CA2102030A1 - Superheavy oil emulsion fuel - Google Patents

Superheavy oil emulsion fuel

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Publication number
CA2102030A1
CA2102030A1 CA 2102030 CA2102030A CA2102030A1 CA 2102030 A1 CA2102030 A1 CA 2102030A1 CA 2102030 CA2102030 CA 2102030 CA 2102030 A CA2102030 A CA 2102030A CA 2102030 A1 CA2102030 A1 CA 2102030A1
Authority
CA
Canada
Prior art keywords
surfactant
weight
salt
superheavy oil
emulsion fuel
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Abandoned
Application number
CA 2102030
Other languages
French (fr)
Inventor
Noboru Moriyama
Akio Hiraki
Tsugitoshi Ogura
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kao Corp
Mitsubishi Heavy Industries Ltd
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Publication of CA2102030A1 publication Critical patent/CA2102030A1/en
Abandoned legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/32Liquid carbonaceous fuels consisting of coal-oil suspensions or aqueous emulsions or oil emulsions
    • C10L1/328Oil emulsions containing water or any other hydrophilic phase

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  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Liquid Carbonaceous Fuels (AREA)

Abstract

Abstract A superheavy oil emulsion fuel, which is excellent in not only handleability as a fuel by virtue of its low viscosity but also long-term stability, comprising at a highly swellable fine clay mineral, a superheavy oil, a surfactant and water.

Description

2 ~ 0 2 ~ 3 ~

SUPERHEAVY OIL EMULSION FUEL ~ ~ ;
. :, .. .
:: :
Background of the Invention -Field o-f the Invention The present invention relates to a superheavy oil emulsion fuel.
Description of the Related Art 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 ca-tegory 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 distlllation residues.
Oleaginous materials containing about 60 to 70%
or, in some cases, 70% or more of a heavy fraction having a boiling point o-f 420 to 450C or, in some cases, 450C or above, do not -flow as such or have a vlscos:Lty as high as tens of thousands o-f centipoises or more. For this reason, Lf use as a fuel is - 1 - , ~':
':

2~ ~03~ :

intended without heating it to a temperature as high as 280 to 300C, there occurs not only problems in handling, atomization, etc., but also problems in the clogging o~ piping, etc., which renders it very difficult to use.
A proposal has hitherto been made with respect to an oil-in-water type (0/W type) emulsion fuel of a superheavy oil produced by emulsi-fying a superheavy oil (0) 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 Paten* Publication-A Nos. 313592/19B9 (Published on December 19, 1989) and 97788/1991 (Published on April 23, 1991)]. The emulsion fuel has a viscosi-ty relatively close to that of water and can be su-fficiently atomized at a temperature range of from ordinary temperatures to 90C, and therefore is a -fuel having very good handleability. In such an 0/W
type emulsion -fuel, the lower the content o-f' W
(water), that is, -the higher the content of 0 (oil), the better the quality o-f the fuel and the lower the fuel 109~ . tn order to handle the emulsion -f'ueL ln the same manner as that of conventional liquid -fue:L

2~L~2~3~ ~

oils, it is necessary that the emulsion fuel has long-term stability, su~icient to withstand transportation and storage. However, the emulsion -f'uel 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 -~
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 handleabllity as a fuel by virtue of its low viscosity but also possesses long-term stability of :
the emulsion.
As a result of various studies, the present inventors have found that a stable emulsion can be provided by using a particular, highly swellable ~ine clay mineral such as smectite, vermiculite or chlorite and that an O/W superheavy oil emulsion having a lower vlscosity and a better long-term stability can be provided by using a surfactant ln combination wlth the 21~2~3~

above-~escribed particular clay mineral, which has led to the completion o~ the present invention.
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 sur-factant and water.
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 descrlption.
Detailed Description of the Invention The clay mineral to be used in the present inventlon 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 sweL:Lably claY mineral that has a water molec~lle relaxation time (T2) of 900 msec or less, pre-ferably .. . , . ~ ~ , . . ~ . ,., . -- - - - .- .

2~2~3~) ~
,~ , 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 (T2) in excess of 900 msec, is used1 the water binding force of the clay mineral is so small that the effect of the yresent invention can not be su-~iciently obtained.
The term "fine clay mineral" is in-tended to mean a clay mineral having an average particle diameter of 100 ~m or less. When a clay mineral having an avera~e~
particle diameter of above 100 ~m 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.
Specifically, fine clay minerals having a high swellability and a high water molecule binding force, for example, smectite, vermiculite and chlorite, fal:L -within the scope of the present invention. Among them, however, those having a T2 value in excess of 900 msec are outside the scope of'-the present in~ention.
~'urther, slnce kaolln native to Georgia, general kdo:Lln and -talc have a low water molecule binding force, they are excluded from the scope of the presen-t invention.

21~2~3~

Highly swellable fine clay minerals, such as smectite, vermiculite and chlorite, to be used in the present invention will now be described.
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:
Xm(~ Y )20r3Z410(OH)2 nH2 wherein X represents K, Na, 1/2Ca or 1/2Mg; y2+
represents M~, Fe(II), i.e., Fe2+, Mn(II), i.e., Mn2+, Ni or Zn; Y3+ represents Al, Fe ~III), i.e., Fe3+, Mn(III), i.e., Mn3f, or Cr(III), i.e., Cr3+; and Z
represents Si or Al; provided that X, Y and Z
represent a intercalated cation, an octahedral cation and a tetrahedral cation, respectively.
Representative examples of smectite are as Yollows.
Dioctahedral (octahedral cations be:ln~ mainly trivalent):
montmorillonite represented by, for example, tlle ~ormula: X033(~ 67Mgo~33)s:l~olo(oH)2 nH2~
belde:L:Li-te represented by, for exampl~, the ~ormula: ~o~33(Al2)(~lo~33sl3~67)olo(ofl)2 n~[2o~ and 21 D2~30 nontronite represented by, for example, the formula: Xo33(Fe(III)2)(Alo~33si3~67)olo(oH)2 nH2o~
Trioctahedral (octahedral cations being mainly divalent):
saponite represented by, for example, the formula: xo33(Mg3)(A10.33Si3.67)10(H)2 nH2' .
iron saponite represented by, for example, the formula: X0.33(Mg, ~e(II))3(A10.33si3.67)10(H)2 nH2' hectorite represented by, for example, the ormula: XO 33(Mg2~67Lio~33)si~olo(oH)2 nH2~
sauconite represented by, -for example, the formula: X033(Mg, Zn)3(si3.67A10.33)10(H)2 n~l2~ and stevensite represented by, for example, the - ~ -formula: Xo~33l2(Mg2~97)si4olo(oH)2 nH2' 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.
The vermiculite belongs to 2 : 1 layer silicates and is represented by, ~or example, the following C;lellli cal f'ormula:
(Mg, ~e(III), Al)2ol~3(s~ x~lx)olo(~fl)2(M ~ M 1/2).(~ 2 In the above formula, M represents an ~ 2~2-~3~ :

intercalated exchangeable cation. When the vermiculite is ln 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. A vermiculite in the coarse particle form produced by the weathering of biotite and phlogopite is a trioctahedral one.
The structure o-f 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 classi.~:Led into a tr:Loctahedral chlori-te and a dio~tahedral one accordlng to the nature of the 2 : :L
layer. The tr:Loctahedral chlorite is represented by, for exaMple, the following formu:la:

~ 21~2~3~
, ::

(R6-X2+R~3)(si4xAl~)olo(oH)8 or (R2+6XR3+x)(si4-xAl~)lO(OH)8 Although R2t is mainly composed of Mg and Fe(II~
i.e., Fe2~, it also includes Mn(II), i.e., Mn2~, Ni, etc. R3+ is malnly composed of Al and also includes Fe(IlI), i.e., Fe3+, Cr(III), i.e., Cr3+, etc. X in the above formula is a value of 0.8 to 1.6. a chlorite wherein R2+ is composed mainly of Mg is called "clinochlore" [e.g., (Mg5Al)(Si3Al)Olo(OH)8], and one wherein R2+ is composed mainly of Fe(II) is called "chamosite" [e.g., (Fe5Al)(Si~Al)010(OH)8]. Examples of other trioctahedral chlorites include pennantite wherein ~2+ is composed mainly of Mn(II), and nimite wherein R2+ is composed mainly of Ni.
The dioctahedral chlorite wherein the octahedral cation is composed mainly of Al is classified into three types, i.e., Sudoite [e.g., (Mg, A1)46or5(Si, A1)4O1o (OH)8], cookeite [e.g., (LiA14)(Si3Al)O1o(OH)8]
and donbassite [e-g-, Al40r4.2Ro.2-(si~ A1)410(H)8]-Those which are composed mainly o-f montmoril]onLte, L.e., a clay materia] belongin~ to smectLte, and contain, as lmpurlt3es, quartz, ~-cristobalite, opal, feldspar, mica, zeolite, calcite, dolom:Lte, gypsum and iron oxlde, are called "bentonlte". The bentonite is cLassl~ied into sodlum 2~2~30 bentonite rich in Na ion and calcium bentonite rich in Ca ion. The sodium bentonite falls within the scope o-f the clay mineral of the present invention because o-f 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.
Of the sodium bentonites, those with a higher montmorillonite content are preferred. The particle diameter is 100 ~m or less, preferably 10 ~m or less.
The sodium bentonite falling within the scope of the clay mineral of the present invention should have a water molecule relaxation time (T2) 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 wei~ht 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 T2 value of the aqueous suspension of the resultant sodium bentonlte becomes low, When such sodlum bentonltes are employed -that the e-~fect of the present invention becomes better.

2 ~ ~ 2 ~ 3 ~ ~ ~

The above-described clay minerals may be used alone or in the form o-f 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 wei~ht, the water binding -force of the clay mineral is insu-fficient, 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 resultan-t emulsion unsuitable as a fuel.
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 hi.gh temperature:
(1) petroleum asphalts and mixtures thereof;
(2) various treated products of petroleum asphalts, intermediates, residues, and mixtures -thereo~`;
(3) oils hav:Lng a high pour polnt that do not flow even at a high temperature, or crude oil;
(4) petroleum tar pitches and mlx-tures thereo-f;

, .;,:

;' : ' -2~203~

and (5) bitumens.
In the present invention, the superheavy oils are an oleagrinous substance that contains about 60% by weight or more of a heavy distillate having a boiling point of 420 to 450C or, in some cases, 450C or above as a vacuum residue. These superheavy oils may be used alone or in the form of a mixture thereof.
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.
(I) A sulfonic acid of an aromatic ring co~pound such as naphthalene, alkylnaphthalene, a]kylphenol and alkylbenzene or a salt thereof, or a formal:in (f'ormaldehyde) condensate of a sulfonic acid of an aromatic rin~r compound or a salt thereof, wherein the average de~rree of condensation of formalin is 1.2 to 100 and the sa:Lt is an ammonium salt, a lo~ver amine ~alt such as a monoethano:l.amLne, diethanol.amine, trle-tharlolamine or tr:Leth~lam:Lne sal-t, or an alka:Li metal or alkaline earth metal salt such as a sod:ium, i: - :: , : : : . : - - . , . , , :.: .: : , ,. ,.: , . - : . ~ ~ .

2~ ~2~

potassium, magnesium or calcium salt.
(II) Ligninsulfonic acid, a salt thereo-f or a derivative thereof, or a -formalin (~ormaldehyde) condensate o-f ligninsulfonic acid and a sulfonic acid o~ an aromatic compound such as naphthalene or alkylnaphthalene, or a salt thereo-f, 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 o~ ~ormalin 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 sal-t, or an alkali metal or alkaline earth metal salt such as a sodium, potassium, calcium or magnesium salt. .
(IV) A polymer o-~ dicyclopentadienesulfon:ic acid or a salt thereo~, wherein the mo:lecular weight i.s 500 -to 500,000 and the salt is an ammon:Lum salt, a ].ower amine sa:lt such as a monoethanolamine, diethanolarnine, - - , . ~ . - . . , . . ... . ~

:` 21~2~3~

triethanolamine or triethylamine salt, or an alkali metal or alkaline earth metal salt such as a sodi.um, 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 thereo-f, 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 es-ter 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 C~l8 alkane-, alkene- or alkylarylsulfonic acld or a salt tthereo~, wherein -the sa].t is an ammonlum salt, a lower amine salt such as a 2~2~

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) A sulfosuccinic acid es-ter salt of a saturated or unsaturated alcohol having 4 to 22 carbon atoms, wherein the sal-t is an ammonium salt, or an alkali metal salt such as a sodium or potassium salt; - ~ ~
(e) An alkyldiphenyletherdisul~onic 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 alka]i earth metal salt such as a sodium, potassium, magnesium or calcium salt.
(-~) 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 lllcludes, ~or example, a mixed tal] acld comprlsLng a tall rosin and a tall ol:L -~atty acld, l.e., a h:Lgher -fatty acid, a tall rosin, a ~um rosin, a wood rosin 2~ ~2~.3~

and salts thereof.
(g) An C418 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 -sulfofatty acid ester salt having an alkyl group o-f 4 to 22 carbon atoms or a derivative thereo-f.
The nonionic sur-factants 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 phenol:Lc hydroxyl group, such as an alkylphenol, phenoJ., m-creso:l, styrenated pheno:l. or benzylated pheno:l., wherein -the average degree o-f' conclensation is 1.2 to 100, preferably 2 -to 20, and the alkylene oxide :Ls ethylene oxlde, propylene oxlde, butylene oxide, styrene oxide, ethylene oxide/propy:Lene oxicle, r~ 2 1 ~ 2 ~
~.

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 es-ter of the above-described polyhydric alcohol with a fatty acid having 8 to 18 carbon atoms, wherein the alkylene oxide ls ethylene oxide, propylene oxlde, buty:Lene oxide, styrene oxide, ethylene oxide/propylene oxide, ekhylene oxlde/butylene oxide or ethylene oxide/
styrene oxide.

2~2~3V ~ ~ ;

(vi) An alkylene oxide adduct o-f a polyamine or the like having a plurality o-f active hydrogen a*oms, 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 o-f an alkylene oxide with a mixture o-~ 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 ~lycerol, trimethylolpropane, pentaerythritol, -~
sorbitol, sucrose, ethylene glycol, polyethylene glycol having a molecular weight of 1000 or less, propylene glycol and polypropylene glycol having a molecular weigh* of 1000 or less, wherein the alkylene oxide is ethylene oxide, propylene oxide, butylene oxide, styrene oxide, ethylene oxide/propylene oxide, ethylene oxlde/butylene oxlde or ethylene ox:icle/
Ytyrene oxide.
(vll:L) An adduct o-~ a tal:l oi:L -fatty acid, a :
tall rosin, a gum rosln, a wood rosin or a mixture thereof with an alkylene oxide.

2 1 ~ 2 ~
;.. ~;

(ix) A mono- 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 Or an aromatic ring compound having in its molecule one or more carboxyl ~roups and derived from petroleum or coal with an alkylene oxide.
(xi) A mono- and/or diester of an aromatic ringr cornpound having in its molecule one or more carboxyl groups and derived from petroleum or coal with an alkylene oxide polymer.
The cationic sur~actants and amphoteric surfactants to be used in the present invention include following ones.
(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):

IR2 ¦
Rl-N-R4 X~ la) wherelrl Rl, R2~ R3 and R4 represent each an alkyl or alkeny:l. grroup havi.ngr 1 to 18 carbon atoms and X~
reprcsents a counter aniorl, e.g., chlorine ion and bromine ion, 2 1 ~ 2 ~

R2 1 ~
R~ N-R~ X
CH2 _ (b) :.

wherein Rl, R2, R3 and X9 are as defined above, and ~;

[ g~\ R s ~ ( c ) wherein R5 represents an alkyl or alkenyl group having 8 to 18 carbon atoms, R6 represents a hydrogen atom or a methyl group and Xa is as defined above.
(3) An alkyl- or alkenylbetaine represented by - the following formula: -CH2CoO3 wherein R represents an alkyl or alkenyl group having 8 to 18 carbon atoms.
(~) An alky:L- or alkenylamine ox:Lde represented by t;he follo~lng Eormula:

f~l3 R-N~0 C~13 - . . . . ~ -: . , . .~: . - , - ,: .

2 1 0 2 ~

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):
RNHC3H6NHY ( d) ..
RNHC3H6N\ ( e ) wherein R is as defined above and Y and Y' represent ~-each an oxyethylene chain represented by the formula -tC2H40t~-H wherein m is 1 to 50.
(7) A polyamine salt represented by the following formulae (f) or (g):
RNHc3H6NH2x RN't[C3H6N~lCs~l6NH2x whereirl R is as defi.ned above and X' represent,s an lnor~an:Lc or organic acid, e.~., hydrochloric acld and acetic acid.
t8) An amphoteric imidazoline surfactant represented by the following formula:

21~2~

~--GHz R--C

E[OCH2CEl2 1 CH~

wherein R is as defined above.
(9) An amphoteric sulfobe-taine sur-factant -represented by the following formula:

.: :, R-N-CH2-~H-CH2S0 wherein R is as defined above. :
Although the above-described highly swellable clay minera]. has excellent ef~ect o-f stabilizin~ the -~

superheavy oi.l emulsion fuel, it has an insu-fficient e-ffect of reducing the size of oil droplets.
Therefore, the combination use of the highly swellable ~-clay mi.neral and a sur-factant excel].ent in the e-f-fect o-L' reducing the s:Lze of oil drop:Le~ts can provlde more stab:l.e emu:ls:lon fuel. For this reason, the use o-f a mixturc of an ionic surfactant with a nonionic surfactant ls particularly pre-ferred. E:specially, it is preferrecl that the weight ratio of the lonic --~` 21~2~3~

surfactant to the nonionic sur~actant be 1 : 99 to 80 : 20. Further, an excellent effect can be attained also when use is made of a system comprising an anionic sur~actant and, incorporated therein, a small amount of a cationic surfactant, for example, a system comprising 100 parts by weight of an anionic surfactant and, lncorporated 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, incorporate~ therein, 20 parts by weight or less (but not 0) of an anionic -surfactant.
The above-described surfactan~s 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.Z to 1.5 parts by weight, based on 100 parts by weight o-f 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 t:Lme, -the stability o-t the emulsion sys-tem becomes unsatisfactory. On the other hand, when the content exceeds 3.0 parts by weight, the thlckening of the emulsion system becomes slgni.-ficant un-favorably and, since the emulsi-fier is more ,, , . .. , . , . : ., .; :: ;:

-- 2:~0~3~

expensive than the oil, such a high content is disadvantageous from the economic viewpoint.
The superheavy oil emulsion fuel of the present invention comprises the above-described components and water and is produced by emulsi-fying 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 pre-ferably 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 co rse particles which are causati~e of the generation of soot and dust.
The superheavy oil emulsion fuel of the present invention may comprise, in addition to the above-described components, at least one o-f 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 usùally 0,OOL to 1.0 part by wei.ght;, preferab:l.y 0.005 ~o 0.5 part by welght, base(l on :L00 parts by we:Lght o~ the en-tire amount of -the superheavy oil emulsion fue:L.
The hydrophi:Lic polymer is classified into a naturally occurring hydrophllic polymer and a water-soluble synthetic polymer.

- 2~ -2~ ~2~

Hydrophilic polymers derived ~rom naturally occurring matter include the following ones.
(A) Hydrophi].ic 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, NH~, Ca or Mg) thereof (b) Derived from seeds:
(i) locust bean gum (ii) guar gum (iii) tara gum ~iv) tamarlnd gum (c) Trees (exudates):
(:L) gum arablc (ii) gum karaya (iii) gum tragacanth ~ ~ ~ 2 ~

(d) Derived from fruits:
(i) pectin :;
(C) Hydrophilic Polymers Derived from Animals (Proteins) .
(i) gelatin :~
(ii) casein (D) Naturally Occurring Polymer Derivatives (i) cellulose deriva-tives (such as carboxyrnethyl.cellulose) (ii) chemieally modi-fied starch Hydrophilic, that is, water-sol-uble synthetic polymers include following ones.
(E) A homopolymer or copolymer o~ acrylic acid or a derivative tbereo~ represented by the following formula: :~

C~{2 I-Zl~

CozH1 n whercln R' represents a hydrogen at;om, a methyl group or an ethyl group; Ml represents a hydrogen a-tom, a sodiurn lon, a potassium ion, a l:Ltt~ m ion or an ammoniurn ion; Zl represents a diva:Lent group derived 21~2~

from a monomer represented by the formula CH2=C
CO~l (wherein R' and Ml are as de-fined above), a comonomer copolymerizable with the monomer or a salt o-f the comonomer, for example, maleic acid (an:hydride), itaconic acid (anhydride), a-olefin, acrylamide, vinylsulfonic acid, allylsulfonic acid, methallyl-sulfonic 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:

tCH~ fH Z2 ~
fo n NH

R"

2 ~ 0 2 ~

wherein R" represents a hydrogen atom or a C2H40H
group; Z2 represents a divalent group derived from a monomer represented by the formula: CH2-CH (wherein R" -~
CO ~ ~ ~
NH

is as de-fined above), a comonomer copolymerizable with the monomer or a salt of the comonomer, for example, vinylsulfonic acid, allylsulfonic acid, methallyl~
sulf'onic acid. acrylamidomethylpropylsul-fonic acid or a salt (NH4, Na, K or Li) thereof, a dialkyl(methyl or ethyl)aminoethylmethacrylate or a salt (chloride, dimethylsul~ate or diethylsulfate) thereof, styrene, a-olefins (C218) and vinylallyl alcohol; and n is 50 to iOO,000. ~, (G) A hopopolymer of maleic anhydride or itaconic anhYdride~ or a copolymer thereof represen-ted by the following formula:

~ Mrz3~il wherein M2 represents a maleic anhydride or itaconic anhydride residue; Z3 represents an a-olefin ~ethylene, propylene, butylene, isobutylene, oc-tene, decene, dvdecene or the llke) or styrene residue; and n is 50 to 100,000.

.:

2~2~3~

~H) A homopolymer of vinyl alcohol, or a copolymer thereof represented by the following formula:
' ~2 IH Z

OH n~

wherein Z~ 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: : ; .
t f J
~ ,o fH2 f~
~:

wherein Z5 represents a divalent group derived from a c~monomer copolymerizable with viny:l.pyrrolldone or a salt (N~l~, Na, K or Li) thereof', -for example, acrylamide, vinylsulfonlc acid, methallylsulfonlc : :;
': :

2 ~ 3 ~

.
acid, maleic anhydride, itaconic anhydride or a salt (NH4, Na, K or Li) thereof, styrene, a-olefin (C218) 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 o-f a block polymer o~ propylene oxide, butylene oxide or styrene oxide, or an alkylaryl or alkyl group.
In the production of the superheavy oil emulsion fuel o-F 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 o~
shear ra~e. Specific examples of the mechanical means -include a model M TK homomixer (manufactured by Tokushu Kika Kogyo Co,, Ltd.) and a line mixer.
The superheavy oil emulsion fuel o-F the present invention thus produced usually has a viscosity as low as 1000 cP or below (at 60DC) and a high percentage undersize, so that it is very easy to handle as a ~uel and is further excellent, particularly in long-term ~
stablllty in the dispersed sta-te after the emulslon is le:Ft to stand. Spec:Lfically, it has the advantage of a remarkable suppression of the generation of coarse partlcies and the thickening phenomenon.

' - `
2 ~ 0 2 ~

Brief Description of the Dr-awing Fi~. 1 is a schematic view of a centrifuge tube used for the evaluation o-f the dispersed state after standing, wherein 1 is the surface layer, 2 is the intermediate layer and 3 is the sedimentation layer.
Examples 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 Middle Eastern petroleum-derived asphalt (penetration: 60 - 80), water, a surfactant and a highly swellable clay mineral were weighed respectively in ~iven amounts (total amount: 300 g) to ~:
give compositions specified in Tables 1 to 3, put into :-~:;
an 800-ml centri~ugation tube and heated to 75C. ~ -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-~iscosity agitation blade; manufactured by Tokushu Kika Kogyo Co., Ltd.)~
to prepare emulsion fuels, which were stored at 60C. :-. :
AL'ter the temperature of the emulsion Puels became constant, the viscosl-ty o-t each -~uel was measured wi-th a Model VS-~1 Vismetron (No. 2 rotor, number of - - :.. :: : .: :,: , :: ,:.~,.,:. , ~ : : :

~ ~ o ~

revolutions of the rotor: 60 rpm) manufactured by Shibaura Systems Co.l Ltd. Part of the emulsion fuel was maintained at 50C 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 percenta~e undersize of a 100-mesh ~ ;
sieve. The percentage sieve undersize was determined by putting abou-t 10 g o-f a sample on a 100-mesh stainless sieve of 70 mm~ in an atmosphere at 50C, measurin~ the oversize after 10 min, and calculating the undersize. The results are given in Tables 1 to 3.
The overall evaluation was conducted by collectively evaluating the viscosity of the emulsion, ;
percentage sieve undersize, and visual observation o~ ;
the dispersed state after the emulsion was left to stand. The overall evaluation is better in the following order: ~ > o > ~ > x, and the effect of the present invention was observed in the systems in which -the overall evaluation was ~ or better.
Wlth respect -to the dlspersed state after standlng, the states of three layers as shown in Fig.
1, i.e., sur~ace ].ayer 1, intermediate layer 2 and sedimentation ]ayer 3, were observed and separately evaluated.

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 ~ilm" ~ "large amt. of oil droplet" > "small amt. of oil film" > "large arnt. of oil film". Namely, "no oil droplet" is best and "large amt. of oil film" is worst.
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.
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 so-ft sediment is a sediment which is soft and easily redispersible, while the hard sediment is a sediment which is hard alld dl~f:Lcult to redisperse.

~ 2~ ~2~

11' ., ~

V ~ V _ V _ V O _ V _~ ~ O _ V _~ V O ~ V ~ _ ~0:. ~ v ~ 3~ 5~ 50 30~ 0 30~ o ..
~1 V _ 2J
C_. V _ _ V _ V _ _ _U~ _ J~ _ Cl O ~ O ~ O
~ ~q ~ -I --V ~ --V ~ --V ~--v _~ O _ Cl ~ :
_ ~ ~ o ~ . o a o =s _ V 3 3 ~
t~. O ~ ~ _ tO ~ -~ ~ tO Cl _~ _1 co ~ ~ CO CD a o ~ ~ _ v o _ C ~1 3 C O ~ ~ O C V 3 O Cl ~ ~ 3 o V 3 C) V~ ~ O SV o ~V o ~V ~ V~_ VVV~

_,J O CD _ CO O V _ ~O _ _ _, _ O V _ CO _ ~ O C) , : ~:
ti~ - C~ C3~ - = Cl 3 _ CO V t3D C o ~ V5 C 3 ~-~J VX a C
_l -- O -- L'~

~V C) co o _ t~ co LqLq ~r _ ' CD ,, V C) tO' .^ o o~ o ~o ~ CJ .
CJ t~ t J ~ Lq It~ t-CJvc I _ ~ V ~:
_' 0 O ê7~o, O O O _~~
~ a _ a o ~ C v ~r '`o o o o ~n V ~1 V IJ C L Ci Cl O O r--l 0 3 ~J _ SC '-~ -a a ~ -o - o - o . c~
co ~ i 3 o o o Lq o ~1 a ~,_ ~ t t t ~ 2;
x ~ = ~ ~ ~

.

- . . . : :. -., -: -: . , , , , ~ ~. ; . : ... .

2102~3~

. .
d ~ C O
~ :~- ~I ~I O O <~ LO
OC~ _ V - _ U~
V O CJ - o_ V e_~ o V ~ - V -V O
~ O V V _ V V _ V _~ V O _ o _ V _~ V C1 _ _ ~. :
-- ~ a -- ~ 5 5 ~ -- ~ -- -- ~ 'O -- _ 5 a v l7 ~ ~ ~ ~ 1 ~l a ~ ( ~ G~ _I v O c~ uJ 4 ~o `q c~ _I v !a v v u~ o o u~ o c~ u~ o c~ 3 o c ~ 3 --o ~ ~ 0 v __ o C) C~ O~ e_ V ~ V V _ V - :L~ -O
?~ q O v ~ 9 L. v C~ 2~ C~ a v- V 3 V C~ ~ V ~ ~, ~ C~ a 3 ~ a ~ ~ - _ 3 ,q a a O ~ , - v o _ v _ ~ v --~ ~ a o a ~ _ ~J u~ o o ~ ~ u~ O ~, a v 3 ~d 3 O O a _ ~ 3 o o ~ 3 _ a ~~ 3 Lq -- 'q L, -- ~ ~ V ~ V V o ~V~ o V _ :~ _ -- V ~ .
a V V o -- -- ~ -- ~ 3 _ _ A ~ ~ a ~ _ _ _ ~

~ a ,1 a ~ o c~ u~ o x 5 0 O ~< 5 0 o X 5 _ ~ o c~ ~ ~. a ~ _.
2 V ,~ C.~ 0 0 _ Lq ~ C~l Lq 'q _ _ O

C~ L. a Lq -~ v v ~ a -- o L Lq ~r O _ _ _ _ _ _ V '' O U
;~ a ~ o o o o o ,,~ L- o C 3 0 ~C 3 :~
cJ a o o o o o a ~ a ra o ~ d C ~ ~ ~ v d d ~z ~ u _ _ ~ ~ a 3 bO L. ~ a~ ~ a~ -- - -- - - ~ -rn ~Jrn CJ 3 o o o o o v 3~? r v ~ ~ ~r rU
CC' _ ::
c~ o cn o 2102~3~ ::
C~

. _3 ~ v o ~ 3 0 0 a o 3 ~ " _ . .

_ O ~ _V ~ V V U ~ O _ _ V _ -- _ V~ _ ~ '~ O ~ :~ _ O ~ ~ ~ ~ ~ 1 0 3 :.C X ~ _ _ X 3 0 O ~: ~ _ X 3 0 ~ 3 o ~ _~
V ~ -- ~ ~ ~ ~ D

_ oc ~ a c co ~ a oc c # a oc ~-0 ~ a o 3~o 3 a co ~ V ~ V V ~ _ r v .0 v ~--_L'~ r L'7 ~r c~ 3 -- O _ V L~ V V
O a- O o ~r L" O O . . ~

O~ ,~
_~ _g O O _~ ~0 ", '.'.~, ~ C ~r ~r ~r ~r ~r o ~ '~ _ rV o~J ~_ - _ ~, v v -~ o . ~1 :~1 O --? 0 ~ ~
_ ~0 _ ~ r i ~ r r r v ~.: __ cl .~ ~ _~ ,, 2 1 0 2 ~

-. '~';.' ~'"' ' . - .
Comparative Examples 1 to 4 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 S to 7 ~-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.

- 37 - ~ :

2 ~ 0 2 ~
_ . ..
>~>~ X ., X X X l l O ~ _ G G G e G e ., ~o ._ ._ ': '_ _ _ _ ~ .
n -- -- I ~
1~5 G ., I G v~ v G <.. -o _ _ .9 9 G v~ ¦ G 1 9 _ ~ ~n ~ ~ ~> ~ <D ~ <~ I ~ ~
~D ~ .~ ~ G ~ e . e ~ ~ V ' " '' ' " ~' " ' C ' 1 - ~
_~ ._ ~

_ -O a G G G a G C O
._ ~:cn o 3 C o ~D C -- -- o .--C ~ --C O ~ C --O ._ c c) O~
_ O _ _ ._ _ _ ._ _ _ ._ a c .--v _ _ ._ _ _ ._ G C ._ v O t~.1~ ~A ~ C ~ ~ G ~ ID a .D a ~= ~

. .. a ~ .~ o _ ,~ ~ _ _ _ _ _ ~ _ V _ _G _ G G G G G o U~
V _,_ ,_ _ _ _ _ _ o _ o_ _ Co ~ ~ .

_ G o v G v~ ve v, v G ~ -- G e c --v _ _ O _ 8 c -- G V
~r _ . G ~ 8 _ oG `-- cn ---- -- ---- -- ---- -- -- -- _ _-- -- U ~ o O C L"

~_ V,V ~8~ o ~ ~ ~ ~ ~ ~ _ ~
o~ ~ o J~V ~ ' ~
~o o o O ~ o C.O o r~
,~o. _ CO 1~> _ _ _ _ V ~ O ~U
,L~C ~ ~_î ~ e~ _ ;;~
X C~ ~70 o o o o o o Q~ O :;5 aa -~ c 'a ~ o O O -- _ ~ ~ ~ ~

~~ .~, "' . _~ O '' ~' 'v. ~ 'v~--8 O o O O ô O _ _ ~ O L'~
~ ~ 1_~ =~

OX _ _ _ ~ ~_ r_ ,. - . . - . . - . , ~ : . ~. ., . :. . .

,- 2la2~3~ l Examples 16 to 18 Emulsion fuels having compositions specified in Table 5 were prepared in the same manner as that of Examples 1 to 15, except that ~thabasca bitumen (softening temperature: 12.5C, 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 An emulslon fuel having a composition specified in Table 5 was prepared in the same manner as that o-f :
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.

2~ 3~ ~

,., o o o o _ __ _ O _ _ V _ V CJ V O V --_ :~J _~ V ~ V 'I O V :. V 3 0 V ~_ _ _, V
O V _O ~ __ V _ V _ ::1 _ o _ ~ 0 0 V V 1 _X -- 5 _ X =1 0 0 0 V V _ O ,~ _ ~,V _ _ C`l W O _ V _ V _ C- OV ..
Q, 0 -5--v v~ v v ,, --v --v V V
_ _ ~d C v O V v O V d 3 -- L'd 3 ---- 3 -- --_ ~ V '---- d 3 ----~ U~
o _~, o _ _ 0 ~, __~ 0 v ~' _1 0 v o q-. ~ 0 v C ~-1 ~~0 V _ 0 O V _ ~q O V _ 0 ~ ~ r-l d ~ _ O O O C C V V C C V V C a 0 ~ 3 0 O -v ~ v ~ V O v C ~0 ~ . .
O O ~ ~v 0 3 _ vv V5 V ~ V d :, , V -: _ V '~ _ V '_ _ d _ O -.-- ,, ~ ~ o v 0 ~ O O _ V O _ 0 v a ~
~ o - o - V V C ~ O~ o V o C ~ ,.
_ O o~ Lq Lq V O 0 _ -- Lq V Vu ~ C`J t- q ~ O
_ ~, ~ ~ o n ~r m c~ o tn_ U ~ ~~~ ~ _ ~
v ~ VU ~ .. O ô ~ O ~, ~
~ ~a, o o o o ~ ~
~ ~ ~o ~

tl~ d ~ V m -! m o _ o o a . O _ ~ _ ~ ~ o v~) ~ i~:
~ ~ co o~:

~ 40 ~

:" ,, :'.' ' . , ": ,, , ,. :"; ` :. ' :: ' '' ': ,. ': ' ' '.': , . ' '': - : . ., ; :, . :- '. , ' 2~
, :

Examples 19 to 22 :~
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 ~ive compositions specified in Table 6, put into a 300-ml centrifugation tube and heated to 75C.
A-fter the temperature o-f 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 60C. .
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 Emulsion fuels havin~ compositions specified in Table 6 were prepared in the same manner as that o-f' ~xamples 19 to 22, except tha-t no use was made of h:lghLy swel:Lable clay minera:L. The fuels were evaluated in the same manner as that of Examples 19 to 22. The results are also given :Ln Table 6.

2102~3~

o o ~ o ':~ ~

J v C v C v C v C ~ v v C
C C ~ v C v v 3 w v ^ v v O o _ C v a o C 5 o _ _ ~ _ U, O a c o _ _ ' ~ 0 - O a 5 v 0 . _ _ _ _ _ _ 0 o _ _ 0 a _ _ 0 a O ,"~ r, _ _ ._ r v a O ,, O o _ 0 o a _ ~ o c, _ r O O ~ 0 _ _ O ' O O _ ~ .0 0 v _ O -- O O _~ 5 0 C O a c O -- O _ O u _ O ~ 5 a ~
r a v C V -- v c v _ c v = o C J, C v v C '~ v v v O O v O C v v ~ v _ ,~,Cl r~ ---- _ rJ C _ 5 -::~ C C~ _ ^~ C _ _,~ V U _ ~ VC ,U sa_ o , _ _ _ ~ _ _ _ ~ a ~ _ a ~ _ a _ o ~_ o o I_ _ o ~ o o _ a _ _ 0 o o o _ 0 _ _~ ~a o o x ~ o a _ x 5 0 O _. 5 0 C`~
, oc o o ~ c ~ o c c o o c c o o c _ o o o ~ c o o c 0 ~ o 00-' C -V -~, -V O O -' -V 'VV C ~V ,_1 ~ 0 v ~ . v a Oc ~ v U Oc LO. V U Oc ' U O a c o J c o w ._ _ ~ - _ = ~ ~ 0 o _ _ 0 ~ _ _ _ _ . ~ 0 o~ ~ 0 o V ~ _ a o o _ D~ o o _ 0 o o _ u, UJ ~ 0 _ o _ 0 u ~ L-O-. O
o ~ - o c o o = o _ e o cO O aO C e O O O CO _ _ O ~, ~::1 , 0 0_ ,J _ ~r :~ C~ ~ _ q oV ~ ~ ~1 _ O C l C~ O ~ ~ Lq ,ooC C C Lq 0 0-- a o ~ ~ o I '~ O --I
U V --o L-- O _~ O _ I _ . I _ _ V
_ ~ u a ~J -- ~ '-~ V O
_ c a ' ~ o o ~ o o O c _ a o c o o w ,, v ~ _ a ~C - -3 v _ ~ .a C
~ t.~C a ~ a _ _ O _ O O _~ " 5 3:~ ,c'U~ ~ o .. , __ _ 0 ;" _ O _ _ Lq _ L ~ . . O Lq .~ O X
:C ~ O O O O O ~

_I' __ _ _ _ ,_~ ~t _ C ~r ~r r .~ r _ ~0 J '-`t CC' C-, L:~ s . ¦ e ~ 42 ~

a ~

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 undersi~e 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 o-f 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.
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 o-f .
Comparative Examples 9 and 10 wherein no use was made of highly swellable clay mineral.

The invent.lon belng thus described, it wil~ be obvious that the same rnay be varied in many ways.

"~"-;~ ""~ , "",, ,," ,, , ,~,,,", j";,,, ",, ,", ~

2~2~V

Such variations are not to be regarded as a departure -from the spi.rit and scope of the invention, and all such modifications as would be obvious to one ski:Lled in the art are intended to be included within the scope of the following claims.

Claims (8)

1. A superheavy oil emulsion fuel comprising at a highly swellable fine clay mineral, a superheavy oil, a surfactant and water.
2. The superheavy oil emulsion fuel according to claim 1, wherein said clay mineral has a water molecule relaxation time (T2) of 900 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, and has an average particle diameter of 100 µm or less.
3. The superheavy oil emulsion fuel according to claim 1, wherein said surfactant is a surfactant mixture comprising an ionic surfactant and a nonionic surfactant with the weight ratio of the ionic surfactant to the nonionic surfactant of 1 : 99 to 80 : 20.
4. The superheavy oil emulsion fuel according to claim 1, wherein said surfactant is a surfactant mixture comprising 100 parts by weight of an anionic surfactant and above 0 to 20 parts by weight of a cationic surfactant.
5. The superheavy oil emulsion fuel according to claim 1, wherein said surfactant is a surfactant mixture comprising 100 parts by weight of a cationic surfactant and above 0 to 20 parts by weight of an anionic surfactant.
6. The superheavy oil emulsion fuel according to claim 1, which comprises the superheavy oil, and, based on 100 parts by weight of the superheavy oil, 0 05 to 2.5 parts by weight of the clay mineral, 0.05 to 3.0 parts by weight of the surfactant and 20 to 85 parts by weight of the water.
7. The superheavy oil emulsion fuel according to claim 1, which further contains a hydrophilic polymer.
8. The superheavy oil emulsion fuel according to claim 7, wherein the content of the hydrophilic polymer is 0.001 o 1.0 part by weight based on 100 parts by weight of the entire amount of the superheavy oil emulsion fuel.
CA 2102030 1992-10-30 1993-10-29 Superheavy oil emulsion fuel Abandoned CA2102030A1 (en)

Applications Claiming Priority (2)

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JP4-316414 1992-10-30
JP31641492A JPH06145677A (en) 1992-10-30 1992-10-30 Super heavy oil emulsion fuel

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CA2102030A1 true CA2102030A1 (en) 1994-05-01

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JPH08325582A (en) * 1995-06-01 1996-12-10 Kao Corp Production of superheavy oil emulsion fuel
CA2205294A1 (en) * 1996-05-23 1997-11-23 Kao Corporation Method for producing superheavy oil emulsion fuel and fuel produced thereby
US7344570B2 (en) * 2001-08-24 2008-03-18 Clean Fuels Technology, Inc. Method for manufacturing an emulsified fuel
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EP0595640B1 (en) 1997-04-16

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