taken at a convenient time and
which would release the dose such that the maximal effect of the dosage form is reached
at that time. Potential drug candidates include antihypertensive agents, antiischemic
agents, and agents that control clotting.
[0121] With respect to hypertension, blood pressure fluctuates over the 24-hour (circadian)
period. In most normotensive patients and in most patients with essential hypertension
(systemic vasoconstriction is associated with increased peripheral vascular resistance
in arterioles), circadian mechanisms plus differences in activity and stress during
the sleep/activity cycle cause blood pressure to rise rapidly upon awakening. After
it peaks during daytime activity, blood pressure declines during sleep by 10% to 20%
of the mean daytime level. Both blood pressure and heart rate typically rise early
in the morning and significantly increase myocardial oxygen demand to cause myocardial
ischemia in patients with known or nondiagnosed coronary artery disease. The rapid
surge in blood pressure on awakening is associated with an increased incidence of
morning cerebrovascular accidents and myocardial infarction. Moreover, the incidence
of cerebrovascular accidents and other cardiovascular events (sudden death, acute
myocardial infarction, and total ischemic burden) also follows a circadian pattern,
being greatest during the first 6 hours of the activity span (6 a.m. to 12 noon) and
least during sleep, as observed from the Framingham Study results. Morning surges
of blood pressure can theoretically rupture atherosclerotic plaques in coronary arteries,
injure underlying tissue, and promote clot formation in the early morning when coagulation
processes are most active. Thus, it would be greatly desirable to provide a chronotherapeutic
oral formulation which would be taken at a convenient time and which would have release
the dose such that the maximal effect of the dosage form is reached at that time.
[0122] In addition to a rapid rise in blood pressure on awakening, a "dip" in blood pressure
occurs in most people during nighttime sleep. The dip may vary or be absent in patients
with more severe forms of hypertension and among patients with secondary hypertension,
in whom blood pressure either fails to decline as expected or else rises during sleep,
relative to daytime levels. Blood pressure patterns have been grouped into four categories:
(i) "dippers" show a 10% to 20% decline in blood pressure during nighttime sleep compared
with their average daytime blood pressure level; (ii) "nondippers" have nighttime
blood pressures that vary little from the daytime levels; (iii) "superdippers" show
a decline in blood pressure greater than 20% at night from the daytime mean level;
and (iv) "risers" experience a high blood pressure at night compared with daytime
levels. Deviations in blood pressure from normal circadian patterns are associated
with an increased risk of end-organ damage and adverse cardiovascular events. Hypertensive
patients with nocturnal patterns of superdipping or nondipping blood pressure are
more likely to develop eye, renal, and cardiac pathologies and show a higher rate
of cardiovascular events, such as cerebrovascular accidents and myocardial infarction,
than normal dippers.
[0123] Chronotherapy is a treatment approach that allows for better control of blood pressure
during the day and night by delivering medication in amounts proportional to patients'
needs and, therefore, in synchrony with the circadian blood pressure rhythm. More
chronotherapeutic antihypertension medication is delivered in the morning and daytime
when blood pressure is greatest, and less at night when blood pressure typically declines
to the lowest level. The incidence of early morning cardiovascular events could theoretically
be decreased if early morning surges in blood pressure and heart rate are blunted
by the chronotherapeutic administration of indicated drugs using appropriate delivery
systems.
[0124] The calcium channel blocker verapamil reduces heart rate as well as blood pressure,
which is especially beneficial for patients with both ischemic heart disease and hypertension.
These characteristics of verapamil and its appropriate half-life made it a good choice
for the formulation of an antihypertensive drug with a chronotherapeutic oral drug
absorption system (CODAS). This system was designed to be taken at bedtime, to cause
a 4- to 5-hour initial lag in drug delivery and, thereafter, to achieve a controlled
release of drug. CODAS-verapamil capsules (Verelan
® PM) were made using the CODAS multiparticulate technology along with verapamil-coated
beads. When taken as directed, this formulation results in a maximum verapamil plasma
concentration around the time of awakening in the morning. Studies showed that nighttime
dosing of verapamil chronotherapy allows for better control of the sharp morning blood
pressure rise than do conventional antihypertensive medications. Bedtime dosing with
verapamil chronotherapy also controls daytime blood pressure without inducing hypotension
or superdipping of blood pressure at night, reducing the risk of target organ damage
due to poor perfusion pressure. Furthermore, verapamil chronotherapy is designed to
deliver more medication in the daytime than conventional verapamil and other antihypertension
medications. Potential drug candidates include antihypertensive medications such as
calcium channel blockers.
[0125] Medications to control high cholesterol, such as HMG-CoA reductase inhibitors, are
also considered to work better when given in the evening, a time when enzyme activity
levels peak. Therefore, it would be greatly desirable to provide a chronotherapeutic
oral formulation which would be taken at a convenient time and which would have release
the dose such that the maximal effect of the dosage form is reached at that time.
[0126] Treating ulcers is another example where timing is important. Since it is known that
the acidity produced by the stomach peaks at 6 p.m., medication to reduce the secretion
of acid in the stomach can therefore be delivered accordingly.
[0127] The benefits of chronotherapeutics include safety and more efficient treatment than
conventional therapies. This is achieved by delivering more medication when risk of
disease is greater, and delivering less medication when potential for disease symptoms
are less likely. Other benefits to the patient include an increased quality of life
and a once-a-day drug delivery system to increase patient compliance.
[0128] In certain preferred embodiments of the invention where the manifestations of the
disease state to be treated (e.g., asthmatic attack, pain from arthritis) are greatest
upon awakening, the chronotherapeutic formulations are preferably orally administered
to the patient at bedtime (e.g., at 9 or 10 p.m.) and have a lag time of 5 or 6 hours,
so that, e.g., a substantial portion of the drug in the compression coated delayed
release oral dosage form is released, e.g., between 2 to 3a.m., or between 3 to 4
a.m., and the drug is absorbed from the gastrointestinal tract and provides therapeutic
efficacy at a time which correlates with the peak of the manifestations of the disease
state.
[0129] In situations where the active agent is a low dose active agent (e.g., a drug administered
in a (unit) dose amount from 0.01 mg to 40 mg), in certain preferred embodiments,
the total tablet weight is from 220 mg to 900 mg; and the core weight is preferably
from 50 mg to 170 mg. Preferably, the core is from 5 to 23 percent, most preferably
18 to 20 percent by weight of the total tablet weight. In embodiments wherein the
active agent is a low dose active agent, the coating is preferably from 150 mg to
850 mg. Preferably, the coating is from 75 to 94 percent by weight, most preferably
from 78 to 80 percent by weight of the total tablet. Preferably, where the active
dose is a low dose active agent, the ratio of the core to gum (in the compression
coating) is from 1:0.37 to 1:5, preferably from 1:0.37 to 1:1.12, most preferably
from 1:0.75. Where the active dose is a low dose active agent, the ratio of the core
to compression coating material (all ingredients) is preferably from 1:2 to 1:9, and
in certain embodiments more preferably 1:4.
[0130] In situations where the active agent is a relatively high dose active agent (e.g.,
a drug administered in a (unit) dose amount from 41 mg to 300 mg), the ratio of core
to gum (in the compression coating) is from 1:0.3 to 1:3, preferably from 1:0.6 to
1:1.5. In certain embodiments, preferably where the active agent is a high dose active
agent, the ratio of the core to compression coating material (all ingredients) is
from 1:1 to 1:5, preferably from 1:2 to 1:3. In situations where the active agent
is a relatively high dose active agent, the total tablet weight is preferably from
500 mg to 1500 mg, more preferably from 750 mg to 1000 mg.
[0131] In the appended examples, the cores comprising the active agent are typically compression
coated with the coating formulation by hand on a rotary tablet press. In such a process,
roughly half the outer core material is first added to the die. An inner core tablet
is typically centered on the powder bed and is covered with the other half of the
outer coating powder. However, one skilled in the art will appreciate that compression
coating may be accomplished via automated tablet presses for commercialization. Prior
to compression coating with any tablet press, preferably 0.75% Pruv
® (sodium stearyl fumarate, NF) or another suitable lubricant is added to the compression
coating material(s). In certain examples wherein the coatings are indicate by the
gums, for example, 50% xanthan gum (XG), the coating comprises 50% xanthan gum diluted
with dextrose; and for example 50% locust bean gum (LBG), the coating comprises 50%
locust bean gum diluted with dextrose, etc.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
[0132] The following examples illustrate various aspects of the present invention. They
are not to be construed to limit the claims in any manner whatsoever.
EXAMPLE 1
[0133] A delayed release material to be used in the compression coatings of the invention
is prepared having the following formulation listed in Table 1:
Table 1
| Component |
Percentage |
| 1. Xanthan Gum |
12 |
| 2. Locust Bean Gum |
18 |
| 3. Dextrose |
70 |
| 4. Water* |
q.s. |
| * Removed during processing |
|
Process:
[0134]
- 1. The requisite amounts of xanthan gum, locust bean gum, and dextrose are dry blended
in a high speed mixer/granulator for 3 minutes.
- 2. Water (125-150 ml) is added to the dry blended mixture, and granulated for another
3 minutes.
- 3. The granulation is then dried in a fluid bed dryer to a LOD (loss on drying) of
less than about 10% by weight (e.g., 4-7% LOD).
EXAMPLE 2
[0135] A delayed release material to be used in the compression coatings of the invention
is prepared having the following formulation listed in Table 2:
Table 2
| Component |
Percentage |
| 1. Xanthan Gum |
25 |
| 2. Locust Bean Gum |
25 |
| 3. Dextrose |
35 |
| 4. Calcium Sulfate Dihydrate |
10 |
| 5. Ethylcellulose |
5 |
| 5. Alcohol, SD3A, anhydrous* |
20 |
| 6. Water* |
q.s. |
| * Removed during processing |
|
Process:
[0136]
- 1. The requisite amounts of xanthan gum, locust bean gum, calcium sulfate, and dextrose
are dry blended in a high speed mixer/granulator for 3 minutes.
- 2. A slurry of hydrophobic polymer (ethylcellulose) is prepared by dissolving ethyl
cellulose in ethyl alcohol.
- 3. The slurry is added to the dry blended mixture, and granulated for another 3 minutes.
- 4. The granulation was then dried in a fluid bed dryer to a LOD (loss on drying) of
less than about 10% by weight (e.g., 4-7% LOD).
EXAMPLE 3
[0137] A delayed release material to be used in the compression coatings of the invention
is prepared having the following formulation listed in Table 3:
Table 3
| Component |
Percentage |
| 1. Xanthan Gum |
15 |
| 2. Locust Bean Gum |
15 |
| 3. Dextrose |
60 |
| 4. Calcium Sulfate Dihydrate |
10 |
| 5. Water* |
q.s. |
| * Removed during processing |
|
Process:
[0138]
- 1. The requisite amounts of xanthan gum, locust bean gum, calcium sulfate, and dextrose
are dry blended in a high speed mixer/granulator for 3 minutes.
- 2. Water (125-150 ml) is added to the dry blended mixture, and granulated for another
3 minutes.
- 3. The granulation is then dried in a fluid bed dryer to a LOD (loss on drying) of
less than about 10% by weight (e.g., 4-7% LOD).
EXAMPLE 4
[0139] A delayed release material to be used in the compression coatings of the invention
is prepared having the following formulation listed in Table 4:
Table 4
| Component |
Percentage |
| 1. Xanthan Gum |
16 |
| 2. Locust Bean Gum |
24 |
| 3. Dextrose |
60 |
| 4. Water* |
q.s. |
| * Removed during processing |
|
Process:
[0140] The same process for Example 1 is used to prepare the delayed release coating of
Example 4.
EXAMPLE 5
[0141] A delayed release material to be used in the compression coatings of the invention
is prepared having the following formulation listed in Table 5:
Table 5
| Component |
Percentage |
| 1. Xanthan Gum |
20 |
| 2. Locust Bean Gum |
30 |
| 3. Dextrose |
45 |
| 4. Calcium Sulfate Dihydrate |
5 |
| 5. Water* |
q.s. |
| * Removed during processing |
|
Process:
[0142] The same process for Example 3 is used to prepare the delayed release material to
be used in the compression coatings of the invention in Example 5.
EXAMPLE 6
[0143] A delayed release material to be used in the compression coatings of the invention
is prepared having the following formulation listed in Table 6:
Table 6
| Component |
Percentage |
| 1. Xanthan Gum |
12 |
| 2. Locust Bean Gum |
18 |
| 3. Dextrose |
65 |
| 4. Calcium Sulfate Dihydrate |
5 |
| 5. Water* |
q.s. |
| * Removed during processing |
|
Process:
[0144] The same process for Example 3 is used to prepare the delayed release material to
be used in the compression coatings of the invention in Example 6.
EXAMPLE 7
[0145] A delayed release material to be used in the compression coatings of the invention
is prepared having the following formulation listed in Table 7:
Table 7
| Component |
Percentage |
| 1. Xanthan Gum |
10 |
| 2. Locust Bean Gum |
15 |
| 3. Dextrose |
75 |
| 4. Water* |
q.s. |
| * Removed during processing |
|
Process:
[0146] The same process for Example 1 is used to prepare the delayed release material to
be used in the compression coatings of the invention in Example 7.
EXAMPLE 8
[0147] A delayed release material to be used in the compression coatings of the invention
is prepared having the following formulation listed in Table 8:
Table 8
| Component |
Percentage |
| 1. Xanthan Gum |
8 |
| 2. Locust Bean Gum |
12 |
| 3. Dextrose |
80 |
| 4. Water* |
q.s. |
| * Removed during processing |
|
Process:
[0148] The same process for Example 1 is used to prepare the delayed release material to
be used in the compression coatings of the invention in Example 8.
EXAMPLE 9
[0149] A delayed release material to be used in the compression coatings of the invention
is prepared having the formulation listed in Table 9:
Table 9
| Component |
Percentage |
| 1. Xanthan Gum |
20 |
| 2. Locust Bean Gum |
30 |
| 3. Lactose |
50 |
| 4. Water* |
q.s. |
| * Removed during processing |
|
Process:
[0150] The same process for Example 1 is used to prepare the delayed release material to
be used in the compression coatings of the invention in Example 5, substituting lactose
for dextrose.
EXAMPLE 10
[0151] A delayed releases material to be used in the compression coatings of the invention
is prepared having the formulation listed in Table 10:
Table 10
| Component |
Percentage |
| 1. Xanthan Gum |
20 |
| 2. Locust Bean Gum |
30 |
| 3. Mannitol |
45 |
| 4. Hydroxypropylmethylcellulose |
5 |
| 5. Water* |
q.s. |
| * Removed during processing |
|
Process:
[0152]
- 1. The requisite amounts of xanthan gum, locust bean gum, mannitol, and hydroxypropylmethylcellulose
are dry blended in a high speed mixer/granulator for 3 minutes.
- 2. Water (125-150 ml) is added to the dry blended mixture, and granulated for another
3 minutes.
- 3. The granulation is then dried in a fluid bed dryer to a LOD (loss on drying) of
less than about 10% by weight (e.g., 4-7% LOD).
EXAMPLE 11
[0153] A delayed release material to be used in the compression coatings of the invention
is prepared having the formulation listed in Table 11:
Table 11
| Component |
Percentage |
| 1. Xanthan Gum |
12 |
| 2. Locust Bean Gum |
18 |
| 3. Mannitol |
70 |
| 4. Water* |
q.s. |
| * Removed during processing |
|
Process:
[0154] The same process for Example 1 is used to prepare the delayed release material to
be used in the compression coatings of the invention in Example 11, substituting mannitol
for dextrose.
EXAMPLE 12
[0155] A delayed release material to be used in the compression coatings of the invention
is prepared having the formulation listed in Table 12:
Table 12
| Component |
Percentage |
| 1. Xanthan Gum |
9 |
| 2. Locust Bean Gum |
13.5 |
| 3. Mannitol |
77.5 |
| 4. Water* |
q.s. |
| * Removed during processing |
|
Process:
[0156] The same process for Example 10 is used to prepare the delayed release material to
be used in the compression coatings of the invention in Example 12.
EXAMPLE 13
[0157] A delayed release material to be used in the compression coatings of the invention
is prepared having the formulation listed in Table 13:
Table 13
| Component |
Percentage |
| 1. Xanthan Gum |
8 |
| 2. Locust Bean Gum |
12 |
| 3. Mannitol |
80 |
| 4. Water* |
q.s. |
| * Removed during processing |
|
Process:
[0158] The same process for Example 12 is used to prepare the delayed release material to
be used in the compression coatings of the invention in Example 13
EXAMPLE 14
[0159] A delayed release material to be used in the compression coatings of the invention
is prepared having the formulation listed in Table 14:
Table 14
| Component |
Percentage |
| 1. Xanthan Gum |
6 |
| 2. Locust Bean Gum |
9 |
| 3. Mannitol |
85 |
| 4. Water* |
q.s. |
| * Removed during processing |
|
Process:
[0160] The same process for Example 12 is used to prepare the delayed release material to
be used in the compression coatings of the invention in Example 14.
EXAMPLE 15
[0161] A delayed release material to be used in the compression coatings of the invention
is prepared having the formulation listed in Table 15:
Table 15
| Component |
Percentage |
| 1. Xanthan Gum |
4 |
| 2. Locust Bean Gum |
6 |
| 3. Mannitol |
90 |
| 4. Alcohol, SD3A, anhydrous* |
- |
| 5. Water* |
q.s. |
| * Removed during processing |
|
Process:
[0162] The same process for Example 12 is used to prepare the delayed release material to
be used in the compression coatings of the invention in Example 15.
EXAMPLE 16
[0163] A delayed release coating is prepared having the following formulation listed in
Table 16:
Table 16
| Component |
Percentage |
| 1. Xanthan Gum |
3 |
| 2. Locust Bean Gum |
4.5 |
| 3. Mannitol |
92.5 |
| 4. Water* |
q.s. |
| * Removed during processing |
|
Process:
[0164] The same process for Example 12 is used to prepare the delayed release material to
be used in the compression coatings of the invention in Example 16.
EXAMPLE 17
[0165] A delayed release material to be used in the compression coatings of the invention
is prepared having the formulation listed in Table 17:
Table 17
| Component |
Percentage |
| 1. Xanthan Gum |
8 |
| 2. Locust Bean Gum |
12 |
| 3. Dextrose |
40 |
| 4. Microcrystalline Cellulose |
40 |
| 5. Water* |
q.s. |
| * Removed during processing |
|
Process:
[0166]
- 1. The requisite amounts of xanthan gum, locust bean gum, dextrose, and microcrystalline
cellulose are dry blended in a high speed mixer/granulator for 3 minutes.
- 2. Water (125-150 ml) is added to the dry blended mixture, and granulated for another
3 minutes.
- 3. The granulation is then dried in a fluid bed dryer to a LOD (loss on drying) of
less than about 10% by weight (e.g., 4-7% LOD).
EXAMPLE 18
[0167] A delayed release material to be used in the compression coatings of the invention
is prepared having the formulation listed in Table 18:
Table 18
| Component |
Percentage |
| 1. Xanthan Gum |
8 |
| 2. Locust Bean Gum |
12 |
| 3. Dextrose |
- |
| 4. Microcrystalline Cellulose |
80 |
| 5. Water* |
q.s. |
| * Removed during processing |
|
Process:
[0168] The same process for Example 1 is used to prepare the delayed release material to
be used in the compression coatings of the invention in Example 18, substituting microcrystalline
cellulose for dextrose.
EXAMPLE 19
[0169] A prednisolone core composition was prepared having the ingredients set forth in
Table 19:
Table 19
| Component |
Percent |
amt. (mg) |
| 1. Prednisolone |
2.0 |
1.0 |
| 2. Prosolv SMCC™ 50 |
32.75 |
16.4 |
| 3. Prosolv SMCC™ 90 |
50 |
25.0 |
| 4. Explotab® |
10 |
5.0 |
| 5. Sodium carboxymethylcellulose |
5 |
2.5 |
| 6. Pruv |
0.25 |
0.1 |
| Total |
100 |
50 |
| Core size and shape |
3/16" Round SC* |
|
| * SC means standard concave |
|
|
Process:
[0170]
- 1. Blend the requisite amounts of prednisolone and Prosolv™ SMCC 50 in a V-blender
for 5 to 10 minutes.
- 2. Add the requisite amounts of Prosolv™ SMCC 90, Explotab® and sodium carboxymethylcellulose to the blend and continue blending for another
5 minutes.
- 3. Add the requisite amount of Pruv to the mixture and blend for an additional 5 minutes.
- 4. Compress the tablet cores using tablet press.
EXAMPLE 20
[0171] A prednisolone core composition was prepared having the formulation ingredients set
forth in Table 20:
Table 20
| Component |
Percent |
amt. (mg) |
| 1. Prednisolone |
10 |
5 |
| 2. Prosolv SMCC™ 50 |
NA |
NA |
| 3. Prosolv SMCC™ 90 |
81.75 |
40.875 |
| 4. Explotab® |
6 |
3 |
| 5. Sodium carboxymethylcellulose |
NA |
NA |
| 6. Pruv |
0.25 |
0.125 |
| 7. PVP |
2 |
1 |
| Total |
100 |
50 |
| Core size and shape |
3/16" Round FF* |
|
| *FF= flat face |
|
|
Process:
[0172]
- 1. Blend the requisite amounts of prednisolone, Prosolv™ SMCC 90, Explotab® for 5 to 10 minutes.
- 2. Add the requisite amount of Pruv and PVP to the mixture and blend for an addition
5 minutes.
- 3. Compress the tablet cores using tablet press.
EXAMPLE 21
[0173] A prednisolone core composition was prepared having the formulation ingredients set
forth in Table 21:
Table 21
| Component |
Percent |
amt. (mg) |
| 1. Prednisolone |
10 |
5 |
| 2. Prosolv SMCC™ 50 |
NA |
NA |
| 3. Prosolv SMCC™ 90 |
75.75 |
37.375 |
| 4. Explotab® |
10 |
5 |
| 5. Sodium carboxymethylcellulose |
5 |
2.5 |
| 6. Pruv |
0.25 |
0.1 |
| Total |
100 |
50 |
| Core size and shape |
3/16" Round FF |
|
Process:
[0174]
- 1. Blend the requisite amounts of prednisolone, Prosolv™ SMCC 90, Explotab®, and sodium carboxymethylcellulose for 5 to 10 minutes.
- 2. Add the requisite amount of Pruv and PVP to the mixture and blend for an additional
5 minutes.
- 3. Compress the tablet cores using tablet press.
EXAMPLE 22
[0175] A prednisolone core composition was prepared having the formulation ingredients set
forth in Table 22:
Table 22
| Component |
Percent |
amt. (mg) |
| 1. Prednisolone |
2 |
1.0 |
| 2. Prosolv SMCC™ 50 |
40 |
20.0 |
| 3. Prosolv SMCC™ 90 |
47.75 |
23.9 |
| 4. Explotab® |
6 |
3.0 |
| 5. PVP |
2 |
1.0 |
| 6. Talc |
2 |
1.0 |
| 7. Pruv |
0.25 |
0.1 |
| Total |
100 |
50 |
| Core size and shape |
3/16" Round SC |
|
Process:
[0176]
1. Blend the requisite amounts of prednisolone and Prosolv™ SMCC 50 in a V-blender
for 5 to 10 minutes.
5. Add the requisite amounts of Prosolv™ SMCC 90, Explotab®, PVP, and talc to the blend and continue blending for another 5 minutes.
6. Add the requisite amount of Pruv to the mixture and blend for an additional 5 minutes.
7. Compress the tablet cores using tablet press.
EXAMPLE 23
[0177] A prednisolone core composition was prepared having the formulation ingredients set
forth in Table 23:
Table 23
| Component |
Percent |
amt. (mg) |
| 1. Prednisolone |
2 |
3.4 |
| 2. Prosolv SMCC™ 50 |
40 |
68 |
| 3. Prosolv SMCC™ 90 |
47.75 |
81.75 |
| 4. Explotab® |
6 |
10.2 |
| 5. Sodium carboxymethylcellulose |
2 |
3.4 |
| 6. Talc |
2 |
3.4 |
| 7. Pruv |
0.25 |
0.425 |
| Total |
100 |
170 |
| Core size and shape |
1/4" Round FF |
|
Process:
[0178]
- 1. Blend the requisite amounts of prednisolone and Prosolv™ SMCC 50 in a V-blender
for 5 to 10 minutes.
- 2. Add the requisite amounts of Prosolv™ SMCC 90, Explotab®, sodium carboxymethylcellulose, and talc to the blend and continue blending for another
5 minutes.
- 3. Add the requisite amount of Pruv to the mixture and blend for an additional 5 minutes.
- 4. Compress the tablet cores using tablet press.
EXAMPLE 24
[0179] A prednisolone core composition was prepared having the formulation ingredients set
forth in Table 24:
Table 24
| Component |
Percent |
amt. (mg) |
| 1. Prednisolone |
2 |
1 |
| 2. Prosolv SMCC™ 50 |
40 |
20 |
| 3. Prosolv SMCC™ 90 |
47.75 |
23.875 |
| 4. Explotab® |
6 |
3 |
| 5. Sodium carboxymethylcellulose |
2 |
1 |
| 6. Talc |
2 |
1 |
| 6. Pruv |
0.25 |
0.125 |
| Total |
100 |
50 |
| Core size and shape |
3/16" Round SC |
|
Process:
[0180] The same process for Example 23 is used to prepare the core of Example 24.
EXAMPLE 25
[0181] A prednisolone core composition was prepared having the formulation ingredients set
forth in Table 25:
Table 25
| Component |
Percent |
amt. (mg) |
| 1. Prednisolone |
2 |
1 |
| 2. Prosolv SMCC™ 50 |
40 |
20 |
| 3. Prosolv SMCC™ 90 |
55.75 |
27.85 |
| 4. Explotab® |
NA |
NA |
| 5. Sodium carboxymethylcellulose |
NA |
NA |
| 6. Talc |
2 |
1 |
| 7. Pruv |
0.25 |
0.125 |
| Total |
100 |
50 |
| Core size and shape |
3/16" Round SC |
|
Process:
[0182] The same process for Example 23 is used to prepare the core of Example 25, without
the inclusion of Explotab
® and sodium carboxymethylcellulose.
EXAMPLE 26
[0183] A prednisolone core composition was prepared having the formulation ingredients set
forth in Table 26:
Table 26
| Component |
Percent |
amt. (mg) |
| 1. Prednisolone |
2 |
1 |
| 2. Prosolv SMCC™ 50 |
40 |
20 |
| 3. Prosolv SMCC™ 90 |
52.75 |
26.375 |
| 4. Explotab® |
3 |
1.5 |
| 5. Sodium carboxymethylcellulose |
NA |
NA |
| 6. Talc |
2 |
1 |
| 7. Pruv |
0.25 |
0.125 |
| Total |
100 |
50 |
| Core size and shape |
3/16" Round SC |
|
Process:
[0184] The same process for Example 23 is used to prepare the core of Example 26, without
the inclusion of sodium carboxymethylcellulose.
EXAMPLE 27
[0185] A prednisolone core composition was prepared having the formulation ingredients set
forth in Table 27:
Table 27
| Component |
Percent |
amt. (mg) |
| 1. Prednisolone |
2 |
1 |
| 2. Prosolv SMCC™ 50 |
40 |
20 |
| 3. Prosolv SMCC™ 90 |
51.75 |
25.875 |
| 4. Explotab® |
3 |
1.5 |
| 5. Sodium carboxymethylcellulose |
1 |
0.5 |
| 6. Talc |
2 |
1 |
| 6. Pruv |
0.25 |
0.125 |
| Total |
100 |
50 |
| Core size and shape |
3/16" Round SC |
|
Process:
[0186] The same process for Example 23 is used to prepare the core of Example 27.
EXAMPLE 28
[0187] A prednisolone core composition was prepared having the formulation ingredients set
forth in Table 28:
Table 28
| Component |
Percent |
amt. (mg) |
| 1. Prednisolone |
2 |
1 |
| 2. Prosolv SMCC™ 50 |
40 |
20 |
| 3. Prosolv SMCC™ 90 |
53.75 |
26.875 |
| 4. Explotab® |
NA |
NA |
| 5. Sodium carboxymethylcellulose |
2 |
1 |
| 6. Talc |
2 |
1 |
| 7. Pruv |
0.25 |
0.125 |
| Total |
100 |
50 |
| Core size and shape |
3/16" Round SC |
|
Process:
[0188] The same process for Example 23 is used to prepare the core of Example 28, without
the inclusion of Explotab
®.
EXAMPLE 29
[0189] A prednisolone core composition was prepared having the formulation ingredients set
forth in Table 29:
Table 29
| Component |
Percent |
amt. (mg) |
| 1. Prednisolone |
2 |
1 |
| 2. Prosolv SMCC™ 50 |
40 |
20 |
| 3. Prosolv SMCC™ 90 |
47.75 |
23.875 |
| 4. Explotab® |
2 |
1 |
| 5. Sodium carboxymethylcellulose |
6 |
3 |
| 6. Talc |
2 |
1 |
| 7. Pruv |
0.25 |
0.125 |
| Total |
100 |
50 |
| Core size and shape |
3/16" Round SC |
|
Process:
[0190] The same process for Example 23 is used to prepare the core of Example 29.
EXAMPLE 30
[0191] A prednisolone core composition was prepared having the formulation ingredients set
forth in Table 30:
Table 30
| Component |
Percent |
amt. (mg) |
| 1. Prednisolone |
2 |
1 |
| 2. Prosolv SMCC™ 50 |
40 |
20 |
| 3. Prosolv SMCC™ 90 |
49.75 |
24.875 |
| 4. Explotab® |
NA |
NA |
| 5. Sodium carboxymethylcellulose |
6 |
3 |
| 6. Talc |
2 |
1 |
| 7. Pruv |
0.25 |
0.125 |
| Total |
100 |
50 |
| Core size and shape |
3/16" Round SC |
|
Process:
[0192] The same process for Example 23 is used to prepare the core of Example 30, without
the inclusion of Explotab
®.
EXAMPLE 31
[0193] A prednisolone core composition was prepared having the formulation ingredients set
forth in Table 31:
Table 31
| Component |
Percent |
amt. (mg) |
| 1. Prednisolone |
2 |
1 |
| 2. Prosolv SMCC™ 50 |
26 |
13 |
| 3. Prosolv SMCC™ 90 |
49.75 |
24.875 |
| 4. Explotab® |
20 |
10 |
| 5. Sodium carboxymethylcellulose |
NA |
NA |
| 6. Talc |
2 |
1 |
| 7. Pruv |
0.25 |
0.125 |
| Total |
100 |
50 |
| Core size and shape |
3/16" Round SC |
|
Process:
[0194] The same process for Example 23 is used to prepare the core of Example 31, without
the inclusion of sodium carboxymethylcellulose.
EXAMPLE 32
[0195] A prednisolone core composition was prepared having the formulation ingredients set
forth in Table 32:
Table 32
| Component |
Percent |
amt. (mg) |
| 1. Prednisolone |
2 |
1 |
| 2. Prosolv SMCC™ 50 |
26 |
13 |
| 3. Prosolv SMCC™ 90 |
49.75 |
24.875 |
| 4. Explotab® |
20 |
10 |
| 5. Sodium carboxymethylcellulose |
NA |
NA |
| 6. Talc |
2 |
1 |
| 7. Pruv |
0.25 |
0.125 |
| Total |
100 |
50 |
| Core size and shape |
3/16" Round SC |
|
Process:
[0196] The same process for Example 23 is used to prepare the core of Example 32, without
the inclusion of sodium carboxymethylcellulose.
EXAMPLE 33
[0197] A prednisolone core composition was prepared having the formulation ingredients set
forth in Table 33:
Table 33
| Component |
Percent |
amt. (mg) |
| 1. Prednisolone |
2 |
1 |
| 2. Prosolv SMCC™ 50 |
40 |
20 |
| 3. Prosolv SMCC™ 90 |
52.75 |
26.375 |
| 4. Explotab® |
3 |
1.5 |
| 5. Sodium carboxymethylcellulose |
NA |
NA |
| 6. Talc |
2 |
1 |
| 7. Pruv |
0.25 |
0.125 |
| Total |
100 |
50 |
| Core size and shape |
3/16" Round SC |
|
Process:
[0198] The same process for Example 23 is used to prepare the core of Example 33, without
the inclusion sodium carboxymethylcellulose.
EXAMPLE 34
[0199] A prednisolone core composition was prepared having the formulation set forth in
Table 34:
Table 34
| Component |
Percent |
amt. (mg) |
| 1. Prednisolone |
2 |
1 |
| 2. Prosolv SMCC™ 50 |
40 |
20 |
| 3. Prosolv SMCC™ 90 |
51.75 |
25.875 |
| 4. Explotab® |
3 |
1.5 |
| 5. Sodium carboxymethylcellulose |
1 |
0.5 |
| 6. Talc |
2 |
1 |
| 7. Pruv |
0.25 |
0.125 |
| Total |
100 |
50 |
| Core size and shape |
3/16" Round SC |
|
Process:
[0200] The same process for Example 23 is used to prepare the core of Example 34.
EXAMPLE 35
[0201] A prednisolone core composition was prepared having the formulation ingredients set
forth in Table 35:
Table 35
| Component |
Percent |
amt. (mg) |
| 1. Prednisolone |
2 |
1 |
| 2. Prosolv SMCC™ 50 |
40 |
20 |
| 3. Prosolv SMCC™ 90 |
53.75 |
26.875 |
| 4. Explotab® |
NA |
NA |
| 5. Sodium carboxymethylcellulose |
2 |
1 |
| 6. Talc |
2 |
1 |
| 7. Pruv |
0.25 |
0.125 |
| Total |
100 |
50 |
| Core size and shape |
3/16" Round SC |
|
Process:
[0202] The same process for Example 23 is used to prepare the core of Example 35, without
the inclusion of Explotab
®.
EXAMPLE 36
[0203] A prednisolone core composition was prepared having the formulation ingredients set
forth in Table 36:
Table 36
| Component |
Percent |
amt. (mg) |
| 1. Prednisolone |
4 |
2 |
| 2. Prosolv SMCC™ 50 |
40 |
20 |
| 3. Prosolv SMCC™ 90 |
45.75 |
22.875 |
| 4. Explotab® |
6 |
3 |
| 5. Sodium carboxymethylcellulose |
2 |
1 |
| 6. Talc |
2 |
1 |
| 7. Pruv |
0.25 |
0.125 |
| Total |
100 |
50 |
| Core size and shape |
3/16" Round SC |
|
Process:
[0204] The same process for Example 23 is used to prepare the core of Example 36.
EXAMPLES 37-39
[0205] In Examples 37-39, prednisolone tablets were prepared having a core formulation as
described in Example 21 and coating formulation as described in Example 3. The tablet
formulations of Examples 37-39 are listed in Table 37 below:
Table 37
| Component |
Ex. 37 Amt. (mg) |
Ex. 38 amt. (mg) |
Ex. 39 amt. (mg) |
| 1. Example 21 core |
50 |
50 |
50 |
| 2. Example 3 coating |
150 |
250 |
350 |
| Total tablet weight |
200 |
300 |
400 |
| Size and shape of tablet |
9/32" round standard concave |
⅜" round standard concave |
⅜" round standard concave |
| Compression force |
8-9 kP |
8-9 kP |
8-9 kP |
Process:
[0206]
- 1. Weigh out the requisite amount of immediate release cores and set aside.
- 2. Blend 0.75% by weight of Pruv® sodium stearyl fumarate, NF, (commercially available from the Edward Mendell Co.,
Inc.) with the requisite amount of coating for 5 minutes.
- 3. Weigh out approximately half of the compression coating.
- 4. Pour the lower layer of the compression coating into the lower punch of the die.
- 5. Place the immediate release core in the center of the compression coating.
- 6. Pour the top layer of into the die.
- 7. Rotate the punch station for compression.
- 8. Weigh out finished tablets to ensure proper weight.
[0207] The tablets of Examples 37-39 were tested using USP apparatus type III with 250 mL
DI water at 15 dips per minute (dpm) giving the following results listed in Table
38:
Table 38
| Time (hours) |
0 |
2 |
4 |
6 |
8 |
10 |
12 |
16 |
| Example 37 % dissolved |
0 |
0 |
0 |
0 |
18.6 |
- |
- |
- |
| Example 38 % dissolved |
0 |
0 |
0 |
0 |
0 |
35.6 |
100 |
100 |
| Example 39 % dissolved |
0 |
0 |
0 |
0 |
0 |
0 |
6.8 |
100 |
[0208] The tablets of Examples 37-39 resulted the following lag times (time when prednisolone
is release from the tablet) and full release times (time when all of prednisolone
is released from the tablet) listed in Table 39:
Table 39
| |
Example 37 |
Example 38 |
Example 39 |
| Lag time (hours) |
6-7 |
8-9 |
10-12 |
| Full release (hours) |
8-9 |
10-12 |
14-16 |
EXAMPLES 40-42
[0209] In Examples 40-42, prednisolone tablets were prepared having a core formulation as
described in Example 21 and coating formulation as described Example 2. The tablet
formulations of Examples 40-42 are listed in Table 40 below:
Table 40
| Component |
Ex. 40 |
Ex. 41 |
Ex. 42 |
| |
Amt. (mg) |
amt. (mg) |
amt. (mg) |
| 1. Example 21 core |
50 |
50 |
50 |
| 2. Example 2 coating |
150 |
250 |
350 |
| Total tablet weight |
200 |
300 |
400 |
| Size and shape of tablet |
9/32" round standard concave |
⅜" round standard concave |
⅜" round standard concave |
| Compression force |
8-9 kP |
8-9 kP |
8-9 kP |
Process:
[0210] The tablets of Examples 40-42 are prepared using the same process as examples 37-39.
[0211] The tablets of Examples 40-42 were tested using USP apparatus type III with 250 mL
DI water at 15 dips per minute (dpm) giving the following results listed in Table
41:
Table 41
| Time (hours) |
0 |
2 |
4 |
6 |
8 |
10 |
12 |
16 |
| Example 40 % dissolved |
0 |
- |
22.7 |
40.6 |
100 |
- |
- |
- |
| Example 41 % dissolved |
0 |
0 |
0 |
0 |
0 |
0 |
100 |
100 |
| Example 42 % dissolved |
0 |
0 |
0 |
0 |
0 |
0 |
19.5 |
19.5 |
[0212] The tablets of Examples 40-42 resulted in the following lag times (time when prednisolone
is release from the tablet) and full release times (time when all of prednisolone
is released from the tablet) listed in Table 42:
Table 42
| |
Example 40 |
Example 41 |
Example 42 |
| Lag time (hours) |
6-7 |
10-11 |
10-11 |
| Full release (hours) |
7-8 |
11-12 |
11-12 |
[0213] As can be seen, as total tablet weight increases (due to increase in coating weight),
lag time and the corresponding release time also tend to increase.
EXAMPLE 43
[0214] In Example 43, various delayed release coating formulations were prepared in order
to determine the effect of the gum percentage in the coating formulation on the time
of release and the rate of release of the active agent within the tablet core.
[0215] The ingredients of the various delayed release coating granulations of this example
having varying gum percentages are as follows:
Table 43a
| Formulation: |
Ex. 2 Coating |
Ex. 3 coating |
Ex. 8 coating |
Xanthan |
| |
% |
mg/tab |
% |
Mg/tab |
% |
mg/tab |
% |
mg/tab |
| 1. a. Core (Ex. 24 core) |
- |
- |
- |
- |
22.73% |
50 |
22.73% |
50 |
| b. Core (Ex. 22 core) |
22.73% |
50 |
22.73% |
50 |
- |
- |
- |
- |
| 2. Ex. 2 coating |
76.69% |
168.725 |
- |
- |
- |
- |
- |
- |
| 3. Ex. 3 coating |
- |
- |
76.69% |
168.725- |
|
- |
- |
- |
| 4. Ex. 8 coating |
- |
- |
- |
- |
76.69% |
168.725 |
- |
- |
| 5. Xanthan Gum |
- |
- |
- |
- |
- |
- |
76.69% |
168.7 |
| 6. Sodium Stearyl |
0.58% |
1.275 |
0.58% |
1.275 |
0.58% |
1.275 |
0.58% |
1.275 |
| Fumarate |
|
|
|
|
|
|
|
|
| Tablet weight (mg) |
|
220 |
|
220 |
|
220 |
|
220 |
| Tablet hardness (kP) |
|
8-9 |
|
8-9 |
|
8-9 |
|
8-9 |
[0216] The effects of the different percentages of gums within the delayed release compression
coating are set forth in the table below.

[0217] As shown in the Table 43b, the formulation with 20% gums released the active drug
faster than did the formulations with 30% or 50% gums. The results followed the rank
order for % gums with granulated delayed release examples. Xanthan gum (ungranulated)
did not track (e.g., provide the same delayed release) as with the other delayed release
coatings in this example (which had granulated gums).
[0218] As can be seen from the results set forth above, as the amount of gum with respect
to drug in the formulation is increased, a corresponding increase in lag time before
release of the drug is observed.
EXAMPLE 44
[0219] In Example 44, various examples of delayed release compression coating formulations
were prepared in order to determine the effect of ratio of the drug within the tablet
to the gum within the coating formulation on the time of release and the rate of release
of the active agent within the tablet core.
[0220] The ingredients of the various delayed release coating granulations are shown in
the examples above. The effects of the different drug to gum ratios are set forth
in the table below.

[0221] In this Example, the gums of the Ex. 8 coating (Drug:Gum ratio of 1:33.75) showed
faster release time than both Ex. 3 coating (Drug:Gum ratio of 1:50.6) and Ex. 2 coating
(Drug:Gum ratio of 1:84.4). Xanthan gum followed rank order with itself (e.g., the
larger tablet having more total gum had a longer delay) but not with the granulated
materials (Ex. 8, 2, and 3 coatings). It was observed that, as the amount of gum relative
to drug is increased, a corresponding increase in lag time is observed. The conclusion
reached is that increasing gum to drug ratio increased (longer) release lag time before
release of the drug.
EXAMPLE 45
[0222] In Example 45, various lots of delayed release coating formulations were prepared
in order to determine the effect of the thickness of the sustained release coating
on the time of release and the rate of release of the active agent within the tablet
core.
[0223] The ingredients of the various inner core formulations are shown in the examples
above, and the ingredients of the various delayed release coating granulations are
shown in Table 45. The effects of the delayed release coating thickness are set forth
in the table below.

[0224] In this example, it was observed that tablets with 170 mg of Example 8 coating were
faster releasing than tablets with 250 mg Example 8 coating. It was thus observed
that, as the thickness of coating is increased in the tablet, a corresponding increase
in lag time is observed. The conclusion reached is that tablets with a thicker coating
showed a longer lag time before release of the drug.
EXAMPLE 46
[0225] In Example 46, the effect of the addition of an extragranular excipient(s) to the
delayed release coating of Example 2 was measured. In this example, the types of excipient
added were Microcrystalline cellulose, Polyvinylpyrrolidone and Polyethylene glycol,
and these excipients were added in levels of 0, 5% and 10%.
[0226] The ingredients of the inner core formulation of this Example is shown in Example
24 above, and the ingredients of the various delayed release coating granulation of
this Example are shown in Example 2 above. The amounts or percentages of extragranular
excipients added are set forth in Tables 46a and 46b below:
TABLE 46a
| Formulation: |
Control |
addition of 5%PVP |
addition of 10%PVP |
| |
% |
mg/tab |
% |
mg/tab |
% |
mg/tab |
| Core (Ex. 24) |
22.72% |
50 |
22.73 % |
50 |
22.73 % |
50 |
| Delayed release coating (Ex. 2) |
76.69% |
168.725 |
73% |
160.225 |
68.97 % |
151.725 |
| Polyvinylpyrolidone K-30 |
Na |
na |
3.86% |
8.5 |
7.73% |
17 |
| Polyethylene Glycol, 6000 |
Na |
na |
Na |
na |
na |
na |
| Microcrystalline Cellulose |
Na |
na |
Na |
na |
na |
na |
| Sodium Stearyl Fumarate |
0.58% |
1.275 |
0.58% |
1.275 |
0.58% |
1.275 |
| Tablet weight (mg) |
|
220 |
|
220 |
|
220 |
| Tablet hardness (kP) |
|
8-9 |
|
8-9 |
|
8-9 |
TABLE 46b
| Formulation: |
addition of 5%PEG |
addition of 10%PEG |
addition of 5%MCC |
Addition of 10%MCC |
| |
% |
mg/tab |
% |
mg/tab |
% |
mg/tab |
% |
mg/tab |
| Core (Ex. 24) |
22.73% |
50 |
22.73% |
50 |
22.73 % |
50 |
22.73 % |
50 |
| Delayed release coating (Ex. 2) |
73% |
160.225 |
68.97% |
151.725 |
73% |
160.225 |
68.97 % |
151.725 |
| Polyvinylpyrolidone K-30 |
na |
na |
Na |
na |
na |
na |
Na |
na |
| Polyethylene Glycol, 6000 |
3.86% |
8.5 |
0.07727 2 |
17 |
na |
na |
Na |
na |
| Microcrystalline Cellulose |
na |
na |
Na |
na |
3.86% |
8.5 |
7.73% |
17 |
| Sodium Stearyl Fumarate |
0.58% |
1.275 |
0.58% |
1.275 |
0.58% |
1.275 |
0.58% |
1.275 |
| Tablet weight (mg) |
|
220 |
|
220 |
|
220 |
|
220 |
| Tablet hardness (kP) |
|
8-9 |
|
8-9 |
|
8-9 |
|
8-9 |
[0227] The effects of the addition of extragranular excipient to the sustained release coating
are set forth in the table below.

[0228] In this example, it was observed that the addition of 5% and 10% Polyethylene Glycol
6000 served to slightly speed the release of active agent. Tablets with 5% PVP K-30
also show slightly shorter lag time compared to the control. The release speed and
lag time of tablets with 10% PVP K-30 were unchanged. Tablets made with 10% MCC showed
no change in lag time, although they were slower with 5% MCC. The conclusion reached
is that lag time can be varied by the addition of extragranular additives into the
sustained release coating.
EXAMPLE 47
[0229] In Example 47, a scaled up production of the sustained release coating was done in
order to determine whether tablets produced at production scale exhibit release profiles
similar to those of tablets produced in laboratory scale.
[0230] In this example, the core-coated tablets were produced on a production press at Elizabeth
Hata. A HT-AP44MSU-C 44 station core coating press was used to press the tablets.
The inner cores of the tablets were made with a ¼" round flat face with a beveled
edge, tableted to 170 mg and 8-10kP. The final tablets were made 9mm round concave,
and were tableted to 525 and 560 mg, 8-10 kP.
[0231] The blends for the production scale were composed as follows:
Inner Core blend: Outer Coating blend:
2% Prednisolone Example 2 w/ 0.75% sodium stearyl
40% Prosolv SMCC 50 fumarate
47.75% Prosolv SMCC 90
6% Croscarmellose Sodium
2% Sodium Starch Glycolate
2% Talc
0.25% Sodium Stearyl Fumarate
[0232] In production of the tablets, the press speed varied from 9 to 12 rpm.
[0233] The effects of the scaled up production of the delayed release coating are shown
in the data points for which are set forth in Table 47 below.

[0234] In this example, it was observed that tablets produced at production scale exhibit
similar release profiles to tablets produced at laboratory scale. Accordingly, the
conclusion reached is that formulation and production technology can be successfully
scaled up.
EXAMPLE 48-57
[0235] In Examples 48-57, prednisolone tablets were prepared having core formulations with
different amounts of disintegrants and coating formulations as described Example 10.
Each tablet had the same core weight, same coating weight, and the same total tablet
weight. The tablet formulations of Examples 48-57 are listed in Tables 48 and 49 below:
Table 48
| Component |
Ex. 48 |
Ex. 49 |
Ex. 50 |
Ex. 51 |
Ex. 52 |
| Core formulation used Disintegrant |
Ex. 25 core |
Ex. 28 core |
Ex. 26 core |
Ex. 27 core |
Ex. 31 core |
| none |
2% Ac-Di-Sol |
3% Explotab |
3% Explotab and 2% Ac-Di-Sol |
6% Ac-Di-Sol |
| |
amt. (mg) |
amt. (mg) |
amt. (mg) |
amt. (mg) |
amt. (mg) |
| 1. Core |
50 |
50 |
50 |
50 |
50 |
| 2. Example 10 coating |
450 |
450 |
450 |
450 |
450 |
| Total tablet weight |
500 |
500 |
500 |
500 |
500 |
Table 49
| Component |
Ex. 53 |
Ex. 54 |
Ex. 55 |
Ex. 56 |
Ex. 57 |
| Core formulation used Disintegrant |
Ex. 29 core |
Ex. 29 core |
Ex. 31 core |
Ex. 30 core |
Ex. 32 core |
| 2% Explotab V17 and 6% Ac-Di-Sol |
2% Explotab V17 and 6% Ac-Di-Sol |
6% Ac-Di-Sol |
20% Explotab |
20% Explotab |
| |
amt. (mg) |
amt. (mg) |
amt. (mg) |
amt. (mg) |
amt. (mg) |
| 1. Core |
50 |
50 |
50 |
50 |
50 |
| 2. Example 10 coating |
450 |
450 |
450 |
450 |
450 |
| Total tablet weight |
500 |
500 |
500 |
500 |
500 |
[0236] The tablets of Examples 48-57 were tested using USP dissolution apparatus type III
with 250 mL DI water at 15 dips per minute (dpm) giving the following results listed
in Table 50:
Table 50
| Time (hours) |
0 |
3 |
4 |
4.5 |
5 |
5.5 |
6 |
6.5 |
7 |
8 |
| Example 48 % dissolved |
0 |
0 |
0 |
- |
0 |
- |
8.3 |
- |
12 |
12 |
| Example 49 % dissolved |
0 |
0 |
0 |
- |
73.7 |
- |
100 |
- |
100 |
100 |
| Example 50 % dissolved |
0 |
0 |
0 |
- |
78.3 |
- |
100 |
- |
100 |
100 |
| Example 51 % dissolved |
0 |
0 |
0 |
- |
14.9 |
- |
100 |
- |
100 |
100 |
| Example 52 % dissolved |
0 |
0 |
0 |
- |
0 |
- |
65.8 |
- |
100 |
100 |
| Example 53 % dissolved |
0 |
0 |
0 |
- |
2.7 |
- |
96.8 |
- |
100 |
100 |
| Example 54 % dissolved |
0 |
- |
9.2 |
56.9 |
100 |
100 |
100 |
100 |
- |
- |
| Example 55 % dissolved |
0 |
- |
17.3 |
50.6 |
64.6 |
66.7 |
100 |
100 |
- |
- |
| Example 56 % dissolved |
0 |
0 |
0 |
0 |
14.9 |
40.8 |
60.6 |
- |
- |
- |
| Example 57 % dissolved |
0 |
0 |
0 |
- |
0 |
- |
66.7 |
- |
100 |
100 |
[0237] The results indicated that the inclusion of a disintegrant in the core can lead to
a more rapid release of the active agent from the formulation.
EXAMPLES 58-60
[0238] In Examples 58-60, prednisolone tablets were prepared having core formulations of
Example 24 and coating formulations as described Examples 2, 4, and a combination
Examples 2 and 4 (25% of Example 2 and 75% of Example 4). Each tablet had the same
core weight, same coating weight, and the same total tablet weight. The tablet formulations
of Examples 58-60 are listed in Table 51 below:
Table 51
| Component |
Ex. 58 |
Ex. 59 |
Ex. 60 |
| |
amt. (mg) |
amt. (mg) |
amt. (mg) |
| 1. Core (Ex. 24) |
50 |
50 |
50 |
| 2. Example 2 coating |
250 |
- |
- |
| 3. Example 4 coating |
- |
250 |
- |
| 4. Coating consisting of 25% of Example 2 and 75% of Example 4 coatings |
- |
- |
250 |
| Total tablet weight |
300 |
300 |
300 |
[0239] Tablets having the formulations described in Examples 58-60 were subjected to dissolution
testing using the USP apparatus type 3 with 250 ml DI water at 15 dips per minute.
The results are set forth in Table 52 below.
Table 52
| Ex. 58 |
Ex. 59 |
Ex. 60 |
| Time (hr) |
% Dissolved |
Time (hr) |
% Dissolved |
Time (hr) |
% Dissolved |
| 0 |
0 |
0 |
0 |
0 |
0 |
| 8 |
3 |
2 |
0 |
4 |
0.3 |
| 10 |
6.9 |
3 |
0 |
6 |
4 |
| 12 |
23.8 |
4 |
59.4 |
8 |
39.6 |
| 14 |
52.3 |
5 |
99.6 |
10 |
99.4 |
| 16 |
99 |
6 |
100 |
12 |
100 |
| 20 |
100 |
7 |
100 |
14 |
100 |
EXAMPLE 61
[0240] In Example 61, prednisolone tablets having the formulations described in Examples
59 were subjected to dissolution variations in pH, ionic strength, and dip rates.
The pH evaluated was 1.5, 7.5 and pH change.
[0241] The pH change method uses increasing pH from one dissolution vessel to the next to
simulate the transport of the dosage form through the gastrointestinal tract. Initially
the pH is 1.5 for 1 hour. The pH of the second station is 3.5 for two additional hours
and then the third station is 5.5 for an additional 2 hours. Finally the last three
stations are at pH 7.5. The time length for the last three stations can vary depending
on the expected release for the dosage form.
[0242] The results are set forth in Tables 53 and 54 below. The results indicate that the
dissolution profiles for a formulation prepared in accordance with Example 59 where
the dissolution media pH and ionic strength were varied.
TABLE 53
| Time |
pH 1.5 (0.25 M) |
pH7.5 (0.01 M) |
pH 7.5 (0.1 M) |
pH 7.5 (0.25 M) |
pH Change (0.1 M) |
| 0 |
0 |
0 |
0 |
0 |
0 |
| 1 |
0 |
0 |
0 |
0 |
0 |
| 3 |
9.3 |
98.1 |
5.9 |
3 |
0 |
| 5 |
20.8 |
100 |
28.9 |
8.8 |
0 |
| 10 |
44.6 |
100 |
88.1 |
42.8 |
11.2 |
| 15 |
87.9 |
100 |
92 |
93.9 |
70 |
| 20 |
100 |
100 |
100 |
95 |
100 |
TABLE 54
| Time |
pH Change No Ions |
| 0 |
0 |
| 1 |
0 |
| 3 |
0 |
| 5 |
0 |
| 7 |
7.7 |
| 9 |
17.7 |
| 11 |
100 |
[0243] The results set forth in Tables 55 and 56 below provide the normalized mean dissolution
profiles for a formulation prepared in accordance with Example 59 using the pH change
method (0.1 M) at 15 and 30 dpm, respectively.
TABLE 55
| Normalized mean values using pH change method (0.1 M) at 15 dpm |
| Normalized Mean |
Normalized SD |
Normalized % CV |
| 0.0 |
0.0 |
#DIV/0! |
| 0.0 |
0.0 |
#DIV/0! |
| 0.0 |
0.0 |
#DIV/0! |
| 0.0 |
0.0 |
#DIV/0! |
| 11.2 |
0.7 |
6.0 |
| 70.0 |
36.7 |
52.4 |
| 100.0 |
0.0 |
0.0 |
TABLE 56
| Normalized mean values using pH change method (0.1M) at 30 dpm |
| Normalized Mean |
Normalized SD |
Normalized % CV |
| 0.0 |
0.0 |
#DIV/0! |
| 0.0 |
0.0 |
#DIV/0! |
| 0.0 |
0.0 |
#DIV/0! |
| 16.7 |
40.8 |
244.9 |
| 100.0 |
0.0 |
0.0 |
| 100.0 |
0.0 |
0.0 |
| 100.0 |
0.0 |
0.0 |
EXAMPLE 62
[0244] In Example 62, a 2 mg prednisolone core composition was prepared similarly to Example
24, increasing the amount of prednisolone in the core and decreasing the amount of
Prosolve SMCC 90, and having the following formulation listed in Table 57:
Table 57
| Component |
Percent |
amt. (mg) |
| 1. Prednisolone |
4 |
2.0 |
| 2. Prosolv SMCC™ 50 |
40 |
20.0 |
| 3. Prosolv SMCC™ 90 |
45.75 |
22.875 |
| 4. Explotab® |
6 |
3.0 |
| 5. Sodium carboxymethylcellulose |
2 |
1.0 |
| 6. Talc |
2 |
1.0 |
| 7. Pruv |
0.25 |
0.125 |
| Total |
100 |
50 |
| Core size and shape |
3/16 Round SC |
EXAMPLE 63-68
[0245] In Examples 63-68, the core formulation of Example 62 was coated with coatings prepared
in accordance with Examples 11, 12, 13, 14, 15, and 16. The formulations of Examples
are listed in Table 58 below:
TABLE 58
| Component |
Ex. 63 |
Ex. 64 |
Ex. 65 |
Ex. 66 |
Ex. 67 |
Ex. 68 |
| |
amt. (mg) |
amt. (mg) |
amt. (mg) |
amt. (mg) |
amt. (mg) |
amt. (mg) |
| 1. Core (Ex. 62) |
50 |
50 |
50 |
50 |
50 |
50 |
| 2. Ex. 11 coating |
250 |
- |
- |
- |
- |
- |
| 3. Ex. 12 coating |
- |
250 |
- |
- |
- |
- |
| 4. Ex. 13 coating |
- |
- |
250 |
- |
- |
- |
| 5. Ex. 14 coating |
- |
- |
- |
250 |
- |
- |
| 6. Ex. 15 coating |
- |
- |
- |
- |
250 |
- |
| 7. Ex. 16 coating |
- |
- |
- |
- |
- |
250 |
| Total tablet weight |
300 |
300 |
300 |
300 |
300 |
300 |
[0246] Dissolution testing was done on each formulation using USP apparatus 3 with 250 ml
of media and 15 dpm. Two dissolution methods using different media (1) DI water and
(2) pH change were performed. Table 59 provides the DI water dissolution results,
and Table 60 provides the pH change (0.1M) dissolution results.
TABLE 59
| Time (hr.) |
Ex. 63 (30% Gums) |
Ex.64 (22.5% Gums) |
Ex. 65 (20% Gums) |
Ex. 66 (15% Gums) |
Ex. 67 (10% Gums) |
Ex. 68 (7.5% Gums) |
| 0 |
0 |
0 |
0 |
0 |
0 |
0 |
| 1 |
0 |
1.2 |
0 |
0 |
0 |
0 |
| 1.5 |
0 |
33.4 |
0 |
30.8 |
64.5 |
98.8 |
| 2 |
30.1 |
98.6 |
64.5 |
99.3 |
98.4 |
100 |
| 2.5 |
98.7 |
100 |
99.5 |
100 |
100 |
100 |
| 3 |
100 |
100 |
100 |
100 |
100 |
100 |
| 3.5 |
100 |
100 |
100 |
100 |
100 |
100 |
TABLE 60
| Time (hr.) |
Ex. 63 (30% Gums) |
Ex. 64 (22.5% Gums) |
Ex. 65 (20% Gums) |
Ex.66 (15% Gums) |
Ex. 67 (10% Gums) |
Ex. 68 (7.5% Gums) |
| 0 |
0 |
0 |
0 |
0 |
0 |
0 |
| 1 |
0 |
0.8 |
0 |
0 |
0 |
32 |
| 3 |
5.8 |
1 |
0 |
0.8 |
0.7 |
98.9 |
| 5 |
6.7 |
3.4 |
3.3 |
5.6 |
91.3 |
100 |
| 8 |
10.8 |
19.4 |
11 |
96.8 |
100 |
100 |
| 11 |
15.7 |
37.6 |
69.5 |
100 |
100 |
100 |
| 14 |
67.8 |
93 |
100 |
100 |
100 |
100 |
[0247] Analysis of the data allows for the approximation of the lag time based a linear
fit of the data obtained. The data demonstrates the lag time can be varied from 0
to 8 hours depending on gum level in the formulation. Table 61 is a summary of the
Example and gum ratio (%) used and the approximated lag time before release.
Table 61
| Approximated Lag Time Before Release |
| Example Number |
Gum Ratio (%) |
Lag Time (Hours) |
| 68 |
7.5 |
0.7 |
| 67 |
10.0 |
1.7 |
| 66 |
15.0 |
3.6 |
| 65 |
20.0 |
5.0 |
| 64 |
22.5 |
7.4 |
| 63 |
30.0 |
9.2 |
EXAMPLE 69
[0248] In Example 69, other formulations were prepared and tested using USP apparatus Type
3, with 250 ml of the dissolution media and dips per minute as indicated in the Table
62.
[0249] The particular dissolution media are defined as follows:
| DI water: |
USP purified water; |
| pH change or |
|
| pH change NI ("no ion"): |
pH change method as described in Example 61, without the use of ions to change adjust
the pH; |
| pH change (0.1M): |
pH change method as described in Example 61 with the use of salts to give an ionic
strength of 0.1molar; |
| pH 7.5: |
dissolution media having a pH of 7.5; |
| pH 7.5 (0.1M): |
dissolution media having a pH of 7.5 and ionic strength of 0.1M; |
| SGI: |
simulated gastric fluid; |
| Peanut oil pH 7.5: |
peanut oil with a pH of 7.5; |
[0250] Other dissolution media indicated would be readily understood by those skilled in
the art (e.g, pH 1,5:dissolution media having a pH of 1.5, etc.) in view of the above.
[0251] With respect to certain excipients indicated in the comments section, these excipients
have been added to the compression coating prior to coating the cores.
TABLE 62
| |
Coating |
Core |
Coating |
Tablet |
Coating |
Dissolution |
Dissol |
Dissolution Time (hrs) (shaded) vs. % Dissolved |
| Test |
Example |
Example |
Amount (mg) |
Weight (mg) |
Size (in.) |
Media |
dpm |
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 1 |
Ex. 14 |
Ex. 22 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
0 |
100 |
100 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
3 |
5 |
7 |
9 |
11 |
| 2 |
Ex. 14 |
Ex. 22 |
250 |
300 |
5/16 |
pH Change NI |
15 |
0 |
0 |
33 |
100 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
3 |
5 |
7 |
9 |
11 |
| 3 |
Ex. 14 |
Ex. 22 |
250 |
300 |
5/16 |
pH Change (0.1M) |
15 |
0 |
0 |
0.8 |
15 |
90 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
4 |
6 |
8 |
10 |
12 |
| 4 |
Ex. 14 |
Ex. 22 |
250 |
300 |
5/16 |
pH 1.5 |
15 |
0 |
0 |
6.3 |
81 |
98 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
4 |
6 |
8 |
10 |
12 |
| 5 |
Ex. 14 |
Ex. 22 |
250 |
300 |
5/16 |
pH 7.5 |
15 |
0 |
0 |
0 |
56 |
95 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
4 |
6 |
8 |
10 |
12 |
| 6 |
Ex. 14 |
Ex. 22 |
180 |
230 |
5/16 |
pH 1.5 (0.1M) |
15 |
0 |
0 |
11 |
98 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
3 |
55 |
7 |
9 |
11 |
| 7 |
Ex. 14 |
Ex. 22 |
180 |
230 |
5/16 |
pH Change |
15 |
0 |
0 |
0 |
81 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 8 |
Ex. 14 |
Ex. 22 |
180 |
230 |
5/16 |
DI Water |
15 |
0 |
0 |
83 |
100 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
5 |
6 |
7 |
8 |
10 |
| 9 |
75% Ex. 2 and 25% Ex. 4 |
Ex. 22 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
0 |
0.9 |
17.1 |
65.1 |
85.8 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 10 |
75% Ex. 2 and 25% Ex. 4 |
Ex. 22 |
250 |
300 |
5/16 |
DI Water |
30 |
0 |
0 |
50 |
82 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
6 |
8 |
10 |
12 |
14 |
| 11 |
75% Ex. 2 and 25% Ex. 4 |
Ex. 22 |
250 |
300 |
5/16 |
DI Water |
5 |
0 |
0 |
0 |
0 |
0 |
2.7 |
7.8 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
4 |
6 |
8 |
10 |
12 |
| 12 |
75% Ex. 2 and 25% Ex.4 |
Ex. 22 |
250 |
300 |
5/16 |
pH 7.5 (0.1M) |
15 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
8 |
12 |
16 |
20 |
24 |
| 13 |
75% Ex. 2 and 25% Ex. 4 |
Ex. 22 |
250 |
300 |
5/16 |
pH 7.5 (0.01M) |
15 |
0 |
0 |
50 |
100 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
3 |
4 |
5 |
6 |
7 |
| 14 |
75% Ex. 2 and 25% Ex. 4 |
Ex. 24 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
0 |
0 |
7.5 |
16.7 |
35.4 |
50 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
5 |
6 |
7 |
8 |
10 |
| 15 |
75% Ex. 2 and 25% Ex. 4 |
Ex. 22 |
250 |
300 |
5/16 |
Peanut Oil |
15 |
0 |
0 |
0.4 |
80 |
86 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
5 |
6 |
7 |
8 |
10 |
| 16 |
75% Ex. 2 and 25% Ex. 4 |
Ex. 24 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
0 |
0 |
3.7 |
55.8 |
77.8 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
4 |
6 |
8 |
10 |
12 |
| 17 |
Ex. 2 |
Ex. 24 |
170 |
220 |
9/32 |
DI Water |
15 |
0 |
0 |
0 |
0 |
0 |
0 |
17 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
4 |
6 |
8 |
10 |
12 |
| 18 |
Ex. 2 |
Ex. 24 |
170 |
220 |
9/32 |
DI Water |
15 |
0 |
0 |
0 |
0 |
0 |
17 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
4 |
6 |
8 |
10 |
14 |
| 19 |
Ex. 2 |
Ex. 24 |
170 |
220 |
9/32 |
DI Water |
15 |
0 |
0 |
0 |
0 |
0 |
0 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
4 |
6 |
8 |
10 |
14 |
| 20 |
Ex. 2 |
Ex. 24 |
170 |
220 |
9/32 |
DI Water |
15 |
0 |
0 |
0 |
0 |
0 |
0 |
42 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
8 |
9 |
10 |
11 |
12 |
14 |
| 21 |
Ex. 2 |
Ex. 24 |
170 |
220 |
9/32 |
DI Water |
15 |
0 |
0 |
0 |
22 |
84 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
8 |
9 |
10 |
11 |
12 |
14 |
| 22 |
Ex. 2 |
Ex. 24 |
170 |
220 |
9/32 |
DI Water |
15 |
0 |
0 |
1.8 |
1.8 |
42 |
62 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
16 |
18 |
20 |
22 |
24 |
26 |
| 23 |
Ex. 10 |
Ex. 24 |
450 |
500 |
3/8 |
pH 1.5 |
15 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
6 |
8 |
10 |
12 |
14 |
16 |
| 24 |
Ex. 10 |
Ex. 24 |
450 |
500 |
3/8 |
pH 7.5 |
15 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
6 |
8 |
10 |
12 |
14 |
16 |
| 25 |
Ex. 10 |
Ex. 24 |
450 |
500 |
3/8 |
pH 1.5 |
15 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
6 |
8 |
10 |
12 |
14 |
16 |
| 26 |
Ex. 10 |
Ex. 24 |
450 |
500 |
3/8 |
pH 7.5 |
15 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
6 |
8 |
10 |
12 |
14 |
16 |
| 27 |
Ex. 10 |
Ex. 24 |
450 |
500 |
3/8 |
pH 1.5 |
15 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
6 |
8 |
10 |
12 |
14 |
16 |
| 28 |
Ex. 10 |
Ex. 24 |
450 |
500 |
3/8 |
pH 7.5 |
15 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
6 |
8 |
10 |
12 |
14 |
16 |
| 29 |
Ex. 10 |
Ex. 24 |
450 |
500 |
3/8 |
pH 1.5 |
15 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
6 |
8 |
10 |
12 |
14 |
16 |
| 30 |
Ex. 10 |
Ex. 24 |
450 |
500 |
3/8 |
pH 1.5 |
15 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
6 |
8 |
10 |
12 |
14 |
16 |
| 31 |
Ex. 10 |
Ex. 24 |
450 |
500 |
3/8 |
pH 1.5 |
15 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
8 |
10 |
12 |
14 |
16 |
18 |
| 32 |
Ex. 6 |
Ex. 24 |
450 |
500 |
3/8 |
DI Water |
15 |
0 |
1.6 |
6.9 |
13 |
46 |
67 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
8 |
10 |
12 |
14 |
16 |
18 |
| 33 |
Ex. 6 |
Ex. 24 |
450 |
500 |
3/8 |
DI Water |
15 |
0 |
0 |
0 |
0 |
3.3 |
4.9 |
37 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
8 |
10 |
12 |
14 |
16 |
18 |
| 34 |
Ex. 6 |
Ex. 24 |
450 |
500 |
3/8 |
DI Water |
15 |
0 |
0 |
0 |
0 |
0 |
2.3 |
|
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
8 |
10 |
12 |
14 |
16 |
18 |
| 35 |
Ex. 6 |
Ex. 24 |
450 |
500 |
3/8 |
DI Water |
15 |
0 |
0 |
0 |
0 |
0 |
64 |
67 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
8 |
10 |
12 |
14 |
16 |
18 |
| 36 |
Ex. 6 |
Ex. 24 |
450 |
500 |
3/8 |
DI Water |
15 |
0 |
4.8 |
10 |
16 |
56 |
99 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
8 |
10 |
12 |
14 |
16 |
18 |
| 37 |
Ex. 6 |
Ex. 24 |
450 |
500 |
3/8 |
ID Water |
15 |
0 |
4.8 |
10 |
16 |
56 |
99 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
10 |
14 |
16 |
18 |
20 |
22 |
| 38 |
Ex. 6 |
Ex. 24 |
450 |
500 |
3/8 |
DI Water |
15 |
0 |
7.3 |
17 |
47 |
62 |
99 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
12 |
14 |
16 |
18 |
20 |
24 |
| 39 |
Ex. 10 |
Ex. 24 |
450 |
500 |
3/8 |
DI Water |
15 |
0 |
2.9 |
5.1 |
7.6 |
10 |
27 |
73 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 40 |
Ex. 10 |
Ex. 24 |
450 |
500 |
3/8 |
DI Water |
15 |
0 |
0 |
0.5 |
0.5 |
0.5 |
99 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
10 |
14 |
16 |
18 |
20 |
22 |
| 41 |
Ex. 6 |
Ex. 24 |
450 |
500 |
3/8 |
DI Water |
115 |
0 |
4.1 |
13 |
40 |
69 |
83 |
83 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
3 |
4 |
5 |
6 |
7 |
8 |
| 42 |
Ex. 10 |
Ex. 25 |
450 |
500 |
3/8 |
DI Water |
15 |
0 |
0 |
0 |
0 |
8.3 |
112 |
12 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
8 |
12 |
16 |
20 |
24 |
| 43 |
Ex. 10 |
Ex. 25 |
450 |
500 |
3/8 |
pH 1.5 |
15 |
0 |
0 |
0 |
0 |
0 |
0 |
14 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
3 |
4 |
5 |
6 |
7 |
8 |
| 44 |
Ex. 10 |
Ex. 28 |
450 |
500 |
3/8 |
DI Water |
15 |
0 |
0 |
0 |
74 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
3 |
4 |
5 |
6 |
7 |
8 |
| 45 |
Ex. 10 |
Ex. 26 |
450 |
500 |
3/8 |
DI Water |
15 |
0 |
0 |
0 |
78 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
8 |
12 |
16 |
20 |
24 |
| 46 |
Ex. 10 |
Ex. 28 |
450 |
500 |
3/8 |
pH 1.5 |
15 |
0 |
0 |
0 |
0 |
0 |
0 |
29 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
8 |
12 |
16 |
20 |
24 |
| 47 |
Ex. 10 |
Ex. 26 |
450 |
500 |
3/8 |
pH 1.5 |
15 |
0 |
0 |
0 |
0 |
0 |
0 |
16 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
3 |
4 |
5 |
6 |
7 |
8 |
| 48 |
Ex. 10 |
Ex. 27 |
450 |
500 |
3/8 |
DI Water |
15 |
0 |
0 |
0 |
15 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
6 |
8 |
10 |
12 |
16 |
| 49 |
Ex. 2 |
Ex. 27 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
0 |
0 |
0 |
0 |
16 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
6 |
8 |
10 |
12 |
18 |
| 50 |
Ex. 2 |
Ex. 28 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
0 |
0.5 |
0.5 |
0.5 |
0.5 |
38 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
8 |
12 |
16 |
20 |
24 |
| 51 |
Ex. 2 |
Ex. 27 |
250 |
300 |
5/16 |
pH 1.5 |
15 |
0 |
0 |
0 |
0 |
0 |
0 |
12 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
8 |
12 |
16 |
20 |
24 |
| 52 |
Ex. 2 |
Ex. 28 |
250 |
300 |
5/16 |
pH 1.5 |
15 |
0 |
0 |
0 |
0 |
0 |
0 |
15 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
8 |
12 |
16 |
20 |
24 |
| 53 |
Ex. 10 |
Ex. 27 |
450 |
500 |
3/8 |
pH 1.5 |
15 |
0 |
0 |
0 |
0 |
0 |
1.9 |
26 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
4.5 |
5 |
5.5 |
6 |
7 |
| 54 |
Ex.10 |
Ex. 31 |
450 |
500 |
3/8 |
DI Water |
15 |
0 |
8.6 |
25.3 |
32.3 |
66.7 |
82.9 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
3 |
4 |
5 |
6 |
7 |
8 |
| 55 |
Ex. 10 |
Ex. 29 |
450 |
500 |
3/8 |
DI Water |
15 |
0 |
0 |
0 |
2.7 |
97 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
4 |
6 |
8 |
12 |
20 |
| 56 |
Ex. 10 |
Ex. 31 |
450 |
500 |
3/8 |
pH ChanGe |
15 |
0 |
0 |
0 |
0 |
0 |
0 |
16 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
4 |
5 |
6 |
12 |
20 |
| 57 |
Ex. 10 |
Ex. 29 |
450 |
500 |
3/8 |
pH Change |
15 |
0 |
0 |
0 |
0 |
0 |
0 |
18 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
4 |
6 |
18 |
22 |
26 |
| 58 |
Ex. 10 |
Ex. 29 |
450 |
500 |
3/8 |
pH Change |
15 |
0 |
0 |
0 |
0 |
19 |
19 |
88 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
4.5 |
5 |
5.5 |
6 |
6.5 |
| 59 |
Ex. 10 |
Ex. 18 |
450 |
500 |
3/8 |
DI Water |
15 |
0 |
9.2 |
57 |
100 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
4 |
6 |
18 |
22 |
26 |
| 60 |
Ex. 10 |
Ex. 31 |
450 |
500 |
3/8 |
pH Change |
15 |
0 |
0 |
0 |
0 |
19 |
19 |
23 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
3 |
4 |
4.5 |
5 |
5.5 |
6 |
| 61 |
Ex. 10 |
Ex. 31 |
450 |
500 |
3/8 |
DI Water |
15 |
0 |
0 |
0 |
0 |
15 |
41 |
61 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
4 |
6 |
16 |
20 |
24 |
| 62 |
Ex. 10 |
Ex. 31 |
450 |
500 |
3/8 |
pH Change |
15 |
0 |
0 |
0 |
0 |
0 |
33 |
33 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
4 |
6 |
16 |
20 |
24 |
| 63 |
Ex. 10 |
Ex. 31 |
450 |
500 |
3/8 |
pH Change |
15 |
0 |
0 |
0 |
0 |
0 |
33 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
4 |
6 |
16 |
20 |
24 |
| 64 |
Ex. 10 |
Ex. 31 |
450 |
500 |
3/8 |
pH Change |
15 |
0 |
0 |
0 |
0 |
11 |
13 |
48 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
4 |
6 |
16 |
20 |
24 |
| 65 |
Ex. 10 |
Ex. 29 |
450 |
500 |
3/8 |
pH Change |
15 |
0 |
0 |
0 |
0 |
11 |
11 |
69 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
3 |
4 |
5 |
6 |
7 |
8 |
| 66 |
Ex. 10 |
Ex. 31 |
450 |
500 |
3/8 |
DI Water |
15 |
0 |
0 |
0 |
0 |
67 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
4 |
6 |
16 |
20 |
24 |
| 67 |
Ex. 10 |
Ex. 35 |
450 |
500 |
3/8 |
pH Change |
15 0 |
0 |
0 |
0 |
0 |
7.1 |
37 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
4 |
6 |
16 |
20 |
24 |
| 68 |
Ex. 10 |
Ex. 32 |
450 |
500 |
3/8 |
pH Change 15 |
|
0 |
0 |
0 |
0 |
150 |
28 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
4 |
6 |
16 |
20 |
24 |
| 69 |
Ex. 10 |
Ex. 34 |
450 |
500 |
3/8 |
pH Change |
15 |
0 |
0 |
0 |
0 |
0 |
18 |
70 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
3 |
4 |
5 |
6 |
7 |
8 |
| 70 |
Ex. 10 |
Ex. 24 |
450 |
500 |
3/8 |
pH 1.5 |
15 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
3 |
4 |
5 |
6 |
7 |
| 71 |
Ex. 10 |
Ex. 24 |
450 |
500 |
3/8 |
pH 5.5 |
15 |
0 |
0 |
0 |
0 |
52 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
3 |
4 |
5 |
6 |
7 |
| 72 |
Ex. 10 |
Ex. 24 |
450 |
500 |
3/8 |
pH 7.5 |
15 |
0 |
0 |
0 |
0 |
20 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
3 |
4 |
5 |
6 |
7 |
| 73 |
Ex. 10 |
Ex. 24 |
450 |
500 |
3/8 |
pH 7.5 Buffer |
15 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
3 |
4 |
5 |
6 |
7 |
8 |
| 74 |
Ex. 10 |
Ex. 24 |
450 |
500 |
3/8 |
pH 3.5 |
15 |
0 |
0 |
0 |
0 |
65 |
95 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
3 |
4 |
5 |
6 |
7 |
8 |
| 75 |
Ex. 10 |
Ex. 24 |
450 |
500 |
3/8 |
pH 5.5 |
15 |
0 |
0 |
0 |
0 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
3 |
5 |
7 |
9 |
11 |
| 76 |
Ex. 10 |
Ex. 24 |
450 |
500 |
3/8 |
pH Change 15 |
15 |
0 |
0 |
0 |
0 |
0 |
78 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
3 |
4 |
5 |
6 |
7 |
8 |
| 77 |
Ex. 10 |
Ex. 24 |
450 |
500 |
3/8 |
SGI |
15 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
8 |
10 |
12 |
14 |
16 |
18 |
| 78 |
Ex. 10 |
Ex. 24 |
450 |
500 |
3/8 |
pH 1.5 |
15 |
0 |
0 |
0 |
0 |
0 |
0 |
57 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
8 |
10 |
12 |
14 |
16 |
18 |
| 79 |
Ex. 10 |
Ex. 24 |
450 |
500 |
3/8 |
pH 1.5 |
30 |
0 |
0 |
0 |
49 |
49 |
49 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
8 |
10 |
12 |
14 |
16 |
18 |
| 80 |
Ex. 10 |
Ex. 24 |
450 |
500 |
3/8 |
pH 7.5 |
15 |
0 |
0 |
0 |
0 |
0 |
0 |
45 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
8 |
10 |
12 |
14 |
16 |
18 |
| 81 |
Ex. 10 |
Ex. 24 |
450 |
500 |
3/8 |
pH 7.5 |
30 |
0 |
0 |
12 |
41 |
41 |
41 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
4 |
6 |
8 |
10 |
12 |
| 82 |
Ex. 10 |
Ex. 24 |
450 |
500 |
3/8 |
Peanut Oil pH 1.5 |
15 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
4 |
6 |
8 |
10 |
12 |
| 83 |
Ex. 10 |
Ex. 24 |
450 |
500 |
3/8 |
Peanut Oil pH 7.5 |
15 |
0 |
0 |
0 |
100 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
4 |
5 |
6 |
7 |
8 |
| 84 |
Ex. 1 |
Ex. 24 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
0 |
86 |
100 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
3 |
4 |
5 |
6 |
7 |
| 85 |
Ex. 10 |
Ex. 24 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
0 |
0 |
18 |
97 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
8 |
9 |
10 |
11 |
12 |
14 |
| 86 |
Ex. 10 |
Ex. 24 |
400 |
450 |
5/16 |
DI Water |
5 |
0 |
0 |
16 |
37 |
99 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
3 |
4 |
5 |
6 |
7 |
| 87 |
Ex. 10 |
Ex. 24 |
400 |
450 |
5/16 |
DI Water |
15 |
0 |
0 |
0 |
0 |
98 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
4.5 |
5 |
5.5 |
6 |
6.8 |
| 88 |
Ex. 10 |
Ex. 24 |
450 |
500 |
3/8 |
DI Water |
15 |
0 |
0 |
0 |
0 |
51 |
83 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
6 |
7 |
8 |
9 |
10 |
11 |
| 89 |
Ex. 10 |
Ex. 24 |
550 |
600 |
7/16 |
DI Water |
10 |
0 |
0 |
0 |
89 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
5 |
5.5 |
6 |
6.5 |
7 |
7.5 |
| 90 |
Ex. 10 |
Ex. 24 |
550 |
600 |
7/16 |
DI Water |
15 |
0 |
0 |
11.5 |
87.1 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
10 |
10.5 |
11 |
11.5 |
12 |
12.5 |
| 91 |
Ex. 10 |
Ex. 24 |
450 |
500 |
3/8 |
DI Water |
5 |
0 |
0 |
0 |
4.3 |
49.1 |
97.1 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
7 |
8 |
9 |
10 |
11 |
12 |
| 92 |
Ex. 10 |
Ex. 24 |
450 |
500 |
3/8 |
DI Water |
10 |
0 |
0 |
45.4 |
56.7 |
83.3 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
5 |
5.5 |
5.75 |
6 |
6.25 |
6.75 |
| 93 |
Ex.10 |
Ex. 24 |
450 |
500 |
3/8 |
DI Water |
15 |
0 |
0 |
33.3 |
33.3 |
66.7 |
83.3 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
3 |
3.5 |
4 |
4.5 |
5 |
5.5 |
| 94 |
Ex. 10 |
Ex. 24 |
450 |
500 |
3/8 |
DI Water |
20 |
0 |
0 |
0 |
39 |
99.3 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
3 |
4 |
5 |
6 |
7 |
| 95 |
Ex. 10 |
Ex. 22 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
0 |
0 |
67 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
4 |
6 |
8 |
10 |
16 |
| 96 |
Ex. 2 |
Ex. 20 |
850 |
900 |
1/2 |
DI Water |
15 |
0 |
37 |
48 |
48 |
48 |
48 |
98 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
4 |
6 |
8 |
10 |
16 |
| 97 |
Ex. 3 |
Ex. 20 |
250 |
300 |
3/8 |
DI Water |
15 |
0 |
0.8 |
42 |
42 |
97 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
6 |
8 |
10 |
12 |
16 |
| 98 |
Ex. 2 |
Ex. 21 |
250 |
300 |
3/8 |
DI Water |
15 |
0 |
0 |
0 |
0 |
0 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
6 |
8 |
10 |
12 |
16 |
| 99 |
Ex. 2 |
Ex. 21 |
350 |
400 |
3/8 |
DI Water |
15 |
0 |
0 |
0 |
0 |
0 |
20 |
20 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
3 |
3 |
4 |
5 6 |
|
8 |
| 100 |
Ex. 2 |
Ex. 21 |
150 |
200 |
9/32 |
DI Water |
15 |
0 |
17 |
17 |
23 |
36 |
41 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
3 |
4 |
5 |
6 |
8 |
| 101 |
Ex. 2 |
Ex. 19 |
150 |
200 |
9/32 |
DI Water |
15 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
5 |
6 |
8 |
10 |
12 |
| 102 |
Ex. 3 |
Ex. 19 |
150 |
200 |
9/32 |
DI Water |
15 |
0 |
55.8 |
55.6 |
66.7 |
66.7 |
85.7 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
6 |
8 |
10 |
12 |
16 |
| 103 |
Ex. 3 |
Ex. 19 |
250 |
300 |
3/8 |
DI Water |
15 |
0 |
0 |
100 |
100 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
6 |
8 |
10 |
12 |
16 |
| 104 |
Ex. 3 |
Ex. 19 |
250 |
300 |
3/8 |
DI Water |
15 |
0 |
0 |
0 |
18 |
52 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
6 |
8 |
10 |
12 |
16 |
| 105 |
Ex. 2 |
Ex. 19 |
150 |
200 |
9/32 |
DI Water |
15 |
0 |
0 |
0 |
0 |
0 |
46 |
67 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
6 |
8 |
10 |
12 |
16 |
| 106 |
Ex. 2 |
Ex. 22 |
175 |
225 |
9/32 |
DI Water |
15 |
0 |
0 |
0 |
0 |
0 |
25 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
6 |
8 |
10 |
12 |
16 |
| 107 |
Ex. 2 |
Ex. 22 |
170 |
220 |
9/32 |
DI Water |
15 |
0 |
0 |
0 |
0 |
0 |
17 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
14 |
15 |
16 |
17 |
18 |
19 |
| 108 |
Ex. 2 |
Ex. 23 |
355 |
525 |
5/16 |
DI Water |
15 |
0 |
7.5 |
55 |
100 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
14 |
14 |
15 |
15 |
16 |
16 |
| 109 |
Ex. 2 |
Ex. 23 |
390 |
560 |
5/16 |
DI Water |
15 |
0 |
35 |
56 |
76 |
80 |
93 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
12 |
13 |
14 |
15 |
16 |
17 |
| 110 |
Ex. 2 |
Ex. 23 |
330 |
500 |
3/8 |
DI Water |
15 |
0 |
11 |
33 |
52 |
75 |
90 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
8 |
10 |
12 |
14 |
16 |
18 |
| 111 |
Ex. 2 |
Ex. 24 |
250 |
300 |
7/16 |
DI Water |
15 |
0 |
0 |
0 |
0 |
0 |
0 |
33 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
8 |
10 |
12 |
14 |
16 |
18 |
| 112 |
Ex. 2 |
Ex. 24 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
3 |
6.6 |
11 |
16 |
34 |
87 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
8 |
10 |
12 |
14 |
16 |
20 |
| 113 |
Ex. 2 |
Ex. 31 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
1.1 |
5.9 |
44 |
92 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
6 |
8 |
10 |
12 |
16 |
| 114 |
Ex. 3 |
Ex. 21 |
350 |
400 |
3/8 |
DI Water |
15 |
0 |
0 |
0 |
0 |
6.8 |
34 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
6 |
8 |
10 |
12 |
16 |
| 115 |
Ex. 3 |
Ex. 21 |
250 |
300 |
3/8 |
DI Water |
15 |
0 |
0 |
0 |
0 |
36 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
3 |
4 |
5 |
6 |
8 |
| 116 |
Ex. 2 |
Ex. 19 |
150 |
200 |
9/32 |
DI Water |
15 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
6 |
8 |
10 |
12 |
16 |
| 117 |
Ex. 2 |
Ex. 19 |
150 |
200 |
9/32 |
DI Water |
15 |
0 |
0 |
0 |
0 |
20 |
67.7 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
6 |
8 |
10 |
12 |
16 |
| 118 |
Ex. 3 |
Ex. 19 |
250 |
300 |
3/8 |
DI Water |
15 |
0 |
100 |
100 |
100 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
6 |
8 |
10 |
12 |
16 |
| 119 |
Ex. 2 |
Ex. 19 |
250 |
300 |
3/8 |
DI Water |
15 |
0 |
0 |
0 |
18 |
52 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
6 |
8 |
10 |
12 |
16 |
| 120 |
Ex. 3 |
Ex. 19 |
170 |
220 |
9/32 |
DI Water |
15 |
0 |
0 |
30 |
65 |
95 |
95 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
4 |
6 |
8 |
10 |
12 |
| 121 |
Ex. 3 |
Ex. 19 |
170 |
220 |
9/32 |
pH Change |
15 |
0 |
0 |
0 |
0 |
0 |
0 |
5 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
6 |
8 |
10 |
12 |
14 |
18 |
| 122 |
Ex. 3 |
Ex. 24 |
450 |
500 |
5/16 |
DI Water |
15 |
0 |
0 |
33 |
33 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
4 |
6 |
8 |
10 |
14 |
| 123 |
Ex. 3 |
Ex. 24 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
0 |
0 |
2.6 |
25 |
68 |
91 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
3 |
4 |
5 |
6 7 |
|
| 124 |
Ex. 9 |
Ex. 24 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
0 |
0 |
32 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
3 |
4 |
5 |
6 |
7 |
| 125 |
Ex. 9 |
Ex. 24 |
450 |
1500 |
3/8 |
DI Water |
15 |
0 |
0 |
0 |
0 |
0.7 |
86 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
3 |
4 |
5 |
6 |
7 |
| 126 |
Ex. 4 |
Ex. 24 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
0 |
22 |
100 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
3 |
4 |
5 |
6 |
7 |
| 127 |
Ex. 4 |
Ex. 24 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
11 |
73 |
100 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
3 |
3.5 |
4 |
4.5 |
5 |
5.5 |
| 128 |
Ex. 4 |
Ex. 22 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
0 |
52 |
100 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
3 |
53.7 |
3.8 |
4 |
4.2 |
4.3 |
| 129 |
Ex. 4 |
Ex. 22 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
0 |
23 |
36 |
45 |
64 |
97 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
3 |
3.5 |
4 |
4.5 |
5 |
5.5 |
| 130 |
Ex. 4 |
Ex. 22 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
3.8 |
74 |
100 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
3 |
4 |
5 |
6 |
7 |
| 131 |
Ex. 4 |
Ex. 22 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
0 |
8.1 |
55 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
0 |
1 |
3 |
5 |
7 |
9 |
11 |
| 132 |
Ex. 4 |
Ex. 22 |
250 |
300 |
5/16 |
pH Change No Ion |
15 |
0 |
0 |
0 |
0 |
7.7 |
18 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 133 |
Ex. 4 |
Ex. 22 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
0 |
0 |
0 |
32 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
3 |
5 |
8 |
11 |
14 |
| 134 |
Ex. 4 |
Ex. 22 |
250 |
300 |
5/16 |
pH Chanqe |
15 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
3 |
5 |
8 |
15 |
10 |
| 135 |
Ex. 4 |
Ex. 22 |
250 |
300 |
5/16 |
pH Chanqe |
15 |
0 |
0 |
0 |
0 |
11 |
70 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
3 |
5 |
10 |
15 |
10 |
| 136 |
Ex. 4 |
Ex. 22 |
250 |
300 |
5/16 |
pH Chanqe |
30 |
0 |
0 |
0 |
17 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
4 |
6 |
8 |
10 |
12 |
| 137 |
Ex. 8 |
Ex. 22 |
170 |
220 |
9/32 |
DI Water |
15 |
0 |
92 |
100 |
100 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 138 |
Ex. 8 |
Ex. 24 |
170 |
220 |
9/32 |
DI Water |
15 |
0 |
28 |
100 |
100 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 139 |
Ex. 8 |
Ex. 24 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
0 |
50 |
100 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 140 |
Ex. 7 |
Ex. 24 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
0 |
13.1 |
94.1 |
71.3 |
96 |
96 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 141 |
Ex. 7 |
Ex. 24 |
350 |
400 |
3/8 |
DI Water |
15 |
0 |
0 |
0 |
25 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
4 |
6 |
8 |
10 |
12 |
| 142 |
Ex. 6 |
Ex. 24 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
0 |
100 |
100 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 143 |
Ex. 5 |
Ex. 24 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
0 |
0 |
0 |
0 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
4 |
5 |
6 |
7 |
8 |
| 144 |
Ex. 5 |
Ex. 24 |
400 |
450 |
3/8 |
DI Water |
15 |
0 |
0 |
0 |
0 |
75 |
91 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 145 |
Ex. 6 |
Ex. 24 |
400 |
450 |
3/8 |
DI Water |
15 |
0 |
0 |
0 |
17 |
83 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
8 |
10 |
12 |
14 |
16 |
20 |
| 146 |
50% LBG |
Ex. 24 |
400 |
450 |
3/8 |
DI Water |
15 |
0 |
2.8 |
6 |
9.5 |
57 |
87.3 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
8 |
10 |
12 |
14 |
16 |
20 |
| 147 |
30% LBG |
Ex. 24 |
400 |
1450 |
3/8 |
DI Water |
15 |
0 |
5.7 |
12 |
19 |
38 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
10 |
14 |
16 |
18 |
20 |
22 |
| 148 |
30% LBG |
Ex.24 |
450 |
500 |
|
DI Water |
15 |
0 |
4.1 |
13 |
40 |
69 |
83 |
83 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
3 |
4 |
5 |
6 |
7 |
| 149 |
50% Ex. |
Ex. 22 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
| |
4 and 50% Ex. 2 |
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
3 |
3.5 |
4 |
4.5 |
5 |
6 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| 150 |
Xanthan Gum |
Ex. 22 |
170 |
220 |
9/32 |
DI Water |
15 |
0 |
0 |
0 |
55.9 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 151 |
Xanthan Gum |
Ex. 24 |
170 |
220 |
9/32 |
DI Water |
15 |
0 |
0 |
0 |
0 |
67 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
3 |
4 |
5 |
6 |
7 |
8 |
| 152 |
Xanthan Gum |
Ex. 24 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
0 |
0 |
38 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
3 |
4 |
5 |
6 |
8 |
| 153 |
30% Xanthan Gum |
Ex. 24 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
0 |
80 |
100 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
4 |
6 |
8 |
10 |
12 |
| 154 |
50 % Xanthan Gum |
Ex. 24 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
0 |
0 |
100 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
5 |
5.5 |
6 |
6.5 |
7 |
| 155 |
50 % Xanthan Gum |
Ex. 24 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
2.6 |
99 |
100 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
6 |
8 |
10 |
12 |
14 |
16 |
| 156 |
Xanthan Gum |
Ex. 24 |
250 |
300 |
5/16 |
pH 1.5 |
15 |
0 |
0 |
0 |
0 |
0 |
0 |
5.2 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
3 |
5 |
8 |
11 |
14 |
| 157 |
Ex. 11 |
Ex. 36 |
250 |
300 |
5/16 |
pH Change |
15 |
0 |
0 |
5.8 |
6.7 |
11 |
16 |
68 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
3 |
5 |
8 |
11 |
14 |
| 158 |
Ex. 12 |
Ex. 36 |
250 |
300 |
5/16 |
pH Change |
15 |
0 |
0.8 |
1 |
3.4 |
19 |
38 |
93 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
3 |
5 |
8 |
11 |
14 |
| 159 |
Ex. 14 |
Ex. 36 |
250 |
300 |
5/16 |
pH Change |
15 |
0 |
0 |
0.8 |
5.6 |
97 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
3 |
5 |
8 |
11 |
14 |
| 160 |
Ex. 16 |
Ex. 36 |
250 |
300 |
5/16 |
pH Change |
15 |
0 |
3.2 |
99 |
100 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
0.5 |
1 |
1.5 |
2 |
2.5 |
3 |
| 161 |
Ex. 16 |
Ex. 36 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
0 |
98 |
100 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
0.51 |
|
1.5 |
2 |
2.5 |
3 |
| 162 |
Ex. 14 |
Ex. 36 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
0 |
31 |
99 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
1.5 |
2 |
2.5 |
3 |
3.5 |
| 163 |
Ex. 15 |
Ex. 36 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
1 |
33 |
99 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
1.5 |
2 |
2.5 |
3 |
3.5 |
| 164 |
Ex. 11 |
Ex. 36 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
0 |
0 |
30 |
99 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
3 |
5 |
8 |
11 |
14 |
| 165 |
Ex. 16 |
Ex. 36 |
250 |
300 |
5/16 |
pH 7.5 [0.1M] |
15 |
0 |
0 |
98 |
100 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
3 |
5 |
8 |
11 |
14 |
| 166 |
Ex. 14 |
Ex. 36 |
250 |
300 |
5/16 |
pH 7.5 [0.1M] |
15 |
0 |
0 |
0 |
42 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
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| |
|
|
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|
|
|
0 |
1 |
3 |
5 |
8 |
11 |
14 |
| 167 |
Ex. 12 |
Ex. 36 |
250 |
300 |
5/16 |
pH 7.5 [0.1M] |
15 |
0 |
0 |
0 |
0 |
6.4 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
3 |
5 |
8 |
11 |
14 |
| 168 |
Ex. 11 |
Ex. 36 |
250 |
300 |
5/16 |
pH 7.5 [0.1M] |
15 |
0 |
0 |
0 |
0 |
4.3 |
11 |
97 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
3 |
5 |
8 |
11 |
14 |
| 169 |
Ex. 16 |
Ex. 36 |
250 |
300 |
5/16 |
pH 1.5 [0.1M] |
15 |
0 |
0 |
98 |
100 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
3 |
5 |
8 |
11 |
14 |
| 170 |
Ex. 14 |
Ex. 36 |
250 |
300 |
5/16 |
pH 1.5 [0.1M] |
15 |
0 |
0 |
0 |
33 |
99 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
3 |
5 |
8 |
11 |
14 |
| 171 |
Ex. 12 |
Ex. 36 |
250 |
300 |
5/16 |
pH 1.5 |
15 [0.1M] |
0 |
0 |
0 |
2.2 |
9.6 |
61 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
3 |
5 |
8 |
11 |
14 |
| 172 |
Ex. 11 |
Ex. 36 |
250 |
300 |
5/16 |
pH 1.5 [0.1M] |
15 |
0 |
0 |
0 |
0 |
6 |
13 |
73 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
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|
|
|
|
|
|
|
|
|
| 173 |
Ex. 15 |
Ex. 36 |
250 |
300 |
5/16 |
DI WAter |
15 |
0 |
0 |
65 |
99 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
0.5 |
1 |
1.5 |
2 |
2.5 |
3 |
| 174 |
Ex. 13 |
Ex. 36 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
0 |
0 |
65 |
100 |
100 |
10 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
3 |
5 |
8 |
11 |
14 |
| 175 |
Ex. 15 |
Ex. 36 |
250 |
300 |
5/16 |
pH Change |
15 |
0 |
0 |
0.7 |
91 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
3 |
5 |
8 |
11 |
14 |
| 176 |
Ex. 13 |
Ex. 36 |
250 |
300 |
5/16 |
pH Change |
15 |
0 |
0 |
0 |
3.3 |
11 |
70 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
3 |
5 |
8 |
11 |
14 |
| 177 |
Ex. 15 |
Ex. 36 |
250 |
300 |
5/16 |
pH 7.5 [0.1M] |
15 |
0 |
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
3 |
5 |
8 |
11 |
14 |
| 178 |
Ex. 13 |
Ex. 36 |
250 |
300 |
5/16 |
pH 7.5 [0.1M] |
15 |
0 |
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
3 |
5 |
8 |
11 |
14 |
| 179 |
Ex. 15 |
Ex. 36 |
250 |
300 |
5/16 |
pH 1.5 [0.1M] |
15 |
0 |
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
3 |
5 |
8 |
11 |
14 |
| 180 |
Ex. 13 |
Ex. 36 |
250 |
300 |
5/16 |
pH 1.5 [0.1M] |
15 |
0 |
|
|
|
|
|
|
[0252] Comments:
- 1. Test 9 was average merged data.
- 2. Test 14 was average merged data.
- 3. Test 16 was average merged data.
- 4. Test 17 utilized 5% PVP added to the coating as an additional excipient.
- 5. Test 18 utilized 10% PVP added to the coating as an additional excipient.
- 6. Test 19 utilized 5% MCC added to the coating as an additional excipient.
- 7. Test 20 utilized 5% MCC added to the coating as an additional excipient.
- 8. Test 21 utilized 10% PEG added to the coating as an additional excipient.
- 9. Test 22 utilized 5% PEG added to the coating as an additional excipient.
- 10. Test 23 utilized 10% MCC added to the coating as an additional excipient.
- 11.Test 24 utilized 20% MCC added to the coating as an additional excipient.
- 12.Test 25 utilized 5% PEG added to the coating as an additional excipient.
- 13. Test 26 utilized 5% PEG added to the coating as an additional excipient.
- 14. Test 27 utilized 10% PVP added to the coating as an additional excipient.
- 15. Test 28 utilized 10% PVP added to the coating as an additional excipient.
- 16. Test 29 utilized 10% PEG added to the coating as an additional excipient.
- 17.Test 30 utilized 5% PVP added to the coating as an additional excipient.
- 18. Test 31 utilized 15% PEG added to the coating as an additional excipient.
- 19. Test 32 utilized 5% Calcium Sulfate added to the coating as an additional excipient.
- 20. Test 33 utilized 10% Calcium Sulfate added to the coating as an additional excipient.
- 21. Test 34 utilized 10% Calcium Sulfate added to the coating as an additional excipient.
- 22. Test 35 utilized 30% Calcium Sulfate added to the coating as an additional excipient.
- 23. Test 36 utilized 5% Calcium Sulfate added to the coating as an additional excipient.
- 24. Test 37 utilized 10% Calcium Sulfate added to the coating as an additional excipient.
- 25. Test 38 utilized 30% Calcium Sulfate added to the coating as an additional excipient.
- 26. Test 39 utilized 30% Calcium Sulfate added to the coating as an additional excipient.
- 27. Test 40 utilized 15% PEG added to the coating as an additional excipient.
- 28. Test 41 utilized 305% Calcium Sulfate added to the coating as an additional excipient.
- 29. Test 54 was average merged data.
- 30. Test 90 was average merged data.
- 31. Test 96 was based on two tablets.
- 32. Test 97 was based on two tablets.
- 33. Test 98 was based on three tablets.
- 34. Test 99 was based on three tablets.
- 35. Test 100 was based on six tablets.
- 36. Test 101 was based on three tablets.
- 37. Test 102 was average merged data.
- 38. Test 103 was based on three tablets.
- 39. Test 104 was based on three tablets.
- 40. Test 105 was based on three tablets.
- 41. Test 106 was based on twelve tablets.
- 42. Test 107 was average merged data.
- 43. Test 108 was based on six tablets.
- 44. Test 109 was based on twelve tablets.
- 45. Test 110 was based on twelve tablets.
- 46. Test 111 was based on three tablets.
- 47. Test 112 was based on six tablets.
- 48. Test 113 was based on twelve tablets.
- 49. Test 117 was averaged merged data.
- 50. Test 120 was average merged data.
- 51. Test 140 was average merged data.
- 52. Test 146 was average merged data.
- 53. Test 150 was average merged data.
EXAMPLE 70
[0253] An albuterol core composition was prepared having the formulation ingredients set
forth in Table 63:
TABLE 63
| Component |
Percent |
amt.(mg) |
| |
|
|
| 1. Albuterol |
19.2 |
9.6 |
| 2. Prosolv SMCC™ 50 |
26.8 |
13.4 |
| 3. Prosolve SMCC™ 90 |
41 |
20.63 |
| 4. Silicone dioxide |
0.5 |
0.25 |
| 5. Explotab |
6 |
3 |
| 6. Sodium carboxymethylcellulose |
2 |
1 |
| 7. Talc |
4 |
2 |
| 8. Pruv |
0.25 |
0.13 |
| |
|
|
| Total |
100 |
50 |
| |
|
|
| Core size and shape |
5/16 Round SC |
|
Process:
[0254] The same process for Example 23 is used to prepare the core in Example 70.
EXAMPLE 71
[0255] An albuterol core composition was prepared having the formulation ingredients set
forth in Table 64:
TABLE 64
| Component |
Percent |
amt. (mg) |
| 1. Albuterol |
10 |
9.60 |
| 2. Prosolv SMCC™ 50 |
26.8 |
25.73 |
| 3. Prosolve SMCC™ 90 |
50 |
48.43 |
| 4. Silicone dioxide |
0.5 |
0.48 |
| 5. Explotab |
6 |
5.76 |
| 6. Sodium carboxymethylcellulose |
2 |
1.92 |
| 7. Talc |
4 |
3.84 |
| 8. Pruv |
0.25 |
0.24 |
| |
|
|
| Total |
100 |
96 |
| |
|
|
| Core size and shape |
¼" Round SC |
|
Process:
[0256] The same process for Example 23 is used to prepare the core in Example 71.
EXAMPLE 72
[0257] An albuterol core composition was prepared having the formulation ingredients set
forth in Table 65:
TABLE 65
| Component |
Percent |
amt. (mg) |
| 1. Albuterol |
4.8 |
2.4 |
| 2. Prosolv SMCC™ 50 |
37.2 |
18.6 |
| 3. Prosolve SMCC™ 90 |
48 |
23.88 |
| 4. Explotab |
6 |
3.0 |
| 5. Sodium carboxymethylcellulose |
2 |
1.0 |
| 6. Talc |
2 |
1.0 |
| 7. Pruv |
0.25 |
0.13 |
| |
|
|
| Total |
100 |
50 |
| |
|
|
| Core size and shape |
3/16 Round SC |
|
| |
|
|
Process:
[0258] The same process for Example 23 is used to prepare the core in Example 72.
EXAMPLE 73
[0259] An albuterol core composition was prepared having the formulation ingredients set
forth in Table 66:
TABLE 66
| Component |
Percent |
Amt. (mg) |
| 1. Albuterol |
8.7 |
9.6 |
| 2. Prosolv SMCC™ 50 |
26.8 |
29.48 |
| 3. Prosolve SMCC™ 90 |
52 |
56.89 |
| 4. Silicon Dioxide |
0.5 |
0.55 |
| 5. Explotab |
6 |
6.60 |
| 6. Sodium carboxymethylcellulose |
2 |
2.20 |
| 7. Talc |
4 |
4.40 |
| 8. Pruv |
0.25 |
0.25 |
| Total |
100 |
110 |
| |
|
|
| |
|
|
| Core size and shape |
¼ Round SC |
|
Process:
[0260] The same process for Example 23 is used to prepare the core in Example 73.
EXAMPLE 74
[0261] An albuterol core composition was prepared having the formulation ingredients set
forth in Table 67:
Table 67
| Component |
Percent |
Amt. (mg) |
| 1. Albuterol |
8.7 |
9.6 |
| 2. Prosolv SMCC™ 50 |
26.8 |
29.48 |
| 3. Prosolve SMCC™ 90 |
52 |
56.89 |
| 4. Silicon Dioxide |
0.5 |
0.55 |
| 5. Explotab |
6 |
6.60 |
| 6. Sodium carboxymethylcellulose |
2 |
2.20 |
| 7. Talc |
4 |
4.40 |
| 8. Pruv |
0.25 |
0.25 |
| No coating |
|
|
| Total |
100 |
110 |
| |
|
|
| |
|
|
| Core size and shape |
¼ round SC |
|
Process:
[0262] The same process for Example 23 is used to prepare the core in Example 74.
EXAMPLE 75
[0263] An albuterol core composition was prepared having the formulation ingredients set
forth in Table 68:
Table 68
| Component |
Percent |
Amt. (mg) |
| 1. Albuterol |
8.7 |
9.6 |
| 2. Prosolv SMCC™ 50 |
26.8 |
29.48 |
| 3. Prosolve SMCC™ 90 |
52 |
56.89 |
| 4. Silicon Dioxide |
0.5 |
0.55 |
| 5. Explotab |
6 |
6.60 |
| 6. Sodium carboxymethylcellulose |
2 |
2.20 |
| 7. Talc |
4 |
4.40 |
| 8. Pruv |
0.25 |
0.25 |
| |
|
|
| Total |
100 |
110 |
| Film coating 3% (3.3mg) Opadry AMB |
|
|
| |
|
|
| Core size and shape |
¼ round SC |
|
Process:
[0264] The same process for Example 23 is used to prepare the core, along with a film coating
where applicable (see Table 68) in Example 75.
EXAMPLE 76
[0265] An albuterol core composition was prepared having the formulation ingredients set
forth in Table 69:
Table 69
| Component |
Percent |
Amt. (mg) |
| 1. Albuterol |
8.7 |
9.6 |
| 2. Prosolv SMCC™ 50 |
26.8 |
29.48 |
| 3. Prosolve SMCC™ 90 |
52 |
56.89 |
| 4. Silicon Dioxide |
0.5 |
0.55 |
| 5. Explotab |
6 |
6.60 |
| 6. Sodium carboxymethylcellulose |
2 |
2.20 |
| 7. Talc |
4 |
4.40 |
| 8. Pruv |
0.25 |
0.25 |
| |
|
|
| Total |
100 |
110 |
| Film Coating 6% (6.6 mg) opadry AMB |
|
|
| |
|
|
| Core size and shape |
¼ round SC |
|
Process:
[0266] The same process for Example 23 is used to prepare the core, along with a film coating
where applicable (see Table 69) in Example 76.
EXAMPLE 77
[0267] An albuterol core composition was prepared having the formulation ingredients set
forth in Table 70:
Table 70
| Component |
Percent |
Amt. (mg) |
| 1. Albuterol |
8.7 |
9.6 |
| 2. Prosolv SMCC™ 50 |
26.8 |
29.48 |
| 3. Prosolve SMCC™ 90 |
52 |
56.89 |
| 4. Silicon Dioxide |
0.5 |
0.55 |
| 5. Explotab |
6 |
6.60 |
| 6. Sodium carboxymethylcellulose |
2 |
2.20 |
| 7. Talc |
4 |
4.40 |
| 8. Pruv |
0.25 |
0.25 |
| |
|
|
| Total |
100 |
110 |
| Film coating 3% (3.3 mg) opadry II |
|
|
| |
|
|
| Core size and shape |
¼ round SC |
|
Process:
[0268] The same process for Example 23 is used to prepare the core, along with a film coating
where applicable (see Table 70) in Example 77.
EXAMPLE 78
[0269] An albuterol core composition was prepared having the formulation ingredients set
forth in Table 71:
Table 71
| Component |
Percent |
Amt. (mg) |
| 1. Albuterol |
8.7 |
9.6 |
| 2. Prosolv SMCC™ 50 |
26.8 |
29.48 |
| 3. Prosolve SMCC™ 90 |
52 |
56.89 |
| 4. Silicon Dioxide |
0.5 |
0.55 |
| 5. Explotab |
6 |
6.60 |
| 6. Sodium carboxymethylcellulose |
2 |
2.20 |
| 7. Talc |
4 |
4.40 |
| 8. Pruv |
0.25 |
0.25 |
| |
|
|
| Total |
100 |
110 |
| Film coating 6% (6.6 mq) Opadry II |
|
|
| |
|
|
| Core size and shape |
¼ round SC |
|
Process:
[0270] The same process for Example 23 is used to prepare the core, along with a film coating
where applicable (see Table 71) in Example 78.
EXAMPLE 79
[0271] An albuterol core composition was prepared having the formulation ingredients set
forth in Table 72:
Table 72
| Component |
Percent |
Amt. (mg) |
| 1. Albuterol |
8.7 |
9.6 |
| 2. Prosolv SMCC™ 50 |
26.8 |
29.48 |
| 3. Prosolve SMCC™ 90 |
52 |
56.89 |
| 4. Silicon Dioxide |
0.5 |
0.55 |
| 5. Explotab |
6 |
6.60 |
| 6. Sodium carboxymethylcellulose |
2 |
2.20 |
| 7. Talc |
4 |
4.40 |
| 8. Pruv |
0.25 |
0.25 |
| |
|
|
| Total |
100 |
|
| Film coating 3% (3.3 mg) Opadry II |
|
|
| |
|
|
| Core size and shape |
¼ round SC |
|
Process:
[0272] The same process for Example 23 is used to prepare the core, along with a film coating
where applicable (see Table 72) in Example 79.
EXAMPLE 80
[0273] An albuterol core composition was prepared having the formulation ingredients set
forth in Table 73:
TABLE 73
| Component |
Percent |
Amt. (mg) |
| 1. Albuterol |
8.7 |
9.6 |
| 2. Prosolv SMCC™ 50 |
26.8 |
29.48 |
| 3. Prosolve SMCC™ 90 |
52 |
56.89 |
| 4. Silicon Dioxide |
0.5 |
0.55 |
| 5. Explotab |
6 |
6.60 |
| 6. Sodium carboxymethylcellulose |
2 |
2.20 |
| 7. Talc |
4 |
4.40 |
| 8. Pruv |
0.25 |
0.25 |
| |
|
|
| Total |
100 |
110 |
| Film coating 6% (6.6 mg) Opadry II |
|
|
| |
|
|
| Core size and shape |
¼ round SC |
|
Process:
[0274] The same process for Example 23 is used to prepare the core, along with a film coating
where applicable (see Table 73) in Example 80.
EXAMPLE 81
[0275] An albuterol core composition was prepared having the formulation ingredients set
forth in Table 74:
Table 74
| Component |
Percent |
Amt. (mg) |
| 1. Albuterol |
8.7 |
9.6 |
| 2. Prosolv SMCC™ 50 |
26.8 |
29.48 |
| 3. Prosolve SMCC™ 90 |
52 |
56.89 |
| 4. Silicon Dioxide |
0.5 |
0.55 |
| 5. Explotab |
6 |
6.60 |
| 6. Sodium carboxymethylcellulose |
2 |
2.20 |
| 7. Talc |
4 |
4.40 |
| 8. Pruv |
0.25 |
0.25 |
| |
|
|
| Total |
100 |
110 |
| Film coating 0.5% (0.55 mg) Magnesium stearate |
|
|
| |
|
|
| Core size and shape |
¼ round SC |
|
Process:
[0276] The same process for Example 23 is used to prepare the core, along with a film coating
where applicable (see Table 74) in Example 81.
Example 82
[0277] In Example 82, other formulations were prepared and tested using USP apparatus type
3, with 250 ml of the dissolution media and dips per minute as indicated in the Table
75.
[0278] The particular dissolution media are defined as follows:
| DI water: |
USP purified water; |
| pH change NI (or no ion): |
pH change method as described in Example 63, without the use of ions to change adjust
the pH; |
| pH change or change (0.1M): |
pH change method as described in Example 63 with the use of salts to give an ionic
strength of 0.1 molar. |
TABLE 75
| Test |
Coating |
Core |
Coating |
Tablet |
Coating |
Dissolution |
Dissol |
Dissolution Time (hrs) (shaded) vs. % Dissolved |
| |
Example |
Example |
Amount |
Weight (mg) |
Size |
Media |
dpm |
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
5 |
5 |
6 |
6 |
7 |
| 1 |
Ex. 10 |
Ex. 72 |
450 |
500 |
3/8 |
DI Water |
15 |
0 |
0 |
0 |
13 |
72 |
98 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
5 |
5 |
6 |
6 |
7 |
| 2 |
Ex. 10 |
Ex. 72 |
450 |
500 |
3/8 |
DI Water |
15 |
0 |
0 |
0 |
0 |
77 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
5 |
5 |
6 |
6 |
7 |
| 3 |
Ex. 10 |
Ex. 70 |
450 |
500 |
3/8 |
DI Water |
15 |
0 |
0 |
2 |
8 |
48 |
79 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
3 |
4 |
5 |
5 |
6 |
6 |
| 4 |
Ex. 10 |
Ex. 70 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
1 |
20 |
29 |
40 |
51 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
3 |
4 |
5 |
6 |
7 |
| 5 |
Ex. 10 |
Ex. 70 |
400 |
450 |
3/8 |
DI Water |
15 |
0 |
0 |
0 |
0 |
40 |
98 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
8 |
10 |
12 |
14 |
16 |
18 |
| 6 |
Ex. 2 |
Ex. 70 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
40 |
68 |
84 |
96 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
6 |
8 |
10 |
12 |
14 |
| 7 |
Ex. 3 |
Ex. 70 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
11 |
50 |
88 |
98 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
4 |
6 |
8 |
10 |
12 |
16 |
| 8 |
Ex. 3 |
Ex. 71 |
350 |
460 |
3/8 |
DI Water |
15 |
0 |
8 |
28 |
57 |
89 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 9 |
Ex. 4 |
Ex. 73 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
0 |
0 |
0 |
86 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 10 |
Ex. 4 |
Ex. 70 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
0 |
0 |
13 |
31 |
79 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
3 |
4 |
5 |
6 |
7 |
| 11 |
Ex. 4 |
Ex. 70 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
0 |
5 |
71 |
84 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
3 |
4 |
4 |
5 |
5 |
| 12 |
Ex. 1 |
Ex. 70 |
250 |
300 |
5/16 |
DI Water |
15 |
0 |
0 |
8 |
30 |
75 |
99 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
3 |
4 |
5 |
6 |
7 |
| 13 |
Ex. 1 |
Ex. 71 |
350 |
460 |
3/8 |
DI Water |
15 |
0 |
14 |
57 |
99 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
2 |
3 |
4 |
5 |
6 |
7 |
| 14 |
Ex. 1 |
Ex. 71 |
350 |
460 |
3/8 |
DI Water |
15 |
0 |
15 |
20 |
83 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 15 |
Ex. 1 |
Ex. 74 |
350 |
460 |
3/8 |
DI Water |
15 0 |
|
0 |
0 |
27 |
91 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 16 |
Ex. 1 |
Ex. 75 |
350 |
460 |
3/8 |
DI Water |
15 |
0 |
0 |
0 |
26 |
98 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 17 |
Ex. 1 |
Ex. 76 |
350 |
460 |
3/8 |
DI Water |
15 |
0 |
0 |
0 |
3 |
68 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 18 |
Ex. 1 |
Ex. 77 |
350 |
460 |
3/8 |
DI Water |
15 |
0 |
0 |
0 |
29 |
71 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 19 |
Ex. 1 |
Ex. 78 |
350 |
460 |
3/8 |
DI Water |
15 |
0 |
0 |
0 |
26 |
98 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
8 |
| 20 |
Ex. 1 |
Ex. 79 |
350 |
460 |
3/8 |
DI Water |
15 |
0 |
0 |
30 |
88 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 21 |
Ex. 1 |
Ex. 81 |
350 |
460 |
3/8 |
DI Water |
15 |
0 |
0 |
0 |
62 |
99 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 22 |
Ex. 1 |
Ex. 71 |
350 |
460 |
3/8 |
DI Water |
15 |
0 |
0 |
0 |
4 |
96 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 23 |
Ex. 1 |
Ex. 81 |
350 |
460 |
3/8 |
DI Water |
15 |
0 |
0 |
0 |
32 |
70 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 24 |
Ex. 1 |
Ex. 74 |
400 |
510 |
3/8 |
DI Water |
15 |
0 |
0 |
0 |
0 |
61 |
99 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 25 |
Ex. 1 |
Ex. 74 |
300 |
410 |
3/8 |
DI Water |
15 |
0 |
0 |
0 |
45 |
77 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 26 |
Ex. 1 |
Ex. 74 |
350 |
460 |
3/8 |
DI Water |
15 |
0 |
0 |
0 |
1 |
67 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
b |
6 |
| 27 |
Ex. 1 |
Ex. 77 |
350 |
460 |
3/8 |
DI Water |
15 |
0 |
0 |
0 |
18 |
46 |
99 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 28 |
Ex. 1 |
Ex. 81 |
350 |
460 |
3/8 |
DI Water |
15 |
0 |
0 |
14 |
96 |
0 |
0 |
0 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 29 |
Ex. 1 |
Ex. 73 |
300 |
410 |
* |
DI Water |
15 |
0 |
0 |
37 |
98 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 30 |
Ex. 1 |
Ex. 73 |
300 |
410 |
* |
DI Water |
15 |
0 |
0 |
27 |
82 |
99 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 31 |
Ex. 1 |
Ex. 73 |
300 |
410 |
* |
DI Water |
15 |
0 |
0 |
24 |
99 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 32 |
Ex. 1 |
Ex. 73 |
350 |
460 |
* |
DI Water |
15 |
0 |
0 |
17 |
65 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 33 |
Ex. 1 |
Ex. 73 |
350 |
460 |
* |
DI Water |
15 |
0 |
0 |
35 |
97 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 34 |
Ex. 1 |
Ex. 73 |
350 |
460 |
* |
DI Water |
15 |
0 |
0 |
14 |
89 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 35 |
Ex. 1 |
Ex. 73 |
400 |
510 |
* |
DI Water |
15 |
0 |
0 |
0 |
69 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 36 |
Ex. 1 |
Ex. 73 |
400 |
510 |
* |
DI Water |
15 |
0 |
0 |
11 |
45 |
97 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 37 |
Ex. 1 |
Ex. 73 |
400 |
510 |
* |
DI Water |
15 |
0 |
0 |
12 |
48 |
96 |
100 |
1100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 38 |
Ex. 1 |
Ex. 81 |
350 |
460 |
* |
DI Water |
15 |
0 |
0 |
14 |
76 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 39 |
Ex. 1 |
Ex. 81 |
350 |
460 |
* |
DI Water |
15 |
0 |
0 |
59 |
98 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 40 |
Ex. 1 |
Ex. 81 |
350 |
460 |
* |
DI Water |
15 |
0 |
0 |
35 |
77 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
|
|
|
|
|
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 41 |
Ex. 1 |
Ex. 81 |
400 |
510 |
* |
DI Water |
15 |
0 |
2 |
2 |
49 |
100 |
100 |
100 |
| |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
| |
|
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0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 42 |
Ex. 1 |
Ex. 81 |
400 |
510 |
* |
DI Water |
15 |
0 |
0 |
0 |
58 |
86 |
100 |
100 |
| |
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0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 43 |
Ex. 1 |
Ex. 81 |
400 |
510 |
* |
DI Water |
15 |
0 |
0 |
0 |
58 |
100 |
100 |
100 |
| |
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0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 44 |
Ex. 1 |
Ex. 81 |
300 |
410 |
* |
DI Water |
15 |
0 |
0 |
70 |
995 |
100 |
100 |
100 |
| |
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0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 45 |
Ex. 1 |
Ex. 81 |
300 |
410 |
* |
DI Water |
15 |
0 |
0 |
0 |
80 |
100 |
100 |
100 |
| |
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0 |
1 |
2 |
3 |
4 |
5 |
6 |
| 46 |
Ex. 1 |
Ex. 81 |
300 |
410 |
* |
DI Water |
15 |
0 |
0 |
59 |
85 |
100 |
100 |
100 |
| |
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0 |
1 |
3 |
5 |
8 |
11 |
14 |
| 47 |
Ex. 1 |
Ex. 78 |
350 |
460 |
* |
pH change |
15 |
0 |
1 |
1 |
16 |
56 |
97 |
100 |
| |
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0 |
1 |
3 |
5 |
8 |
11 |
14 |
| 48 |
Ex. 1 |
Ex. 80 |
350 |
460 |
* |
pH change |
15 |
0 |
0 |
1 |
15 |
68 |
97 |
100 |
| |
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0 |
1 |
3 |
5 |
8 |
11 |
14 |
| 49 |
Ex. 1 |
Ex. 76 |
350 |
460 |
* |
pH change |
15 |
0 |
0 |
2 |
19 |
53 |
94 |
100 |
| |
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0 |
1 |
3 |
5 |
8 |
11 |
14 |
| 50 |
Ex. 1 |
Ex. 81 |
350 |
460 |
* |
pH change |
15 |
0 |
0 |
1 |
15 |
63 |
96 |
100 |
[0279] The effects of the different percentages of gums within the sustained release coating
are shown in Table 76 below:
TABLE 76
| Ex. 1 coating 300 mg coating Example 70 Core |
Ex. 1 coating 446 mg coating Example 71 Core |
Ex. 2 coating 300 mg coating Example 70 Core |
Ex. 3 coating 446 mg coating Example 71 Core |
| Time (hrs.) |
% released |
Time (hrs.) |
% released |
Time (hrs.) |
% released |
Time (hrs.) |
% released |
| 0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
| 2 |
0.4 |
2 |
13.7 |
8 |
39.6 |
4 |
7.7 |
| 3 |
8.4 |
3 |
51.2 |
10 |
67.5 |
6 |
28.3 |
| 3.5 |
29.6 |
4 |
99.3 |
12 |
83.5 |
8 |
56.7 |
| 4 |
74.8 |
5 |
100 |
14 |
96.2 |
10 |
88.7 |
| 4.5 |
99.1 |
6 |
100 |
16 |
99.5 |
12 |
100 |
| 5.0 |
100 |
7 |
100 |
18 |
100 |
16 |
100 |
| |
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| |
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| |
Ex. 4 coating 300 mg coating Example 70 Core |
Ex. 10 coating 450 mg coating Example 72 Core |
Ex. 10 coating 500 mg coating Example 70 Core |
|
| |
Time (hrs.) |
% released |
Time (hrs.) |
% released |
Time (hrs.) |
% released |
|
| |
0 |
0 |
0 |
0 |
0 |
0 |
|
| |
1 |
0 |
4 |
0 |
2 |
0 |
|
| |
2 |
0 |
4.5 |
0 |
3 |
0 |
|
| |
3 |
13.3 |
5 |
12.6 |
4 |
0.3 |
|
| |
4 |
30.6 |
5.5 |
72.3 |
5 |
40.1 |
|
| |
5 |
79.2 |
6 |
98.3 |
6 |
98.4 |
|
| |
6 |
100 |
6.5 |
100 |
7 |
100 |
|
[0280] As shown in the Table 76, the formulation with 20% gums released the active drug
faster than formulations with 30% or 50% gums. The coating used affects the release
rate. In Example 82(a), delayed release coating formulations were prepared in order
to determine the effect of the coating weight and compression force on the time of
release and the rate of release of the active agent within the tablet core.
EXAMPLE 83
[0281] A metoprolol core composition was prepared having the formulation ingredients set
forth in Table 77:
TABLE 77
| Component |
Percent |
Amt. (mg) |
| 1. Metoprolol Tartrate |
47.5 |
100 |
| 2. Prosolv HD™ 90 |
47.5 |
100 |
| 3. Hydroxypropyl methyl cellulose |
5 |
11 |
| 4. Explotab |
4 |
10 |
| 5. Ac-Di-Sol |
2 |
5 |
| 6. Prosolv |
5.75 |
14 |
| 7. Talc |
4 |
10 |
| 8. Pruv |
0.25 |
1 |
| Total |
100 |
250 |
| |
|
|
| Film coating 6% (6.6mg) Opadry AMB |
|
|
Process:
[0282] The same process for Example 23 is used to prepare the core, except that a film coating
is included in Example 83.
[0283] The core of Example 83 was then compression coated with compression coating materials
from previous examples and the resultant tablets were subjected to in-vitro dissolution
studies.
ABSTRACT OF THE DISCLOSURE
[0284] A chronotherapeutic pharmaceutical formulation comprising a core containing an active
agent (e.g., a drug) and a delayed release compression coating comprising a natural
or synthetic gum applied onto the surface of the core.