Process for the production of fuel compositions

Claim 2

A process for producing a w/o type dispersion composition suitable for use as a fuel, comprising kneading (a) a bituminous substance which is a semi-solid or heavy liquid substance having a viscosity of at least 20 cSt at 50° C., (b) a low molecular weight aliphatic alcohol, and (c) water, a water-containing organic compound, or an aqueous organic compound suspension, said water-containing organic compound and said aqueous organic compound suspension being a mixture of fine solid organic compound particles or liquid organic compound particles and water, said kneading being performed at a temperature ranging between about 0° C. and 65° C., to provide a w/o type dispersion composition wherein the aqueous alcohol solution as a dispersed phase is dispersed in the bituminous substance as an continuous phase.

Claim 3

A process for producing a o/w type dispersion composition suitable for use as a fuel which comprises kneading (a) a bituminous substance which is a semi-solid or heavy liquid substance having a viscosity of at least 20 cSt at 50° C., (b) a low molecular weight aliphatic alcohol, and (c) water, a water-containing organic compound, or an aqueous organic compound suspension, said water-containing organic compound and said aqueous organic compound suspension being a mixture of fine solid organic compound particles or liquid organic compound particles and water, said kneading being performed at a temperature ranging between about 0° C. and 65° C., to provide a w/o type dispersion composition wherein the aqueous alcohol solution as a dispersed phase is dispersed in the bituminous substance as a continuous phase, adding to said w/o type dispersion composition (d) a protective colloid in an amount of 1.5 to 5 parts by weight per 100 parts by weight of the bituminous substance contained in said w/o type dispersion composition, said protective colloid being selected from the group consisting of polyvinyl alcohol, a partial saponification product of polyvinyl acetate, a partial saponification product of an ethylene-vinyl acetate copolymer, and mixtures comprising two or more thereof, and kneading the resulting mixture at a temperature ranging between about 5° C. and 60° C., to cause phase inversion of said dispersion composition and to provide a o/w type dispersion composition wherein the bituminous substance as a dispersed phase is dispersed in the aqueous alcohol solution as a continuous phase.

Claim 4

A process for producing a o/w type dispersion composition suitable for use as a fuel which comprises kneading (a) a bituminous substance which is a semi-solid or heavy liquid substance having a viscosity of at least 20 cSt at 50° C., (b) a low molecular weight aliphatic alcohol, and (c) water, a water-containing organic compound, or an aqueous organic compound suspension, said water-containing organic compound and said aqueous organic compound suspension being a mixture of fine solid organic compound particles or liquid organic compound particles and water, said kneading being performed at a temperature ranging between about 0° C. and 65° C., to provide a w/o type dispersion composition wherein the aqueous alcohol solution as a dispersed phase is dispersed in the bituminous substance as a continuous phase, adding to said w/o type dispersion composition (d) a protective colloid in an amount of 1.5 to 5 parts by weight per 100 parts by weight of the bituminous substance contained in said w/o type dispersion composition, said protective colloid being selected from the group consisting of polyvinyl alcohol, a partial saponification product of polyvinyl acetate, a partial saponification product of an ethylene-vinyl acetate copolymer, and mixtures comprising two or more thereof, and kneading the resulting mixture at a temperature ranging between about 5° C. and 60° C., to cause phase inversion of said dispersion composition and to provide a o/w type dispersion composition wherein the bituminous substance as a dispersed phase is dispersed in the aqueous alcohol solution as a continuous phase.

Claim 5

A process as in claim 1 or 2, wherein the components (a), (b), and (c) are kneaded at a temperature ranging between about 0° C. and 65° C.

Claim 6

A process as in claim 1 or 2, wherein the components (a), (b), and (c) are kneaded in a kneader at a rotary speed of the stirring blade of the kneader of from 5 to 240 rpm.

Claim 7

A process as in claim 1 or 2, wherein the components (a), (b), and (c) are kneaded until the amount of water absorbed in the bituminous substance reaches from 5 to 70 parts by weight per 100 parts by weight of the bituminous substance.

Claim 8

A process as in claim 1 or 2, wherein the weight ratio of the low molecular weight aliphatic alcohol to the water, or water contained in the water-containing organic compound or the aqueous organic compound suspension, is from 1/0.1 to 1/10.

Claim 9

A process as in claim 1 or 2, wherein the components (a), (b), and (c) are kneaded simultaneously.

Claim 10

A process as in claim 1 or 2, wherein the components (a) and (b) are first kneaded, and then the component (c) is added thereto and kneaded.

Claim 11

A process as in claim 1 or 2, wherein the components (a) and (c) are first kneaded, and then the component (b) is added thereto and kneaded.

Claim 12

A process as in claim 1 or 2, wherein the components (a), (b), and (c) are kneaded in the presence of a sulfur trapping agent.

Claim 13

A process as in claim 10, wherein the sulfur trapping agent is selected from the group consisting of Ca(OH) 2 , CaCO 3 , (HCOO) 2 Ca, Ba(OH) 2 , BaCO 3 , (HCOO) 2 Ba, CaCO 3 .MgCO 3 , Mg(OH) 2 , MgCO 3 and (HCOO) 2 Mg.

Claim 14

A process as in claim 1 or 2, wherein the components (a), (b) and (c) are kneaded in the presence of a protective colloid present in an amount of from 0.05 to 0.5 part by weight per 100 parts by weight of the bituminous substance in the course of preparing the water-in-oil type dispersion composition, said protective colloid being selected from the group consisting of a partial saponification product of polyvinyl acetate, a partial ester of polyvinyl alcohol with a higher aliphatic acid, and a vinyl acetate-vinyl alcohol-vinyl alcohol higher aliphatic acid ester copolymer.

Claim 15

A process as in claim 12, wherein the protective colloid is selected from the group consisting of polyvinyl alcohol, a partial saponification product of an ethylene-vinyl acetate copolymer, a partial saponification product of polyvinyl acetate, a partial ester of polyvinyl alcohol with a higher aliphatic acid, and a vinyl acetate-vinyl alcohol-vinyl alcohol higher aliphatic acid ester copolymer.

Claim 16

A process for producing a fuel composition which comprises mixing a w/o type dispersion composition, wherein an aqueous low molecular weight aliphatic alcohol solution is dispersed in a bituminous substance according to the process of claim 1, with an oil-soluble liquid to convert the dispersion composition into a w/o type dispersion composition whose water content is from 5 to 70 parts by weight per 100 parts by weight of the bituminous substance.

Claim 17

A process for producing a fuel composition which comprises mixing a o/w type dispersion composition, wherein a bituminous substance is dispersed in an aqueous low molecular weight aliphatic alcohol solution according to the process of claim 2, with water, a low molecular weight aliphatic alcohol, or a mixture thereof, to convert the dispersion composition into a o/w type dispersion composition whose water content is from 5 to 70 parts by weight per 100 parts by weight of the bituminous substance.

Claim 18

A process as in claim 1 or 2, wherein the bituminous substance is selected from the group consisting of asphalt, crude oil, a distillation residue of oil, tar, pitch, and mixtures comprising two or more thereof.

Claim 19

A process as in claim 1 or 2, wherein the low molecular weight aliphatic alcohol is selected from the group consisting of methanol, ethanol, propanol-2, and n-propanol, and mixtures comprising two or more thereof.

Claim 20

A process as in claim 1, wherein the protective colloid is selected from the group consisting of polyvinyl alcohol, a partial saponification product of polyvinyl acetate, a partial saponification product of an ethylene-vinyl acetate copolymer, a partial ester of polyvinyl alcohol with a higher aliphatic acid, a vinyl acetate-vinyl alcohol-vinyl alcohol higher aliphatic acid ester copolymer, and mixtures comprising two or more thereof.

Claim 21

A process as in claim 1 or 2, wherein the water-containing organic compound or aqueous organic compound suspension is selected from the group consisting of active sludge, sewerage sludge, home waste sludge, peat, water-containing brown coal particles, water-containing coal powder, waste liquids containing suspension solids formed during cold rolling of iron, muddy substances in extracts produced as a by-product in the production of gelatin, muddy substances in molasses, oil tank sludge, aqueous wastes containing suspension solids by-produced in the production of palm oil, sweet water containing suspended fatty materials, aqueous wastes containing suspension solids by-produced in the production of paper, aqueous wastes containing suspension solids by-produced in the production of an ethylene-vinyl acetate emulsion polymer or vinyl acetate emulsion polymer, aqueous wastes containing suspension solids formed in the suspension polymerization of styrene, process water containing suspended solids formed in the production of epoxy resins, dyeing waste water containing suspended solids obtained during the step of dyeing, aqueous wastes containing oily substances from oil refining operations, cane juice containing colored substances in cane sugar processing, sulfuric acid washing waste liquids containing fine carbon particles and sludge resulting from sulfuric acid washing of gases in oil refining operations, oil-in-water type waste emulsions of cutting oil and rolling oil, oil-in-water type emulsions of oils and bituminous substances, and mixtures comprising two or more thereof.

Claim 22

A process as in claim 1 or 2, wherein the components (a), (b), and (c) are kneaded in a kneader at a rotary speed of the stirring of the kneader blade of from 10 to 120 rpm.

Claim 23

A process as in claim 1 or 2, wherein the weight ratio of the low molecular weight aliphatic alcohol to the water, or water contained in the water-containing organic compound or the aqueous organic compound suspension, is from 1/0.2 to 1/3.