Method of refining coal by short residence time partial liquefaction to produce petroleum substitutes and chemical feedstocks

Claim 2

An improved method for refining a volatile containing carbonaceous material in a partial liquefaction type process to produce a slate of hydrocarbon-containing products wherein char is gasified with oxygen and the resulting syngas subjected to a Fischer Tropsch type synthesis to produce liquids and a methane-rich gas comprising the steps of: (a) heating a particulate volatile containing carbonaceous material at a heat rate sufficient to maximize decomposition and minimize formation of char and condensation products to a volatilization temperature effective to produce a substantially decomposed volatilization product and char; and (b) contacting said substantially decomposed volatilization product with a hydrogen donor-rich gaseous atmosphere at a hydrogenation temperature effective to minimize formation of condensation products and reduce thermal cracking for a hydrogenation residence time effective to produce a hydrogenated volatilization product wherein said hydrogen donor-rich gaseous atmosphere is produced in substantial part from said carbonaceous material, including the gasification of said char.

Claim 3

The method of claim 1 comprising the further step of producing stabilized hydrogenated product by adjusting the temperature of said hydrogenated volatilization product to a stabilization temperature effective to substantially terminate formation of condensation products and thermal cracking of said hydrogenated volatilization product.

Claim 4

The method of claim 1 wherein said heating rate is at least about 10,000° F. per second and said volatilization temperature is from about 1,000° F. to about 2,000° F.

Claim 5

The method of claim 1 wherein said hydrogenation temperature is from about 900° F. to about 1,500° F. and said hydrogenation residence time is from about 0.1 seconds to about 5.0 seconds.

Claim 6

The method of claim 2 wherein said stabilization temperature is below about 1,000° F.

Claim 7

The method of claim 1 wherein said hydrogenation temperature is effected by direct partial quench.

Claim 8

The method of claim 6 wherein said direct partial quench is effected by using hydrogen donor-rich gas, or heavy hydrocarbon process liquid which heavy hydrocarbon process liquid is thermally cracked to produce lighter process liquids during said partial quench, or mixtures thereof.

Claim 9

The method of claim 1 wherein said hydrogen donor-rich gaseous atmosphere is obtained in substantial part from gasification of said char and wherein at least a part of said hydrogen donor-rich gaseous atmosphere and said volatilizing temperatures are produced in substantial part in a partial oxidation reaction wherein steam and hydrodisproportionation recycle gas rich in methane and carbon monoxide are reacted with a sub-stoichiometric amount of oxygen.

Claim 10

The method of claim 1 wherein said carbonaceous material is selected from a group consisting of coals, lignites, low rank and waste coals, peats, and mixtures thereof.

Claim 11

The method of claim 1 further comprising the addition of a methane-rich gas to said heating step in an amount effective to inhibit hydrocarbon gas formation wherein a substantial part of said methane is obtained from the gasification of said char.

Claim 12

An improved method for refining a volatile containing carbonaceous material in a partial liquefaction-type process to produce a slate of hydrocarbon-containing products wherein char is gasified with oxygen and the resulting syngas is subjected to a Fischer Tropsch type synthesis to produce liquids and a methane-rich gas comprising the steps of: (a) heating a particulate volatile containing carbonaceous material by admixing said particulate with a gaseous heating medium at a volatilization temperature of from about 1,000° F. to 2,000° F. and at a decomposing heat rate of at least 10,000° F. per second to produce a substantially decomposed volatilization product and char; (b) contacting said substantially decomposed volatilization product with a hydrogen donor-rich reducing gaseous atmosphere consisting essentially of hydrogen, steam, and carbon monoxide at a temperature of from about 900° F. to about 1,500° F. and at a hydrogenation residence time of from about 0.1 seconds to about 5.0 seconds to produce a hydrogenated volatilization product, said hydrogen and carbon monoxide being formed in substantial part in a partial oxidation reaction wherein steam and a hydrodisproportionation recycle gas rich in methane and carbon monoxide are reacted with a substoichiometric amount of oxygen wherein at least a portion of said methane is obtained from said gasification of said char; and (c) cooling said hydrogenated volatilization product to reduce the temperature of said product to below about 1000° F., said cooling accomplished at a rate to provide a total residence time from the heating of said carbonaceous material to said cooling of said hydrogenated volatilization product of between about 0.02 seconds and about 5.0 seconds.

Claim 13

An improved method for refining a volatile containing carbonaceous material in a partial liquefaction-type process to produce a slate of hydrocarbon-containing products wherein char is gasified with oxygen and the resulting syngas is subjected to a Fischer Tropsch type synthesis to produce liquids and a methane-rich gas comprising the steps of: (a) heating a particulate volatile containing carbonaceous material by admixing said particulate with a gaseous heating medium at a volatilization temperature of from about 1,000° F. to 2,000° F. and at a decomposing heat rate of at least 10,000° F. per second to produce a substantially decomposed volatilization product and char; (b) contacting said substantially decomposed volatilization product with a hydrogen donor-rich reducing gaseous atmosphere consisting essentially of hydrogen, steam, and carbon monoxide at a temperature of from about 900° F. to about 1,500° F. and at a hydrogenation residence time of from about 0.1 seconds to about 5.0 seconds to produce a hydrogenated volatilization product, said hydrogen and carbon monoxide being formed in substantial part in a partial oxidation reaction wherein steam and a hydrodisproportionation recycle gas rich in methane and carbon monoxide are reacted with a substoichiometric amount of oxygen wherein at least a portion of said methane is obtained from said gasification of said char; and (c) cooling said hydrogenated volatilization product to reduce the temperature of said product to below about 1000° F., said cooling accomplished at a rate to provide a total residence time from the heating of said carbonaceous material to said cooling of said hydrogenated volatilization product of between about 0.02 seconds and about 5.0 seconds.

Claim 14

The method of claim 11 wherein said contacting step temperature is effected by direct partial quench.

Claim 15

The method of claim 12 wherein said direct partial quench is effected by using a hydrogen donor-rich gas, or heavy hydrocarbon process liquid which heavy hydrocarbon process liquid is thermally cracked to produce lighter process liquids during said partial quench, or mixtures thereof.

Claim 16

The method of claim 11 wherein said hydrogen in said reducing gaseous atmosphere is obtained in substantial part from said carbonaceous material.

Claim 17

The process of claim 11 wherein said carbonaceous material is selected from a group consisting of coals, lignites, low rank and waste coals, peats, and mixtures thereof.

Claim 18

An improved method for refining a volatile containing coal by a partial liquefaction process employing a Fischer Tropsch type synthesis of syngas from process char to produce a slate of hydrocarbon containing co-products by short residence time hydroisproportionation comprising the steps of: (a) containing a particulate coal with a hydrogen donor-rich reducing gaseous mixture having a temperature in the range of about 1,300° F. to about 3,000° F. to heat said particulate coal at a volatilization temperature of from about 1,000° F. and about 2,000° F. at a heating rate greater than about 10,00° F. per second at pressures of from about 100 psig to about 2,000 psig for a time of from about 0.002 seconds to about 2.0 seconds to produce a substantially decomposed volatilization product and char, wherein said hydrogen donor-rich gaseous reducing gaseous mixture is obtained in substantial part from said carbonaceous material by a partial oxidation reaction wherein steam and hydroisproportionation recycle gas rich in methane and carbon monoxide are reacted with a sub-stoichiometric amount of oxygen and wherein said methane is produced in substantial part from the gasification of said char with a substoichiometric amount of oxygen in a gasifier; (b) cooling said substantially decomposed volatilization product to temperatures from about 900° F. to about 1,500° F. for residence times of from about 0.1 seconds to about 5.0 seconds to produce a hydrogenated volatilization product, wherein said cooling is effected by direct partial quench by using a hydrogen donor-rich gas or a heavy hydrocarbon process liquid, which heavy hydrocarbon process liquid is thermally cracked to produce lighter process liquids during said partial quench or mixtures thereof; and (c) stabilizing said hydrogenated volatilization product at a temperature of less than about 1,000° F. to produce a stabilized hydrogenated volatilization product wherein said stabilization is accomplished by contacting the hydrogenated volatilization product with a mixture of water and lighter oils, said mixture being recycled from said hydrodisproportionation process.

Claim 19

An improved method for refining a volatile containing coal by a partial liquefaction process employing a Fischer Tropsch type synthesis of syngas from process char to produce a slate of hydrocarbon containing co-products by short residence time hydroisproportionation comprising the steps of: (a) containing a particulate coal with a hydrogen donor-rich reducing gaseous mixture having a temperature in the range of about 1,300° F. to about 3,000° F. to heat said particulate coal at a volatilization temperature of from about 1,000° F. and about 2,000° F. at a heating rate greater than about 10,00° F. per second at pressures of from about 100 psig to about 2,000 psig for a time of from about 0.002 seconds to about 2.0 seconds to produce a substantially decomposed volatilization product and char, wherein said hydrogen donor-rich gaseous reducing gaseous mixture is obtained in substantial part from said carbonaceous material by a partial oxidation reaction wherein steam and hydroisproportionation recycle gas rich in methane and carbon monoxide are reacted with a sub-stoichiometric amount of oxygen and wherein said methane is produced in substantial part from the gasification of said char with a substoichiometric amount of oxygen in a gasifier; (b) cooling said substantially decomposed volatilization product to temperatures from about 900° F. to about 1,500° F. for residence times of from about 0.1 seconds to about 5.0 seconds to produce a hydrogenated volatilization product, wherein said cooling is effected by direct partial quench by using a hydrogen donor-rich gas or a heavy hydrocarbon process liquid, which heavy hydrocarbon process liquid is thermally cracked to produce lighter process liquids during said partial quench or mixtures thereof; and (c) stabilizing said hydrogenated volatilization product at a temperature of less than about 1,000° F. to produce a stabilized hydrogenated volatilization product wherein said stabilization is accomplished by contacting the hydrogenated volatilization product with a mixture of water and lighter oils, said mixture being recycled from said hydrodisproportionation process.

Claim 20

The process of claim 16 wherein said contacting is accomplished at a volatilization temperature of from about 1,200° F. to about 1,750° F. and a heating rate greater than about 50,000° F. per second and a residence time of from about 0.05 seconds to about 0.5 seconds.

Claim 21

The process of claim 16 wherein said cooling is accomplished at temperatures of from about 1,100° F. to about 1,300° F. and residence time of from about 0.2 to about 2.0 seconds.

Claim 22

The process of claim 15 wherein said stabilization step is accomplished at temperatures less than about 900° F.

Claim 23

The method of claim 16 wherein said partial oxidation reaction is carried out at temperatures of from about 1,800° F. to about 2,500° F. and pressure of from about 1,000 psig to about 2,000 psig with a mole equivalent of oxygen to CH 4 /CO of from about 0.5 to about 0.75.

Claim 24

The method of claim 16 wherein prior to said contacting, the particulate coal is first subjected to a preconditioning step wherein the carbonaceous material is contacted with CH 4 /CO rich recycle gas at from about 1,000 psig to about 2,000 psig at a coal/gas mix temperature of from about 450° F. to about 650° F. at residence times of from about 30 seconds to about 3 minutes.

Claim 25

The method of claim 16 comprising the addition of methane-rich gas to said heating step in an amount effective to inhibit the formation of hydrocarbon gas.