Background of the Invention
Field of the Invention
[0001] The present invention relates to a superheavy oil emulsion fuel.
Description of the Related Art
[0002] Oil sand, bitumens (e.g. Orinoco tar and Athabasca bitumen), and so forth have attracted
special attention as fossil fuel resources which do not fall under the category of
petroleum, coal and LNG by virtue of their high reserve. Among the fossil fuel resources
under the category of petroleum as well, asphalt obtained by removing the distillates,
such as naphtha, from petroleum or residues obtained by heat-treating the asphalt
are in surplus. These superheavy oils, i.e., asphalt and residues obtained by heat-treating
the asphalt, are generally obtained as vacuum distillation residues.
[0003] Oleaginous materials containing about 60 to 70% or, in some cases, 70% or more of
a heavy fraction having a boiling point of 420 to 450°C or, in some cases, 450°C or
above, do not flow as such or have a viscosity as high as tens of thousands of centipoises
or more. For this reason, if use as a fuel is intended without heating it to a temperature
as high as 280 to 300°C, there occurs not only problems in handling, atomization,
etc., but also problems in the clogging of piping, etc., which renders it very difficult
to use.
[0004] A proposal has hitherto been made with respect to an oil-in-water type (O/W type)
emulsion fuel of a superheavy oil produced by emulsifying a superheavy oil (O) in
water (W) with the use of a surfactant [see, for example, U.S. Patent Nos. 5,024,676
(Assignees; Kao Corp. and Mitsubishi Jukogyo kabushiki Kaisha, Published on June 18,
1991) and 4,923,483 (Assignee; Intevep, S.A., Published on May 8, 1990), and Japanese
Patent Publication-ANos. 313592/1989 (Published on December 19,1989) and 97788/1991
(Published on April 23, 1991)]. The emulsion fuel has a viscosity relatively close
to that of water and can be sufficiently atomized at a temperature range of from ordinary
temperatures to 90°C, and therefore is a fuel having very good handleability. In such
an O/W type emulsion fuel, the lower the content of W (water), that is, the higher
the content of O (oil), the better the quality of the fuel and the lower the fuel
loss. In order to handle the emulsion fuel in the same manner as that of conventional
liquid fuel oils, it is necessary that the emulsion fuel has long-term stability,
sufficient to withstand transportation and storage. However, the emulsion fuel produced
by emulsifying a superheavy oil which has a very high heavy-fraction content and which
does not flow or has a viscosity as high as tens of thousands of centipoises or more,
is insufficient in long-term stability, which is an improvement which has been desired
in the art.
Disclosure of the Invention
Summary of the Invention
[0005] An object of the present invention is to solve the above-described problem and to
provide a superheavy oil emulsion fuel which is excellent not only in handleability
as a fuel by virtue of its low viscosity but also possesses long-term stability of
the emulsion.
[0006] As a result of various studies, the present inventors have found that a stable emulsion
can be provided by using a particular, highly swellable fine clay mineral such as
smectite, vermiculite or chlorite and that an O/W superheavy oil emulsion having a
lower viscosity and a better long-term stability can be provided by using a surfactant
in combination with the above-described particular clay mineral, which has led to
the completion of the present invention.
[0007] Thus, the present invention relates to a superheavy oil emulsion fuel comprising
or consisting essentially of at least a highly swellable fine clay mineral, a superheavy
oil, a surfactant and water.
[0008] Further scope and the applicability of the present invention will become apparent
from the detailed description given hereinafter. However, it should be understood
that the detailed description and specific examples, while indicating preferred embodiments
of the invention, are given by way of illustration only, since various changes and
modifications within the spirit and scope of the invention will become apparent to
those skilled in the art from this detailed description.
Detailed Description of the Invention
[0009] The clay mineral to be used in the present invention is a highly swellable fine clay
mineral. In the present invention, the term "highly swellable" is intended to mean
a property that when a clay mineral is suspended in water, it binds a large amount
of water molecules, and the highly swellable clay mineral is a swellably clay mineral
that has a water molecule relaxation time (T
2) of 900 msec or less, preferably 500 msec or less as measured with a nuclear magnetic
resonance spectrometer when it is suspended in water in an amount of 1% by weight
on a dry basis. When a clay mineral, which has a relaxation time (T
2) in excess of 900 msec, is used, the water binding force of the clay mineral is so
small that the effect of the present invention can not be sufficiently obtained. The
term "fine clay mineral" is intended to mean a clay mineral having an average particle
diameter of 100 µm or less. When a clay mineral having an average particle diameter
of above 100 µm is used, since the water binding force of the clay mineral is small
and, at the same time, sedimentation thereof is liable to occur, the effect of the
present invention can not be attained sufficiently.
[0010] Specifically, fine clay minerals having a high swellability and a high water molecule
binding force, for example, smectite, vermiculite and chlorite, fall within the scope
of the present invention. Among them, however, those having a T
2 value in excess of 900 msec are outside the scope of the present invention. Further,
since kaolin native to Georgia, general kaolin and talc have a low water molecule
binding force, they are excluded from the scope of the present invention.
[0011] Highly swellable fine clay minerals, such as smectite, vermiculite and chlorite,
to be used in the present invention will now be described.
[0012] Smectite has a complicate chemical composition because, in a 2 : 1 layer tetrahedral
sheet or octahedral sheet, substitution occurs in a wide range and various ions accompanied
by water molecules are intercalated. Smectite is represented by, for example, the
following general formula:

wherein X represents K, Na, 1/2Ca or 1/2Mg; Y
2+ represents Mg, Fe(II), i.e., Fe
2+, Mn(II), i.e., Mn
2+, Ni or Zn; Y
3+ represents Al, Fe (III), i.e., Fe
3+, Mn(III), i.e., Mn
3+, or Cr(III), i.e., Cr
3+; and Z represents Si or AI; provided that X, Y and Z represent a intercalated cation,
an octahedral cation and a tetrahedral cation, respectively.
[0013] Representative examples of smectite are as follows.
[0014] Dioctahedral (octahedral cations being mainly trivalent):
montmorillonite represented by, for example, the formula: X0.33(Al1.67Mg0.33)Si4O10(OH)2· nH20, beidellite represented by, for example, the formula: X0.33(Al2)(Al0.33Si0.67)O10(OH)2·nH2O, and nontronite represented by, for example, the formula: XO.33(Fe(111)2)(AIO.33Si3.67)010(OH)2. nH20.
[0015] Trioctahedral (octahedral cations being mainly divalent):
saponite represented by, for example, the formula: X0.33(Mg3) (Al0.33Si3.67)O10(OH)2. nH20,
iron saponite represented by, for example, the formula: XO.33(Mg, Fe(II))3(Al0.33Si3.67)O10(OH)2· nH20, hectorite represented by, for example, the formula: X0.33(Mg2.67Li0.33)Si4O10(OH)2· nH20,
sauconite represented by, for example, the formula: Xo.33(Mg, Zn)3(Si3.67Al0.33)O10(OH)2. nH20, and stevensite represented by, for example, the formula: X0.33/2(Mg2.97)Si4O10(OH)2· nH20.
[0016] Among them, montmorillonite, beidellite and nontronite constitute a series and bring
about isomorphous substitution. The stevensite has a layer charge of one half of that
of the other smectites and properties intermediate between the dioctahedral and trioctahedral
smectites.
[0017] The vermiculite belongs to 2 : 1 layer silicates and is represented by, for example,
the following chemical formula:

[0018] In the above formula, M represents an intercalated exchangeable cation. When the
vermiculite is in the coarse particle form, M is mainly Mg. N in the above formula
represents the quantity of water. When the intercalated cation is Mg, water forms
a bimolecular layer over a wide temperature range and n is about 3.5 to 5. X in the
above formula represents layer charges and is in the range of 0.6 to 0.9. The above
formula assumes that all the layer charges are generated by the substitution of the
tetrahedral cations. In fact, in some cases, the octahedral sheet carries a negative
charge on which the layer charge relies. The number of octahedral cations is 2 to
3, and the vermiculite is classified into a dioctahedral vermiculite and a trioctahedral
one. Aver- miculite in the coarse particle form produced by the weathering of biotite
and phlogopite is a trioctahedral one.
[0019] The structure of the chlorite is similar to those of the smectite and the vermiculite,
and the base plane interval is 14 to 15A. The chlorite is typically a 2: 1 hydrous
silicate which can be classified into a trioctahedral chlorite and a dioctahedral
one according to the nature of the 2 : 1 layer. The trioctahedral chlorite is represented
by, for example, the following formula:

or

[0020] Although R
2+ is mainly composed of Mg and Fe(II), i.e., Fe
2+, it also includes Mn(II), i.e., Mn
2+, Ni, etc. R
3+ is mainly composed of AI and also includes Fe(III), i.e., Fe
3+, Cr(III), i.e., Cr
3+, etc. X in the above formula is a value of 0.8 to 1.6. A chlorite wherein R
2+ is composed mainly of Mg is called "clinochlore" [e.g., (Mg
5Al)(Si
3Al)O
10(OH)
8], and one wherein R
2+ is composed mainly of Fe(II) is called "chamosite" [e.g., (Fe
5Al)(Si
3Al)O
10(OH)
8]. Examples of other trioctahedral chlorites include pennantite wherein R
2+ is composed mainly of Mn(II), and nimite wherein R
2+ is composed mainly of Ni.
[0021] The dioctahedral chlorite wherein the octahedral cation is composed mainly of AI
is classified into three types, i.e., Sudoite [e.g., (Mg, Al)
4.6or5(Si,Al)
40
10 (OH)
8], cookeite [e.g., (LiAl
4)(Si
3Al)O
10(OH)
8] and donbassite [e.
g. , Al
4or4.2R
0.2(Si, Al)
4O
10(OH)
8].
[0022] Those which are composed mainly of montmorillonite, i.e., a clay material belonging
to smectite, and contain, as impurities, quartz, a-cristobalite, opal, feldspar, mica,
zeolite, calcite, dolomite, gypsum and iron oxide, are called "bentonite". The bentonite
is classified into sodium bentonite rich in Na ion and calcium bentonite rich in Ca
ion. The sodium bentonite falls within the scope of the clay mineral of the present
invention because of its high swellability, while the calcium bentonite is excluded
from the scope of the clay mineral of the present invention because of its low swellability.
[0023] Of the sodium bentonites, those with a higher montmorillonite content are preferred.
The particle diameter is 100 µm or less, preferably 10 µm or less. The sodium bentonite
falling within the scope of the clay mineral of the present invention should have
a water molecule relaxation time (T
Z) of 900 msec or less, preferably 500 msec or less, as measured with a nuclear magnetic
resonance spectrometer when it is suspended in water in an amount of 1% by weight
on a dry basis. Among the sodium bentonites, impurities vary depending upon the place
of origin and a difference is observed also in the swellability according to the place
of origin. When the montmorillonite content of the sodium bentonite is increased by
elutriation or other means, the T
2 value of the aqueous suspension of the resultant sodium bentonite becomes low. When
such sodium bentonites are employed that the effect of the present invention becomes
better.
[0024] The above-described clay minerals may be used alone or in the form of a mixture of
two or more of them. In this case, the clay mineral content is usually 0.005 to 2.5
parts by weight, preferably 0.02 to 1.0 part by weight, based on 100 parts by weight
of the superheavy oil. When the content is lower than 0.005 part by weight, the water
binding force of the clay mineral is insufficient, which lowers the storage stability
of the superheavy oil emulsion fuel. On the other hand, when the content exceeds 2.5
parts by weight, the water binding force becomes so large that a phenomenon such as
thickening of the superheavy oil emulsion fuel is observed and, at the same time,
the amount of ash becomes large, which renders the resultant emulsion unsuitable as
a fuel.
[0025] Examples of the superheavy oil to be used in the present invention include the following
oils that do not flow unless they are heated to a high temperature:
(1) petroleum asphalts and mixtures thereof;
(2) various treated products of petroleum asphalts, intermediates, residues, and mixtures
thereof;
(3) oils having a high pour point that do not flow even at a high temperature, or
crude oil;
(4) petroleum tar pitches and mixtures thereof; and
(5) bitumens.
[0026] In the present invention, the superheavy oils are an oleaginous substance that contains
about 60% by weight or more of a heavy distillate having a boiling point of 420 to
450°C or, in some cases, 450°C or above as a vacuum residue. These superheavy oils
may be used alone or in the form of a mixture thereof.
[0027] The surfactant to be used in the present invention is not particularly limited. A
surfactant selected from the group consisting of commonly known anionic surfactants,
nonionic surfactants, cationic surfactants and amphoteric surfactants may be used.
The following surfactants, for example, can provide particularly favorable results.
[0028]
(I) A sulfonic acid of an aromatic ring compound such as naphthalene, alkylnaphthalene,
alkylphenol and alkylbenzene or a salt thereof, or a formalin (formaldehyde) condensate
of a sulfonic acid of an aromatic ring compound or a salt thereof, wherein the average
degree of condensation of formalin is 1.2 to 100 and the salt is an ammonium salt,
a lower amine salt such as a monoethanolamine, diethanolamine, triethanolamine or
triethylamine salt, or an alkali metal or alkaline earth metal salt such as a sodium,
potassium, magnesium or calcium salt.
(II) Ligninsulfonic acid, a salt thereof or a derivative thereof, or a formalin (formaldehyde)
condensate of ligninsulfonic acid and a sulfonic acid of an aromatic compound such
as naphthalene or alkylnaphthalene, or a salt thereof, wherein the salt is an ammonium
salt, a lower amine salt such as a monoethanolamine, diethanolamine, triethanolamine
or triethylamine salt, or an alkali metal or alkaline earth metal salt such as a sodium,
potassium, calcium or magnesium salt and the average degree of condensation of formalin
is 1.2 to 50.
(III) Polystyrenesulfonic acid or a salt thereof, or a copolymer of styrenesulfonic
acid with other comonomer(s) or a salt thereof, wherein the molecular weight is 500
to 500,000 and the salt is an ammonium salt, a lower amine salt such as a monoethanolamine,
diethanolamine, triethanolamine or triethylamine salt, or an alkali metal or alkaline
earth metal salt such as a sodium, potassium, calcium or magnesium salt. (IV) A polymer
of dicyclopentadienesulfonic acid or a salt thereof, wherein the molecular weight
is 500 to 500,000 and the salt is an ammonium salt, a lower amine salt such as a monoethanolamine,
diethanolamine, triethanolamine or triethylamine salt, or an alkali metal or alkaline
earth metal salt such as a sodium, potassium, calcium or magnesium salt.
(V) A copolymer of maleic anhydride or/and itaconic anhydride with other comonomer(s),
or a salt thereof, wherein the molecular weight is 500 to 500,000, and the salt is
an ammonium salt or an alkali metal salt such as a sodium or potassium salt.
(VI) A maleinized liquid polybutadiene or a salt thereof, wherein the molecular weight
of the liquid polybutadiene as the starting material is 500 to 200,000, and the salt
is an ammonium salt or an alkali metal salt such as a sodium or potassium salt.
(VII) An anionic surfactant having in its molecule one or two hydrophilic groups and
selected from the group consisting of the follwings (a) to (h).
(a) A sulfuric ester salt of an alcohol having 4 to 18 carbon atoms, wherein the salt
is an ammonium salt, a lower amine salt such as a monoethanolamine, diethanolamine,
triethanolamine or triethylamine salt, or an alkali metal or alkaline earth metal
salt such as a sodium, potassium, magnesium or calcium salt.
(b) An C4-18 alkane-, alkene- or alkylarylsulfonic acid or a salt thereof, wherein
the salt is an ammonium salt, a lower amine salt such as a monoethanolamine, diethanolamine,
triethanolamine or triethylamine salt, or an alkali metal or alkaline earth metal
salt such as a sodium, potassium, magnesium or calcium salt.
(c) A sulfate or phosphate of an adduct of a compound having in its molecule at least
one active hydrogen with an alkylene oxide or a salt thereof, wherein the salt is
an ammonium salt, or an alkali metal or alkaline earth metal salt such as a sodium,
potassium, magnesium or calcium salt.
(d) Asulfosuccinic acid ester salt of a saturated or unsaturated alcohol having 4
to 22 carbon atoms, wherein the salt is an ammonium salt, or an alkali metal salt
such as a sodium or potassium salt;
(e) An alkyldiphenyletherdisulfonic acid or a salt thereof, wherein the alkyl group
has 8 to 18 carbon atoms, and the salt is an ammonium salt, or an alkali metal or
alkali earth metal salt such as a sodium, potassium, magnesium or calcium salt.
(f) A rosin (or a resin acid) or a salt thereof, wherein the salt is an ammonium salt,
or an alkali metal salt such as a sodium or potassium salt, which includes, for example,
a mixed tall acid comprising a tall rosin and a tall oil fatty acid, i.e., a higher
fatty acid, a tall rosin, a gum rosin, a wood rosin and salts thereof.
(g) An C4-18 alkane or alkene fatty acid or a salt thereof, wherein the salt is an
ammonium salt, or an alkali metal salt such as a potassium or sodium salt.
(h) An a-sulfofatty acid ester salt having an alkyl group of 4 to 22 carbon atoms
or a derivative thereof. The nonionic surfactants to be used in the present invention
include following ones.
(i) An alkylene oxide adduct of a compound having a phenolic hydroxyl group, such
as phenol, cresol, butylphenol, nonylphenol, dinonylphenol, dodecylphenol, p-cumylphenol
or bisphenol A, wherein the alkylene oxide is ethylene oxide, propylene oxide, butylene
oxide, styrene oxide, ethylene oxide/ propylene oxide, ethylene oxide/butylene oxide
or ethylene oxide/styrene oxide.
(ii) An alkylene oxide adduct of a formalin (formaldehyde) condensate of a compound
having a phenolic hydroxyl group, such as an alkylphenol, phenol, m-cresol, styrenated
phenol or benzylated phenol, wherein the average degree of condensation is 1.2 to
100, preferably 2 to 20, and the alkylene oxide is ethylene oxide, propylene oxide,
butylene oxide, styrene oxide, ethylene oxide/propylene oxide, ethylene oxide/butylene
oxide or ethylene oxide/ styrene oxide.
(iii) An alkylene oxide adduct of a monohydric aliphatic alcohol and/or aliphatic
amine having 2 to 50 carbon atoms, wherein the alkylene oxide is ethylene oxide, propylene
oxide, butylene oxide, styrene oxide, ethylene oxide/propylene oxide, ethylene oxide/butylene
oxide or ethylene oxide/ styrene oxide.
(iv) A product of a block or random addition polymerization of ethylene oxide/propylene
oxide, ethylene oxide/butylene oxide, ethylene oxide/styrene oxide, ethylene oxide/propylene
oxide/butylene oxide or ethylene oxide/propylene oxide/styrene oxide.
(v) An alkylene oxide adduct of a polyhydric alcohol, such as glycerol, trimethylolpropane,
pentaerythritol, sorbitol, sucrose, polyglycerol, ethylene glycol, polyethylene glycol,
propylene glycol or polypropylene glycol, or an ester of the above-described polyhydric
alcohol with a fatty acid having 8 to 18 carbon atoms, wherein the alkylene oxide
is ethylene oxide, propylene oxide, butylene oxide, styrene oxide, ethylene oxide/propylene
oxide, ethylene oxide/butylene oxide or ethylene oxide/ styrene oxide.
(vi) An alkylene oxide adduct of a polyamine or the like having a plurality of active
hydrogen atoms, such as ethylenediamine, tetraethylenediamine or polyethyleneimine
(molecular weight: 600 to 10,000), wherein the alkylene oxide is ethylene oxide, propylene
oxide, butylene oxide, styrene oxide, ethylene oxide/propylene oxide, ethylene oxide/
butylene oxide or ethylene oxide/styrene oxide.
(vii) A product prepared by the addition reaction of an alkylene oxide with a mixture
of 1 mol of a fat and oil comprising a triglyceride with 0.1 to 5 mol of a polyhydric
alcohol and/or water, which alcohol is selected from the group consisting of glycerol,
trimethylolpropane, pentaerythritol, sorbitol, sucrose, ethylene glycol, polyethylene
glycol having a molecular weight of 1000 or less, propylene glycol and polypropylene
glycol having a molecular weight of 1000 or less, wherein the alkylene oxide is ethylene
oxide, propylene oxide, butylene oxide, styrene oxide, ethylene oxide/propylene oxide,
ethylene oxide/butylene oxide or ethylene oxide/ styrene oxide.
(viii) An adduct of a tall oil fatty acid, a tall rosin, a gum rosin, a wood rosin
or a mixture thereof with an alkylene oxide.
(ix) Amono- and/or diester of a tall oil fatty acid, a tall rosin, a gum rosin, a
wood rosin or a mixture thereof with an alkylene oxide polymer.
(x) An adduct of an aromatic ring compound having in its molecule one or more carboxyl
groups and derived from petroleum or coal with an alkylene oxide.
(xi) A mono- and/or diester of an aromatic ring compound having in its molecule one
or more carboxyl groups and derived from petroleum or coal with an alkylene oxide
polymer.
[0029] The cationic surfactants and amphoteric surfactants to be used in the present invention
include following ones.
[0030]
(1) An alkyl- or alkenylamine salt produced by neutralizing an alkyl- or alkenylamine
having 4 to 18 carbon atoms with an inorganic or organic acid.
(2) A quaternary ammonium salt represented by the following formulae (a), (b) or (c):

wherein R1, R2, R3 and R4 represent each an alkyl or alkenyl group having 1 to 18 carbon atoms and X° represents
a counter anion, e.g., chlorine ion and bromine ion,

wherein R1, R2, R3 and X° are as defined above, and

wherein R5 represents an alkyl or alkenyl group having 8 to 18 carbon atoms, R6 represents a hydrogen atom or a methyl group and X° is as defined above.
(3) An alkyl- or alkenylbetaine represented by the following formula:

wherein R represents an alkyl or alkenyl group having 8 to 18 carbon atoms.
(4) An alkyl- or alkenylamine oxide represented by the following formula:

wherein R is as defined above.
(5) An alkyl- or alkenylalanine represented by the following formula:

wherein R is as defined above.
(6) A polyamiet represented by the following formulae (d) or (e):


wherein R is as defined above and Y and Y' represent each an oxyethylene chain represented
by the formula (̵C2H4O m H wherein m is 1 to 50.
(7) A polyamine salt represented by the following formulae (f) or (g):


wherein R is as defined above and X' represents an inorganic or organic acid, e.g.,
hydrochloric acid and acetic acid.
(8) An amphoteric imidazoline surfactant represented by the following formula:

wherein R is as defined above.
(9) An amphoteric sulfobetaine surfactant represented by the following formula:

wherein R is as defined above.
[0031] Although the above-described highly swellable clay mineral has excellent effect of
stabilizing the superheavy oil emulsion fuel, it has an insufficient effect of reducing
the size of oil droplets. Therefore, the combination use of the highly swellable clay
mineral and a surfactant excellent in the effect of reducing the size of oil droplets
can provide more stable emulsion fuel. For this reason, the use of a mixture of an
ionic surfactant with a nonionic surfactant is particularly preferred. Especially,
it is preferred that the weight ratio of the ionic surfactant to the nonionic surfactant
be 1 : 99 to 80: 20. Further, an excellent effect can be attained also when use is
made of a system comprising an anionic surfactant and, incorporated therein, a small
amount of a cationic surfactant, for example, a system comprising 100 parts by weight
of an anionic surfactant and, incorporated therein, 20 parts by weight or less (but
not 0) of a cationic surfactant. Furthermore, the same effect can be attained when
use is made of a system comprising 100 parts by weight of a cationic surfactant and,
incorporated therein, 20 parts by weight or less (but not 0) of an anionic surfactant.
[0032] The above-described surfactants may be used alone or in the form of a mixture thereof.
In this case, the content of the surfactant is usually 0.05 to 3.0 parts by weight,
preferably 0.2 to 1.5 parts by weight, based on 100 parts by weight of the superheavy
oil. When the content is lower than 0.05 part by weight, the amount of coarse particles
becomes large and, at the same time, the stability of the emulsion system becomes
unsatisfactory. On the other hand, when the content exceeds 3.0 parts by weight, the
thickening of the emulsion system becomes significant unfavorably and, since the emulsifier
is more expensive than the oil, such a high content is disadvantageous from the economic
viewpoint.
[0033] The superheavy oil emulsion fuel of the present invention comprises the above-described
components and water and is produced by emulsifying and/or dispersing the above-described
components in water. In this case, the water content is usually 20 parts by weight
or more, preferably 20 to 80 parts by weight, still preferably 25 to 80 parts by weight,
based on 100 parts by weight of the superheavy oil. When the water content is lower
than 20 parts by weight, there occurs an increase in the amount of coarse particles
which are causative of the generation of soot and dust.
[0034] The superheavy oil emulsion fuel of the present invention may comprise, in addition
to the above-described components, at least one of the following hydrophilic polymers
(A) to (J) that can provide a better emulsion. The content of the hydrophilic polymer
in the superheavy emulsion fuel is usually 0.001 to 1.0 part by weight, preferably
0.005 to 0.5 part by weight, based on 100 parts by weight of the entire amount of
the superheavy oil emulsion fuel.
[0035] The hydrophilic polymer is classified into a naturally occurring hydrophilic polymer
and a water-soluble synthetic polymer.
[0036] Hydrophilic polymers derived from naturally occurring matter include the following
ones.
(A) Hydrophilic Polymers Derived from Microorganisms (Polysaccharides)
(a) xanthan gum
(b) pullulan
(c) dextran
(B) Hydrophilic Polymers Derived from Plants (Polysaccharides)
(a) Derived from marine algae:
(i) agar
(ii) carrageenan
(iii) furcellaran
(iv) alginic acid and salts (Na, K, NH4, Ca or Mg) thereof
(b) Derived from seeds:
(i) locust bean gum
(ii) guar gum
(iii) tara gum
(iv) tamarind gum
(c) Trees (exudates):
(i) gum arabic
(ii) gum karaya
(iii) gum tragacanth
(d) Derived from fruits:
(i) pectin
(C) Hydrophilic Polymers Derived from Animals (Proteins)
(i) gelatin
(ii) casein
(D) Naturally Occurring Polymer Derivatives
(i) cellulose derivatives (such as carboxymethylcellulose)
(ii) chemically modified starch Hydrophilic, that is, water-soluble synthetic polymers
include following ones.
(E) A homopolymer or copolymer of acrylic acid or a derivative thereof represented
by the following formula:

wherein R' represents a hydrogen atom, a methyl group or an ethyl group; M1 represents a hydrogen atom, a sodium ion, a potassium ion, a lithium ion or an ammonium
ion; Z1 represents a divalent group derived from a monomer represented by the formula:

(wherein R' and M1 are as defined above), a comonomer copolymerizable with the monomer or a salt of
the comonomer, for example, maleic acid (anhydride), itaconic acid (anhydride), α-olefin,
acrylamide, vinylsulfonic acid, allylsulfonic acid, methallylsulfonic acid, acrylamidomethylpropylsulfonic
acid or a salt (NH4, Na, K or Li) thereof, a dialkyl(methyl or ethyl)aminoethylmethacrylate or a salt
(chloride, diethylsulfate or dimethylsulfate) thereof; and n is 50 to 100,000.
(F) A homopolymer or copolymer of acrylamide or a derivative thereof represented by
the following formula:

wherein R" represents a hydrogen atom or a C2H40H group; Z2 represents a divalent group derived from a monomer represented by the formula:

(wherein R" is as defined above), a comonomer copolymerizable with the monomer or
a salt of the comonomer, for example, vinylsulfonic acid, allylsulfonic acid, methallylsulfonic
acid, acrylamidomethylpropylsulfonic acid or a salt (NH4, Na, K or Li) thereof, a dialkyl(methyl or ethyl)aminoethylmethacrylate or a salt
(chloride, dimethylsulfate or diethylsulfate) thereof, styrene, α-olefins (C2-18) and vinylallyl alcohol; and n is 50 to 100,000.
(G) A hopopolymer of maleic anhydride or itaconic anhydride, or a copolymer thereof
represented by the following formula:

wherein M2 represents a maleic anhydride or itaconic anhydride residue; Z3 represents an α-olefin (ethylene, propylene, butylene, isobutylene, octene, decene,
dodecene or the like) or styrene residue; and n is 50 to 100,000.
(H) A homopolymer of vinyl alcohol, or a copolymer thereof represented by the following
formula:

wherein Z4 represents a vinyl acetate or styrene residue; and n' is 30 to 100,000.
(I) A homopolymer of vinylpyrrolidone, or a copolymer thereof represented by the following
formula:

wherein Z5 represents a divalent group derived from a comonomer copolymerizable with vinylpyrrolidone
or a salt (NH4, Na, K or Li) thereof, for example, acrylamide, vinylsulfonic acid, methallylsulfonic
acid, maleic anhydride, itaconic anhydride or a salt (NH4, Na, K or Li) thereof, styrene, α-olefin (C2-18) or the like; and n is 50 to 100,000.
(J) A polyalkylene oxide having a molecular weight of 10,000 to 5,000,000 (wherein
the ethylene oxide content is 95% or more). It may contain in its molecule 5% or less
of a block polymer of propylene oxide, butylene oxide or styrene oxide, or an alkylaryl
or alkyl group.
[0037] In the production of the superheavy oil emulsion fuel of the present invention, it
is preferred to use mechanical means having a shear force of 1100/sec or more, preferably
4,000 to 30,000/sec, in terms of shear rate. Specific examples of the mechanical means
include a model M TK homomixer (manufactured by Tokushu Kika Kogyo Co., Ltd.) and
a line mixer.
[0038] The superheavy oil emulsion fuel of the present invention thus produced usually has
a viscosity as low as 1000 cP or below (at 60°C) and a high percentage undersize,
so that it is very easy to handle as a fuel and is further excellent, particularly
in long-term stability in the dispersed state after the emulsion is left to stand.
Specifically, it has the advantage of a remarkable suppression of the generation of
coarse particles and the thickening phenomenon.
Brief Description of the Drawing
[0039] Fig. 1 is a schematic view of a centrifuge tube used for the evaluation of the dispersed
state after standing, wherein 1 is the surface layer, 2 is the intermediate layer
and 3 is the sedimentation layer.
Examples
[0040] The present invention will now be described in more detail with reference to the
following Examples which should not be considered to limit the scope of the present
invention.
Examples 1 to 15
[0041] Middle Eastern petroleum-derived asphalt (penetration: 60 - 80), water, a surfactant
and a highly swellable clay mineral were weighed respectively in given amounts (total
amount: 300 g) to give compositions specified in Tables 1 to 3, put into an 800-ml
centrifugation tube and heated to 75°C. After the temperature of the mixture became
constant, the mixture was agitated (8000/sec x 2 min) with a TK homomixer (provided
with a low-viscosity agitation blade; manufactured by Tokushu Kika Kogyo Co., Ltd.)
to prepare emulsion fuels, which were stored at 60°C. After the temperature of the
emulsion fuels became constant, the viscosity of each fuel was measured with a Model
VS-A1 Vismetron (No. 2 rotor, numberof revolutions of the rotor: 60 rpm) manufactured
by Shibaura Systems Co., Ltd. Part of the emulsion fuel was maintained at 50°C to
observe the state of the emulsion fuel 1 day, 9 days and 6 months after the initiation
of the storage. Part thereof was taken out to measure the percentage undersize of
a 100-mesh sieve. The percentage sieve undersize was determined by putting about 10
g of a sample on a 100-mesh stainless sieve of 70 mmϕ in an atmosphere at 50°C, measuring
the oversize after 10 min, and calculating the undersize. The results are given in
Tables 1 to 3.
[0042] The overall evaluation was conducted by collectively evaluating the viscosity of
the emulsion, percentage sieve undersize, and visual observation of the dispersed
state after the emulsion was left to stand. The overall evaluation is better in the
following order: @ > 0 > Δ > x, and the effect of the present invention was observed
in the systems in which the overall evaluation was A or better.
[0043] With respect to the dispersed state after standing, the states of three layers as
shown in Fig. 1, i.e., surface layer 1, intermediate layer 2 and sedimentation layer
3, were observed and separately evaluated.
[0044] In the surface layer 1, the size of oil droplets present on the surface and that
of an oil film formed by the growth of the oil droplets were observed. The dispersed
state is better in the following order: "no oil droplet" > "small amt. of oil droplet"
> "no oil film" a "large amt. of oil droplet" > "small amt. of oil film" > "large
amt. of oil film". Namely, "no oil droplet" is best and "large amt. of oil film" is
worst.
[0045] In the intermediate layer 2, the emulsified state was observed. The emulsified state
is better in the following order: "excellent emulsification" > "slightly creamy state"
> "creamy state" > "separation" > "remarkable separation" > "complete separation".
Namely, "excellent emulsification" is best and "complete separation" is worst.
[0046] In the sedimentation layer 3, the state is better in the following order: "no sediment"
> "soft sediment" > "hard sediment". Namely, "no sediment" is best and "hard sediment"
is worst. The soft sediment is a sediment which is soft and easily redispersible,
while the hard sediment is a sediment which is hard and difficult to redisperse.

Comparative Examples 1 to 4
[0047] Emulsion fuels having compositions specified in Table 4 were prepared in the same
manner as that of Examples 1 to 15, except that the surfactant and the highly swellable
clay mineral were not simultaneously used. The fuels were evaluated in the same manner
as that of Examples 1 to 15. The results are given in Table 4.
Comparative Examples 5 to 7
[0048] Emulsion fuels having compositions specified in Table 4 were prepared in the same
manner as that of Examples 1 to 15, except that use was made of clay minerals outside
the scope of the present invention. The fuels were evaluated in the same manner as
that of Examples 1 to 15. The results are also given in Table 4.

Examples 16 to 18
[0049] Emulsion fuels having compositions specified in Table 5 were prepared in the same
manner as that of Examples 1 to 15, except that Athabasca bitumen (softening temperature:
12.5°C, native to Canada) was used instead of the Middle Eastern petroleum-derived
asphalt (penetration: 60 - 80). The fuels were evaluated in the same manner as that
of Examples 1 to 15. The results are also given in Table 5.
Comparative Example 8
[0050] An emulsion fuel having a composition specified in Table 5 was prepared in the same
manner as that of Examples 16 to 18, except that no use was made of highly swellable
clay mineral. The fuel was evaluated in the same manner as that of Examples 16 to
18. The results are also given in Table 5.

Examples 19 to 22
[0051] Middle Eastern petroleum-derived asphalt (penetration: 60 - 80), water, a surfactant,
a highly swellable clay mineral and a hydrophilic polymer were weighed respectively
in given amounts (total amount: 300 g) to give compositions specified in Table 6,
put into a 300-ml centrifugation tube and heated to 75°C. Afterthe temperature of
the mixture became constant, the mixture was agitated (8000/sec x 2 min) with a TK
homomixer manufactured by Tokushu Kika Kogyo Co., Ltd. to prepare emulsion fuels,
which were stored at 60°C. The viscosity and percentage undersize of a 100-mesh sieve
of the fuels were measured in the same manner as that of Examples 1 to 15. Further,
the state of dispersion after the standing was evaluated in the same manner as that
of Examples 1 to 15. The results are given in Table 6.
Comparative Examples 9 and 10
[0052] Emulsion fuels having compositions specified in Table 6 were prepared in the same
manner as that of Examples 19 to 22, except that no use was made of highly swellable
clay mineral. The fuels were evaluated in the same manner as that of Examples 19 to
22. The results are also given in Table 6.

[0053] Each of the superheavy oil emulsion fuels of the present invention provided in Examples
1 to 18 had a low viscosity and a high percentage undersize and was stable also in
the state of dispersion after the emulsion was left to stand. By contrast, each of
the emulsion fuels not containing at least one of the surfactant and the highly swellable
clay mineral (Comparative Examples 1 to 4 and 8) and those containing clay minerals
outside the scope of the present invention (Comparative Examples 5 to 7) had a high
viscosity and a low percentage undersize and was unstable also in the state of dispersion
after the emulsion was left to stand.
[0054] In each of the emulsion fuels wherein the highly swellable clay mineral was used
in combination with the hydrophilic polymer, the dispersed state after the emulsion
was left to stand was stable. In this case, each of the superheavy oil emulsion fuels
provided in Examples 19 to 22 was superior in the dispersed state after the emulsion
was left to stand to those of Comparative Examples 9 and 10 wherein no use was made
of highly swellable clay mineral.
[0055] The invention being thus described, it will be obvious that the same may be varied
in many ways. Such variations are not to be regarded as a departure from the spirit
and scope of the invention, and all such modifications as would be obvious to one
skilled in the art are intended to be included within the scope of the following claims.