[0001] This invention relates to a process for controlling natural pitch deposition obtained
from the processing of various wood pulps which are then used to manufacture paper
products. These natural pitch depositions are detrimental to efficient operations
of paper mills. Pitch deposits on process equipment used in the paper making systems
result in operational problems related to the accumulation of pitch deposits on consistency
regulators and other instrumental probes used to monitor the process of manufacturing
paper from various types of pulp and paper furnishes.
[0002] In addition pitch deposits can form on screens and can reduce throughput as well
as upset the operation of the paper manufacturing process. The deposition of natural
pitch can occur not only on the metal surfaces in the system but also on plastic and
synthetic surfaces such as machinery wires, felts, foils, UHLE boxes, and head box
components. These pitch deposits may also break off resulting in spots and defects
in the final paper product which thereby decreases the paper quality.
[0003] Surfactants, anionic polymers and co-polymers of anionic monomers and hydrophobic
monomers have been used extensively to prevent pitch deposition. For example, in the
text "Pulp and Paper" by James B. Casey, volume II, second edition, pages 1096-7,
the above types of polymers are described for this purpose.
[0004] In addition, bentonite, talc, diatomaceous earth, silica, starch, animal glue, gelatin
and alum have also been used to reduce pitch deposits. U.S. Patent 3,081,219, Drennen
et al., discloses the use of polymeric N-vinyl lactam to control pitch in making paper
from sulfite pulps.
[0005] In addition the following patents have disclosed the use of various kinds of chemicals
both polymeric and nonpolymeric for pitch control.
U.S. Patent 3,154,466, Nothum
U.S. Patent 3,582,461, Lipowski et al.,
U.S. Patent 3,619,351, Kolosh
U.S. Patent 3,748,220, Gard
U.S. Patent 3,992,249, Farley
U.S. Patent 4,184,912, Payton
U.S. Patent 4,190,491, Drennen et al.,
U.S. Patent 4,253,912, Becker et al.,
U.S. Patent 4,871,424, Dreisbach, et al.,
U.S. Patent 4,765,867, Dreisbach et al.,
U.S. Patent 4,744,865, Dreisback et al.,
Canadian Patent 1,194,254, Molnar
Canadian Patent 1,150,914, Molnar
U.S. Patent 4,313,790, Pelton et al.,
[0006] All of the above patents disclose certain processes and formulations, including cationic
polymers and specifically, for example, in Canadian 1,194,254, certain cationic polymers
formed by polymerization of diallyl dimethyl ammonium chloride, which polymers are
useful for pitch control.
[0007] In addition, an article appearing in a publication by the Institute of Paper Science
and Technology in Atlanta, Georgia, authored by Weigel, et al., and entitled "Resin
Deposits and Their Control in Papermaking" and translated from Papier 40(10A): V52-62
(October 1986), also described pitch deposits and their control in various paper mills.
[0008] An article, "Unusual Applications of Dual Polymer Systems" by Dykstra, et al., published
in the 1987 TAPPI Advanced Topics in Wet End Chemistry Seminar, speaks of the use
of anionic polymers in combination with charged condensation polymers having cationic
charge for use in pitch control.
[0009] Another article entitled "Pitch and Stickies Control in Pulp and Paper Mills" by
Pamela J. Allison published in Paper Southern Africa, Volume 8, No. 3, 1988, talks
of pitch and stickies deposits and techniques for their control. Another paper by
Dykstra et al., entitled, "A New Method for Measuring Depositable Pitch and Stickies
and Evaluating Control Agents", published in 1988 TAPPI Papermakers Conference Proceedings,
page 327, also talks of pitch and stickies control. This paper also talks of dual
polymer treatment.
[0010] Finally in the June, 1988, Tappi Journal, on page 195, an article by Hassler, entitled,
"Pitch Deposition in Papermaking and the Function of Pitch-control Agents," speaks
of various pitch control agents and techniques to assist in pitch deposition and control.
[0011] All of the above patent and literature references are incorporated herein by reference.
[0012] In none of the references, including the specific Canadian patent to Molnar referring
to the use of a homopolymer of DADMAC, i.e., diallyl dimethyl ammonium chloride, is
there any mention of the use of ampholytic polymers containing diallyl dimethyl ammonium
halide monomers.
[0013] The present invention provides an improved process of pitch control which process
uses as a pitch control agent, water soluble co-polymers or terpolymers which are
formed by polymerization of diallyl dimethyl ammonium salts with acrylic acid or methacrylic
acid or their salts, and optionally using various alkyl acrylate esters or hydroxy
substituted alkyl esters of acrylic acid or methacrylic acid.
[0014] Another object of the invention is to eliminate or minimize the effect of natural
pitch deposits in the manufacture of paper by adding to a pitch contaminated paper
furnish prior to sheet formation, an improved pitch control agent which agent is a
co-polymer or terpolymer containing diallyl dimethyl ammonium salts, acrylic acid
or methacrylic acid and its salts, and, optionally, alkyl acrylate or hydroxy alkyl
acrylates.
[0015] Another object of the invention is to provide a specific co-polymer and/or terpolymer
which is useful as a pitch control agent which polymer has a molecular weight ranging
from about 10,000 to about 1,000,000 and contains from 75 - 95 mole per cent of diallyl
dimethyl ammonium chloride; contains from about 2 to about 25 mole per cent of acrylic
acid, methyacrylic acid, or their salts, or mixtures thereof; and from about 0 to
about 10 mole per cent of an alkyl acrylate or a hydroxy alkyl acrylate or mixtures
thereof.
[0016] We have determined that an improved process for controlling natural pitch deposition
onto paper machine surfaces and into the paper sheet can be demonstrated, which process
includes the addition of an effective pitch deposit controlling amount of pitch control
agents to the pitch contaminated paper furnish prior to paper sheet formulation, the
improvement comprising using as a pitch control agent a water soluble co-polymer comprising
a combination of monomers chosen from the group consisting of diallyl dimethyl ammonium
salts, (meth)acrylic acids and salts thereof, and alkyl or hydroxyalkyl acrylates,
thereby forming polymers having the structure:

wherein R is individually chosen, at each occurrence, from hydrogen, methyl groups,
and ethyl groups, provided that if R is covalently bonded to a nitrogen, R is chosen,
at each occurrence, only from methyl groups and ethyl groups; and
M is chosen, at each occurrence, from hydrogen, alkali metal cations, equivalent amounts
of alkaline earth metal cations, ammonium cations, protonated amine or quaternary
ammonium cations and mixtures thereof; and
R' is a multivalent hydrocarbonaceous linear or branched alkyl group containing from
1-24 carbon atoms; and
X is an anion present in electroneutral amounts relative to positively charged nitrogen
in the polymer backbone;
Y is chosen from -H, -OH, and mixtures thereof; wherein the sum of a+b+d is sufficient
to provide for a weight average molecular weight ranging between about 10,000 and
about 1,000,000;
e is from 0 to 6; and the following relationships exist:
a:b is at least 3:1
a:(b + d) is at least 75:25, and
d:(a + b) ranges from 0 to 1:9, and further
d, but not a or b, can be zero.
THE POLYMER STRUCTURE
[0017] The polymer structure is as that described above. In this structure each monomer
unit is essentially randomly distributed along the polymer chain and the polymer is
ampholytic in nature, i.e. it can carry both a positive and a negative charge.
[0018] In addition the polymer optionally contains from 0 to about 10 mole per cent of a
monomer which is oleophillic in character. This oleophillic monomer is preferably
an ester or hydroxyester of acrylic acid, methacrylic acid, ethacrylic acid, or mixture
thereof.
[0019] The cationic character of the polymers described above are provided by inclusion
of from about 75 to about 95 mole per cent of diallyl dimethyl ammonium salts. These
salts may be chlorides, bromides, iodides, sulfates, nitrates, phosphates, and the
like. Preferably, these quaternary di-vinyllic salts are in the form of diallyl dimethyl
ammonium chloride (known in abbreviation as DADMAC). The diallyl dimethyl ammonium
chloride (DADMAC) monomer is contained in the polymer at from about 75 to about 95
mole per cent, preferably from about 80 to about 90 mole per cent, and most preferably
between 85 to about 90 mole per cent. This provides for an overwhelming positive charge
on the backbone polymer.
[0020] However, it has been demonstrated that improvements in the use of these materials
as pitch control agents are provided by the inclusion in the backbone of the polymers
described above of from 2 to about 25 mole per cent of an anionic monomer unit. The
preferred anionic monomer is chosen from acrylic acid, methacrylic acid, ethacrylic
acid, and their common salts, or mixtures thereof. Preferably the salts are in the
form of alkali metal salts, equivalent amounts of alkaline earth metal salts, or salts
of ammonium cations, quaternary amine cations, or protonated amine cations. Most preferably
the anionic monomer is acrylic acid, or methacrylic acid, or mixtures thereof, used
either as the free acid or as the sodium, potassium, and/or ammonium salts. Of course
any mixtures of the salts are also included in the concept of using these anionic
monomer units and incorporating them in the monomer structures above. These anionic
monomers can be represented by the term (meth)acrylic acid, but this term is used
herein to represent any vinylic acid, or vinylic acid salt having the structure:

where R is H, CH
3, C
2H
s, and mixtures therof; and M is as defined above.
[0021] As above, the polymer can be improved by the incorporation, optionally, of certain
oleophillic monomers such as (meth) acrylic acid esters, or (meth)acrylic acid hydroxy
esters. These compounds provide some oleophillic character to the polymer and can
assist in accumulating and dispersing pitch particles and attaching these pitch particles
to cellulosic fibers so they do not accumulate disadvantageously on paper machine
surfaces or cause difficulties otherwise in the manufacture of paper. These vinylic
acid esters and vinylic acid hydroxy esters are primarily those materials chosen from
acrylic acid esters, methacrylic acid esters, or ethacrylic acid esters. By the term
acrylic acid ester, methacrylic acid ester, or ethacrylic acid ester we mean to also
include the hydroxy esters that contain one or more hydroxyl groups on the alkyl unit
attached to the ester oxygen.
[0022] The polymer that is preferred is a polymer that has a molecular weight ranging from
about 10,000 to about 1,000,000 and most preferably has a molecular weight ranging
from about 50,000 to about 500,000. These molecular weights are weight average molecular
weights. The most preferred polymer contains from about 80 to about 90 mole per cent
of diallyl dimethyl ammonium chloride, from about 5 to about 20 mole per cent of acrylic
acid or methacrylic acid or mixtures thereof, (or salts thereof) and from about 0
to about 10 mole per cent of acrylic acid esters chosen from the group consisting
of hydroxy alkyl acrylates and alkyl acrylates, or mixtures thereof, where the alkyl
group of the ester functionality has from about 1 to about 24 carbon atoms, preferably
from about 2 to about 14 carbon atoms.
[0023] The ampholytic polymers of this invention do not necessarily have to contain the
(meth)acrylate esters or hydroxy alkyl (meth) acrylate esters, but can be formed merely
as co-polymers of diallyl dimethyl ammonium chloride (or other salt) and either acrylic
acid, methacrylic acid, ethacrylic acid, their salts, or mixtures thereof. When co-polymers
are used, it is preferred that DADMAC is present between about 80 to about 95 mole
per cent and the anionic (meth)acrylic acid units are present at between about 5 to
about 20 mole per cent. Most preferably these co-polymers contains about 80 to 90
mole per cent DADMAC and from about 10 to about 20 mole per cent (meth)acrylic acid,
or its salts.
DOSAGES
[0024] Typically, dosages of products containing the pitch control agents described above
normally range from about 0.05 to about 20 pounds of formulated product per ton of
paper product, on a dry fiber basis. The pitch control agents normally are provided
as liquid dispersions or solutions of the polymers described in water which products
normally range from about 1 to about 40 weight per cent active polymer. The polymer
may also be provided as a water-in-oil latex emulsion containing a dispersed aqueous
phase in which the polymer described above has been dissolved. This emulsion normally
also contains a controlled HLB surfactant system such that when the water-in-oil emulsion
is added to the paper making system, inversion of phases occurs, and the polymer is
rapidly dissolved and dispersed in the aqueous paper making media. When the product
is supplied as a water-in-oil emulsion, the polymer content of the emulsion product
can range from about 5 to about 55 weight per cent of the product. On an active polymer
basis, the polymer dosage for the polymers of this invention, and described above,
normally ranges from about 0.05 to about 2.0 pounds per ton, on the basis of active
polymer per ton of dry fiber. To further exemplify and demonstrate our invention the
following examples are provided:
EXAMPLES
[0025] Laboratory trials of products meeting the descriptions provided above were tested
by the following procedure:
Example 1.
[0026] Approximately 7,000 ml of a hardwood kraft paper stock was prepared. This hardwood
kraft stock contained 2.27 weight per cent fiber. This paper stock material was diluted
with water until it contained approximately 1.5 weight per cent hardwood kraft stock
fiber. The pH of this stock was adjusted to about 10.6 with sodium hydroxide solution.
Approximately 100 ml of a 1 per cent dispersion of a laboratory pitch mixture was
added to 700 ml of the 1.5 per cent hardwood kraft stock. The pH dropped to a pH of
approximately 7.4-7.5. To this pitch containing slurry of hardwood kraft fibers was
added 5 ml of a 0.5 molar calcium chloride dihydrate solution. This mixture was gently
stirred and the pH checked. The pH had dropped to approximately 6.5. The pH of this
test preferably ranges somewhere between 5.5 and 7.0 during the testing sequence for
pitch deposition control.
[0027] The mixture of hardwood kraft stock, which mixture contains synthetic pitch dispersion
and calcium chloride as described above is then poured into an laboratory blender.
To this slurry is added a preweighed poly tetrafluoro ethylene plastic (PTFE) coupon
which acts as a surface on which pitch is accumulated. This PTFE coupon is added to
the pitch contaminated hardwood kraft stock in the blender. The blender used had 14
buttons controlling agitation blade speed. After addition of the preweighed PTFE plastic
coupon, button number 4 is pushed and the stock is agitated for three minutes. Other
blender speeds are also operable. A pitch deposit is obtained on the PTFE coupon,
and after the coupon is removed, rinsed with distilled water from a wash bottle and
dried in air, the coupon is then weighed. Drying time can range from about 4 hours
to about 24 hours. The amount of deposited pitch is calculated by the difference from
the original weight of the coupon.
[0028] By using this technique for each test sample, the following results were obtained.

Example II.
[0029] In addition, various tests were also performed on a trial and experimental basis,
on a machine chest stock obtained from an active producing paper mill. The pH of the
machine chest stock was measured at 7.95 and samples of this stock were treated in
the laboratory with a homopolymer of diallyl dimethyl ammonium chloride, as taught
by Molnar, and was simultaneously treated with the polymers of this invention. Results
are shown in Table II.

[0030] Success in Table II is measured by the percent decrease in filtrate turbidity which
is a measure of the amount of pitch which has been suspended and attached to the fiber
so that it does not contribute to filtrate turbidity.
[0031] In addition to the Polymer #3 described above which polymer is a polyampholyte containing
DADMAC/acrylic acid, salts, and hydroxypropylacrylate in a terpolymer, as described
above, the following data is also presented which describes other co-polymers and
terpolymers which fall within the claims of our invention and the use of these experimental
polymers for pitch deposition control.
Examples III. (A - L)
[0032] The following test polymers were treated in the laboratory using the procedures set
forth in Example I, except that a modified synthetic laboratory pitch was used.

[0034] In all the tests above using the procedures set forth in Example I, the pitch dispersion
used is a synthetic laboratory pitch comprising a mixture of fatty and resin acids
and esters, sterols, sterol esters and fatty alcohols, which is representative of
actual softwood and/or hardwood pitch. This synthetic pitch is used to form the 1
% dispersion described in Example I, and ranges in content as described in Table V.

[0035] This synthetic laboratory pitch is dispersed in isopropanol to form a
[0036] 1% dispersion used as in Example I.
1. The process of controlling pitch deposition on paper machine surfaces by the addition
of pitch control agents to a paper furnish prior to sheet formation, characterized
in that the pitch control agent is a polymer having the structure:

wherein R is chosen, at each occurrence, from H, CH
3 and C
2H
5;
R' is a multivalent hydrocarbonaceous bridging group containing from 1 - 24 carbon
atoms and chosen from linear and branched alkyl groups, cyclic groups, aromatic groups,
alkaryl and aralkyl groups, and mixtures thereof;
M is chosen, at each occurrence, from H, alkali metals, alkaline earth metals in equivalent
amount, ammonium, protonated amine and quaternary amine cations, and mixtures thereof;
X is an anion present in electroneutral amounts relative to positively charged nitrogen
in the polymer backbone;
Y is chosen from -H, -OH, and mixtures thereof; and the sum of a + b + d is sufficient
to provide a weight average molecular weight ranging between about 10,000 and about
1,000,000;
e is from 0 to 6; and
the following ratios exist:
a:b is at least 3:1,
a:(b + d) is at least 75:25,
d:(a + b) ranges from 0 to 1:9; and
d, but not a or b, can be zero.
2. The process of claim 1 wherein the pitch control agent is a terpolymer having a
weight average molecular weight ranging between about 50,000 to about 500,000, and
R, when attached to nitrogen in the polymer structure is - CH
3, and when attached to carbon in the polymer structure is from the group H, CH
3, or mixtures thereof; R' is a linear or branched alkylene group having from 1 to
16 atoms; and e is from 0 to 4; and
the following ratios exist:
a: b is at least 4:1,
a: (b + d) is at least 80:20, and
d: (a + b) ranges from 0 to 1:9, and the effective pitch deposit controlling amont
of the copolymer ranges from about 0.01 to about 2.0 pounds active copolymer per ton
of dry fiber.
3. The process of claim 1 wherein R is chosen at each occurrence from H and CH
3;
R' is linear or branched alkyl group having from 1 to about 14 carbon atoms;
X is CI
M is H, Na, K, Li, NH4, or mixture thereof;
Y is from H and -OH, and mixtures thereof;
e is from 0 to 2; and
the sum a + b + d is sufficient to obtain a weight average molecular weight from about
50,000 to 500,000; d, but neither a or b can be zero; and the ratio a:b is at least
4:1; and the ratio, d:(a + b) never exceeds 1:9.
4. The process according to any one of the preceding claims wherein the polymer is
added to the paper stock at a dosage of from about 0.05 to about 1.5 pounds active
polymer per ton paper, on a dry fiber basis.