Processes for producing a transportation fuel from a renewable feedstock

Patent metadata

Field	Value
Publication number	US-2016289568-A1
Application number	US-201514677530-A
Country	US
Kind code	A1
Filing date	Apr 2, 2015
Priority date	Apr 2, 2015
Publication date	Oct 6, 2016
Grant date	—

Abstract

Processes for the production of transportation fuel from a renewable feedstock. A gaseous mixture of carbon monoxide and hydrogen is used to deoxygenate and hydrogenate the glycerides to produce long chain hydrocarbons. The hydrocarbons may be isomerized to improve cold flow properties to provide a diesel fuel. Prior to isomerization, the long chain hydrocarbons can be separated or the separation can be after isomerization. Recycle gas streams from the isomerization and the deoxygenation and hydrogenation reactions may be used to supply at least a portion of the gaseous mixture of carbon monoxide and hydrogen. Synthesis gas may also be used to supply at least a portion of the gaseous mixture of carbon monoxide and hydrogen.

First claim

What is claimed is:

1 . A process for producing a transportation fuel from a renewable feedstock comprising:
passing a liquid stream comprising oil derived from a biomass to a reaction zone; passing a gaseous stream to the reaction zone, the gaseous stream comprising a mixture of hydrogen and carbon monoxide; operating the reaction zone under conditions to remove oxygen from the oil and to hydrogenate the oil to provide an effluent; and, isomerizing at least a portion of the effluent to increase a cold flow property of the at least a portion of the effluent.

2 . The process of claim 1 wherein the gaseous stream comprises a molar ratio of hydrogen to carbon monoxide of between 50:50 to 99:1.

3 . The process of claim 1 wherein the gaseous stream comprises a molar ratio of hydrogen to carbon monoxide of between 50:50 to 80:20.

4 . The process of claim 1 wherein the gaseous stream comprises synthesis gas.

5 . The process of claim 4 wherein the synthesis gas is produced from a biomass.

6 . The process of claim 1 wherein the gaseous stream comprises a steel production gaseous stream.

7 . The process of claim 1 wherein the gaseous stream comprises a refinery gas stream.

8 . The process of claim 1 wherein the transportation fuel comprises green diesel.

9 . A process for producing a transportation fuel from a renewable feedstock comprising:
passing a renewable feedstock to a deoxygenation zone, the renewable feedstock comprising vegetable oil; passing a gaseous stream to the deoxygenation zone, the gaseous stream comprising a mixture of hydrogen and carbon monoxide; deoxygenating the renewable feedstock in the deoxygenation to remove oxygen from the vegetable oil and to hydrogenate the vegetable oil and to provide a deoxygenated effluent; separating the deoxygenated effluent into a recycle gas and a liquid effluent, wherein the recycle gas forms a portion of the gaseous stream; isomerizing at least a portion of the liquid effluent to provide an isomerized effluent; and, separating a transportation fuel from at least a portion of the isomerized effluent.

10 . The process of claim 9 wherein the gaseous stream comprises a molar ratio of hydrogen to carbon monoxide of between 50:50 to 99:1.

11 . The process of claim 9 further comprising:
separating the liquid effluent into a heavy effluent and a light effluent, the light effluent comprising the portion of the liquid effluent that is isomerized.

12 . The process of claim 11 further comprising:
mixing at least a portion of the heavy effluent with the renewable feedstock to form a combined feed.

13 . The process of claim 11 further comprising:
quenching the deoxygenation zone with at least a portion of the heavy effluent.

14 . The process of claim 9 further comprising:
separating the isomerized effluent into a second recycle gas stream and a liquid isomerized effluent, wherein the second recycle gas forms a portion of the gaseous stream.

15 . The process of claim 14 further comprising:
separating the liquid isomerized effluent into a product and a bottoms, wherein the product comprises a transportation fuel.

16 . The process of claim 15 further comprising:
mixing at least a portion of the bottoms with the renewable feedstock to form a combined feed.

17 . The process of claim 15 further comprising:
quenching the deoxygenation zone with at least a portion of the bottoms, with a recycle gas stream, or both.

18 . The process of claim 9 further comprising:
removing carbon dioxide from the recycle gas to provide a carbon dioxide lean gaseous stream, wherein the carbon dioxide lean gaseous stream forms a portion of the gaseous stream.

19 . The process of claim 18 further comprising:
passing a portion of the carbon dioxide lean gaseous stream to an isomerization zone; and,
isomerizing at least a portion of the liquid effluent to increase a cold flow property of the at least a portion of the liquid effluent in the isomerization zone to provide an isomerized effluent.

20 . The process of claim 9 wherein at least a portion of the gaseous stream comprises synthesis gas.

Assignees

• Uop Llc

Inventors

• Dutta Kanchan
• Kumar Avnish
• Mani Krishna
• Ray Anjan

Classifications

• C10G45/58 Primary

  to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins (C10G32/00 takes precedence; improving or increasing the octane number or aromatic content of naphtha C10G35/00) · CPC title

• C10L2270/026

  for diesel engines, e.g. automobiles, stationary, marine · CPC title

• C10G3/46 Primary

  in combination with chromium, molybdenum, tungsten metals or compounds thereof · CPC title

• C10L1/026

  for compression ignition · CPC title

• C10L2290/10

  Recycling of a stream within the process or apparatus to reuse elsewhere therein · CPC title