초록 ▼

A process for the conversion of high boiling organic materials to lower boiling materials is described. The process comprises contacting said high boiling organic materials under supercritical conditions in a reducing atmosphere with an aqueous acidic medium containing a halogen, a hydrogen halide,

A process for the conversion of high boiling organic materials to lower boiling materials is described. The process comprises contacting said high boiling organic materials under supercritical conditions in a reducing atmosphere with an aqueous acidic medium containing a halogen, a hydrogen halide, a compound which can form a halide or a hydrogen halide in the aqueous acidic medium under the process conditions, or mixtures thereof. Under the supercritical conditions of the process, the high boiling organic materials and aqueous acidic medium form a single phase allowing efficient conversion of the high boiling materials to lower boiling materials. The process of the invention is useful for producing and recovering fuel range liquids from petroleum, coal, oil shale, shale oil, tar sand solids, bitumen and heavy hydrocarbon oils such as crude oil distillation residues. Preferably, the aqueous acidic medium contains a halogen or a hydrogen halide.

대표청구항 ▼

1. A process for the conversion of high boiling organic materials to lower boiling materials comprising contacting said high boiling organic materials at a temperature of from about 300° to 1000° C. and at a reaction pressure of from about 2000 to 9,000 psi in a reducing atmosphere with an aqueous a

1. A process for the conversion of high boiling organic materials to lower boiling materials comprising contacting said high boiling organic materials at a temperature of from about 300° to 1000° C. and at a reaction pressure of from about 2000 to 9,000 psi in a reducing atmosphere with an aqueous acidic medium containing, as a promoter, a halogen, a hydrogen halide, a halogen-containing organic compound which can form a halide or a hydrogen halide in the aqueous acidic medium under the process conditions, or mixtures thereof whereby the high boiling organic material and aqueous acidic medium form a substantially single phase system. 2. The process of claim 1 wherein the organic material is contacted with a halogen or a hydrogen halide. 3. The process of claim 1 wherein the high boiling organic material is coal, oil shale, shale oil, tar sand solids, bitumen or a heavy hydrocarbon oil. 4. The process of claim 2 wherein the halogen is chlorine or bromine. 5. The process of claim 2 wherein the hydrogen halide is hydrogen chloride or hydrogen bromide. 6. The process of claim 1 wherein the weight ratio of water to high boiling organic materials used in the process is in the range of from 0.1:1 to about 50:1. 7. The process of claim 1 wherein the weight ratio of water to high boiling organic materials used in the process is in the range of from about 0.5:1 to about 5:1. 8. The process of claim 1 wherein the weight ratio of promoter to organic material is from about 0.001:1 to about 0.5:1. 9. The process of claim 1 wherein the reducing atmosphere contains hydrogen. 10. The process of claim 9 wherein the hydrogen partial pressure is from about 500 to 5000 psi. 11. A process for recovering fuel range liquids from heavy hydrocarbon oil feedstocks which comprise (a) contacting a heavy hydrocarbon oil feedstock at a temperature of from about 375° to 600° C. and at a pressure of from about 2000 to 9,000 psi in a reducing atmosphere with an aqueous acidic medium containing as a promoter, a halogen, a hydrogen halide, or a halogen-containing organic compound which can form a halide or a hydrogen halide in the aqueous acidic medium under the process conditions, or mixtures thereof, whereby the heavy hydrocarbon oil feed stocks and aqueous acidic medium form substantially a single-phase system for a period of time sufficient to provide the desired conversion of feedstock to fuel range liquids, (b) allowing the mixture to form an aqueous phase and an organic phase, and (c) separating the organic phase from the aqueous phase and recovering the fuel range liquids from the organic phase. 12. The process of claim 11 wherein the heavy hydrocarbon oil feedstock is shale oil. 13. The process of claim 11 wherein the aqueous acidic medium contains a halogen. 14. The process of claim 13 wherein the halogen is chlorine or bromine. 15. The process of claim 11 wherein the aqueous acidic medium contains a hydrogen halide. 16. The process of claim 15 wherein the hydrogen halide is hydrogen chloride or hydrogen bromide. 17. The process of claim 11 wherein the weight ratio of water to hydrocarbon oil feedstock is from about 0.5:1 to about 5:1. 18. The process of claim 11 wherein the hydrocarbon oil feedstock is in contact with the acidic water-containing medium in step (a) for a period of from about one minute to about six hours. 19. The process of claim 11 wherein the reducing atmosphere contains hydrogen. 20. The process of claim 19 wherein the hydrogen partial pressure is from about 500 to 5000 psi. 21. A process for converting heavy hydrocarbon oil feedstocks to fuel range liquids which comprises (a) contacting said heavy hydrocarbon oil feedstocks in a reducing atmosphere with an aqueous acidic medium containing a halogen, a hydrogen halide, or a mixture thereof at a temperature in excess of 375° C., and at a pressure of at least about 2000 psi whereby the temperature and pressure are sufficient to maintain the mixture of hydrocarbon oil feedstock and aqueous acidic medium in a substantially single-phase system for a period of time sufficient to provide the desired degree of conversion of the feedstock to fuel range liquids, (b) allowing the mixture to form an aqueous phase and an organic phase, and (c) separating the organic phase from the aqueous phase and recovering the fuel range liquids from the organic phase. 22. The process of claim 20 wherein the aqueous acidic medium contains hydrogen chloride. 23. The process of claim 21 wherein the weight ratio of water to heavy hydrocarbon oil is in the range of from about 0.5:1 to about 5:1. 24. The process of claim 21 wherein the heavy hydrocarbon oil is shale oil. 25. The process of claim 21 wherein the heavy hydrocarbon oil is a crude oil distillation residue. 26. The process of claim 21 wherein the acidic medium contains hydrogen halide and the weight ratio of hydrogen halide to heavy hydrocarbon oil feedstock is in the range of from about 0.001:1 to about 0.5:1. 27. The process of claim 21 wherein the hydrocarbon oil feedstock is in contact with the aqueous acidic medium in step (a) for a period of from about one minute to about six hours. 28. The process of claim 21 wherein the reducing atmosphere contains hydrogen. 29. The process of claim 28 wherein the hydrogen partial pressure is from about 500 to 5000 psi.