Process for removing oxygenates from hydrocarbon streams

Patent metadata

Field	Value
Publication number	US-10160921-B2
Application number	US-201815901550-A
Country	US
Kind code	B2
Filing date	Feb 21, 2018
Priority date	May 25, 2016
Publication date	Dec 25, 2018
Grant date	Dec 25, 2018

Abstract

A system for removing oxygenates from a hydrocarbon stream includes a caustic wash unit comprising a plurality of caustic wash loops, and a hydrogenation reactor. The hydrogenation reactor is configured to receive a first gaseous stream from a first caustic wash loop of the plurality of caustic wash loops and pass a second gaseous stream from the hydrogenation reactor to a second caustic wash loop of the plurality of caustic wash loops, wherein the hydrogenation reactor comprises a sulfided catalyst.

First claim

What is claimed is:

1. A system for removing oxygenates from a hydrocarbon stream, the system comprising:
a caustic wash unit comprising a plurality of caustic wash loops; and
a hydrogenation reactor configured to receive a first gaseous stream from a first caustic wash loop of the plurality of caustic wash loops and pass a second gaseous stream from the hydrogenation reactor to a second caustic wash loop of the plurality of caustic wash loops, wherein the hydrogenation reactor comprises a sulfided catalyst.

2. The system of claim 1 , further comprising:
a cracking unit configured to convert one or more hydrocarbons to lighter products, wherein the cracking unit is fluidly coupled to the caustic wash unit and is arranged upstream of the caustic wash unit.

3. The system of claim 2 , wherein the cracking unit comprises a fluid catalytic cracking unit, a steam cracking unit, or any combination thereof.

4. The system of claim 2 , wherein the cracking unit comprises:
a fluid catalytic cracking unit;
a separation unit fluidly coupled to the fluid catalytic cracking unit and configured to receive a first product stream from the fluid catalytic cracking unit and separate a dry gas stream from the first product stream; and
a steam cracking unit fluidly coupled to the separation unit and configured to receive the dry gas stream from the separation unit.

5. The system of claim 2 , further comprising:
a quenching unit arranged between the cracking unit and the caustic wash unit, wherein the quenching unit is configured to cool a product stream from the cracking unit prior to the product stream passing to the caustic wash unit.

6. The system of claim 1 , wherein the sulfided catalyst comprises a sulfide of nickel, zinc, copper, gallium, cadmium, chromium, molybdenum, tungsten, cobalt, ruthenium, iron, or any mixtures thereof.

7. The system of claim 1 , further comprising:
a dryer fluidly coupled to the caustic wash unit, wherein the dryer is configured to receive a gaseous product stream from the caustic wash unit and remove at least a portion of the water in the gaseous product stream.

8. The system of claim 1 , further comprising:
a separation unit fluidly coupled to the caustic wash unit, wherein the separation unit is disposed downstream of the caustic wash unit, and wherein the separation unit is configured to receive a gaseous product stream from the caustic wash unit and separate the gaseous product stream into a plurality of product streams.

9. The system of claim 1 , wherein the caustic wash unit comprises a caustic wash tower, and wherein the caustic wash tower comprises at least one of a packed column or a plate absorption column.

10. The system of claim 1 , wherein the sulfided catalyst comprises a sulfided nickel catalyst or a sulfided copper catalyst.

11. A system for removing oxygenates from a hydrocarbon stream, the system comprising:
a hydrocarbon stream, wherein the hydrocarbon stream comprises one or more hydrocarbons, one or more oxygen containing components, and one or more sulfur containing compounds
a caustic wash unit comprising a plurality of caustic wash loops, wherein the caustic wash unit is configured to receive the hydrocarbon stream and produce a first gaseous stream in a first caustic wash loop of the plurality of caustic wash loops; and
a hydrogenation reactor configured to receive the first gaseous stream from the first caustic wash loop of the plurality of caustic wash loops and pass a second gaseous stream from the hydrogenation reactor to a second caustic wash loop of the plurality of caustic wash loops, wherein the hydrogenation reactor comprises a sulfided catalyst, and wherein the hydrogenation reactor is configured to convert at least a portion of the one or more sulfur containing compounds in the presence of the sulfided catalyst to hydrogen sulfide in the second gaseous stream.

12. The system of claim 11 , further comprising:
a cracking unit configured to convert one or more hydrocarbons to lighter products in the hydrocarbon stream, wherein the cracking unit is fluidly coupled to the caustic wash unit and is arranged upstream of the caustic wash unit.

13. The system of claim 12 , wherein the cracking unit comprises a fluid catalytic cracking unit, a steam cracking unit, or any combination thereof.

14. The system of claim 12 , wherein the cracking unit comprises:
a fluid catalytic cracking unit;
a separation unit fluidly coupled to the fluid catalytic cracking unit and configured to receive a first product stream from the fluid catalytic cracking unit and separate a dry gas stream from the first product stream; and
a steam cracking unit fluidly coupled to the separation unit and configured to receive the dry gas stream from the separation unit.

15. The system of claim 12 , further comprising:
a quenching unit arranged between the cracking unit and the caustic wash unit, wherein the quenching unit is configured to cool a product stream from the cracking unit prior to produce the hydrocarbon stream.

16. The system of claim 11 , wherein the sulfided catalyst comprises a sulfide of nickel, zinc, copper, gallium, cadmium, chromium, molybdenum, tungsten, cobalt, ruthenium, iron, or any mixtures thereof.

17. The system of claim 11 , further comprising:
a dryer fluidly coupled to the caustic wash unit, wherein the dryer is configured to receive a gaseous product stream from the caustic wash unit and remove at least a portion of the water in the gaseous product stream.

18. The system of claim 11 , further comprising:
a separation unit fluidly coupled to the caustic wash unit, wherein the separation unit is disposed downstream of the caustic wash unit, and wherein the separation unit is configured to receive a gaseous product stream from the caustic wash unit and separate the gaseous product stream into a plurality of product streams.

19. The system of claim 11 , wherein the caustic wash unit comprises a caustic solution, wherein a concentration of the caustic solution used in each caustic wash loop of the plurality of caustic wash loops increases from the first caustic wash loop to a last caustic wash loop of the plurality of caustic wash loops.

20. The system of claim 11 , wherein the hydrogenation reactor is configured to remove at least 80% of the one or more sulfur containing compounds from the first gaseous stream.

Assignees

• Fluor Tech Corp

Inventors

• Dierickx Jan

Classifications

• C10G55/06 Primary

  including at least one catalytic cracking step · CPC title

• C10G59/02

  plural serial stages only · CPC title

• C10G2300/4087

  Catalytic distillation · CPC title

• C10G70/02

  by hydrogenation · CPC title

• C10G2300/1037

  Hydrocarbon fractions · CPC title