Processes for producing fuels from a renewable feed

Patent metadata

Field	Value
Publication number	US-9822314-B2
Application number	US-201514678268-A
Country	US
Kind code	B2
Filing date	Apr 3, 2015
Priority date	Apr 3, 2015
Publication date	Nov 21, 2017
Grant date	Nov 21, 2017

Abstract

Processes for the production of hydrocarbons from a renewable feedstock in which the renewable feedstock is partially hydrogenated prior to being deoxygenated. The partially hydrogenation utilizes a lower pressure, lower purity or both hydrogen gas compared to the deoxygenation. The partially hydrogenated product may be stored in containers and transported to be deoxygenated. Prior to partially hydrogenation, the feedstock may be pretreated. After deoxygenation an isomerization zone may be used to increase the cold flow properties for a diesel fuel.

First claim

What is claimed is:

1. A process for producing a transportation fuel from a renewable feedstock, the process comprising:
pretreating a renewable feedstock to remove contaminants from said renewable feedstock in a first pretreatment zone to provide a pretreated feedstock;
pre-hydrogenating the pretreated feedstock in a pre-hydrogenation zone, the pre-hydrogenation zone comprising at least one reactor having a hydrogenation catalyst and being operated under conditions to partially hydrogenate the pretreated feedstock to provide a pre-hydrogenated feedstock that has at least 50% of phosphorus removed;
removing contaminants from said pre-hydrogenated feedstock;
deoxygenating the pre-hydrogenated feedstock in a deoxygenation zone, the deoxygenation zone comprising at least one reactor having a catalyst capable of deoxygenating the pre-hydrogenated feedstock under deoxygenation conditions and providing a deoxygenated effluent;
separating a liquid portion from said deoxygenated effluent comprising mostly normal paraffins, and separating a gaseous portion from said deoxygenated effluent comprising hydrogen, carbon dioxide, carbon monoxide, water vapor, propane, at least one sulfur component and a phosphorus component;
wherein both the pre-hydrogenation zone and the deoxygenation zone receive a hydrogen gas stream, and wherein the hydrogen gas stream received by the pre-hydrogenation zone has a lower purity, a lower pressure or both compared to the hydrogen gas stream received by the deoxygenation zone and;
isomerizing said liquid portion in an isomerization zone comprising a reactor having a catalyst capable of isomerizing at least a portion of said liquid portion to provide an isomerized effluent;
separating at least one transportation fuel stream from said isomerized effluent.

2. The process of claim 1 and wherein the hydrogen gas stream received by the pre-hydrogenation zone has a lower purity and a lower pressure compared to the hydrogen gas stream received by the deoxygenation zone.

3. The process of claim 1 wherein the pressure of the hydrogen gas stream received by the deoxygenation zone is at least 2 MPa.

4. The process of claim 1 wherein the purity of the hydrogen gas stream received by the deoxygenation zone is at least 90%.

5. The process of claim 1 wherein the reactor in the isomerization zone and the reactor in the deoxygenating zone are the same.

6. The process of claim 1 further comprising:
storing the pre-hydrogenated feedstock in containers.

7. The process of claim 6 further comprising:
transporting the containers of the pre-hydrogenated feedstock to the deoxygenation zone.

8. The process of claim 1 further comprising:
removing contaminants from the pre-hydrogenated feedstock in a guard bed prior to deoxygenating the pre-hydrogenated feedstock in the deoxygenation zone.

9. A process for producing a transportation fuel from a renewable feedstock, the process comprising:
passing a renewable feedstock to a first pretreatment zone, the pretreatment zone comprising at least one reactor configured to degum the renewable feedstock, bleach the renewable feedstock, polish the renewable feedstock or a combination thereof, to provide a pretreated feedstock;
passing the pretreated feedstock to a pre-hydrogenation zone, the pre-hydrogenation zone comprising at least one reactor having a hydrogenation catalyst and being operated under conditions to partially hydrogenate, in the presence of hydrogen, the pretreated feedstock to provide a pre-hydrogenated feedstock that has at least 50% of phosphorus removed;
removing contaminants from said pre-hydrogenated feedstock:
passing a first hydrogen containing gas to the pre-hydrogenation zone, the first hydrogen containing gas having a first pressure and a first purity;
passing the pre-hydrogenated feedstock to a deoxygenation zone, the deoxygenation zone comprising at least one reactor having a catalyst capable of deoxygenating, in the presence of hydrogen, the pre-hydrogenated feedstock under deoxygenation conditions to provide a deoxygenated effluent; and,
passing a second hydrogen containing gas to the deoxygenation zone, the second hydrogen containing gas having a second pressure and a second purity;
wherein the second pressure is at least 2 MPa, and
wherein at least one of the second pressure and the first pressure and the first purity and the second purity are different,
isomerizing the deoxygenated effluent in an isomerization zone, the isomerization zone comprising a reactor having a catalyst capable of isomerizing at least a portion of the deoxygenated effluent to provide a isomerized effluent; and,
separating at least one transportation fuel stream from the isomerized effluent.

10. The process of claim 9 further comprising:
separating at least one transportation fuel stream from the deoxygenated effluent.

11. The process of claim 9 wherein the first pressure is lower than the second pressure and wherein the first purity is less that the second purity.

12. The process of claim 11 wherein the second purity is greater than 90%.

13. The process of claim 9 further comprising:
storing the pre-hydrogenated feedstock in one or more containers prior to passing the pre-hydrogenated feedstock to the deoxygenation zone.

14. The process of claim 9 wherein the pre-hydrogenated feedstock is passed to the deoxygenation zone without passing through a guard bed.

15. The process of claim 9 further comprising:
removing contaminants from the pre-hydrogenated feedstock in a guard bed prior to deoxygenating the pre-hydrogenated feedstock in the deoxygenation zone.

16. The process of claim 9 wherein the pre-hydrogenated feedstock is rich in saturated oils.

17. The process of claim 9 further comprising:
passing the deoxygenated effluent to a separation zone having a separation vessel and a fractionation column;
separating the deoxygenated effluent into liquid hydrocarbon stream and a vapor hydrocarbon stream in the separation vessel; and,
separating the liquid hydrocarbon stream into a light hydrocarbon stream, a naphtha stream and a diesel stream.

Assignees

• Uop Llc

Inventors

• Ray Anjan

Classifications

• C11C3/12

  by hydrogenation · CPC title

• Y02T50/678

  Aviation using fuels of non-fossil origin · CPC title

• C10L1/04

  essentially based on blends of hydrocarbons · CPC title

• Y02E50/13

  Cross-Sectional Technologies · mapped topic

• C10G3/42

  Catalytic treatment · CPC title