Paraffin dehydrogenation process and apparatus

Patent metadata

Field	Value
Publication number	US-11447707-B2
Application number	US-202017131453-A
Country	US
Kind code	B2
Filing date	Dec 22, 2020
Priority date	Dec 22, 2020
Publication date	Sep 20, 2022
Grant date	Sep 20, 2022

Abstract

A process for recovering hydrogen from dehydrogenation reactor effluent is disclosed. A feed stream comprising hydrocarbons and hydrogen to a dehydrogenation reactor maintained at dehydrogenation conditions to provide a dehydrogenation reactor effluent. The dehydrogenation reactor effluent is passed to a cold box separation unit to provide a liquid hydrocarbon product stream and a recycle hydrogen stream. A return portion of the recycle hydrogen stream is passed to the reactor effluent compressor. The subject matter disclosed improved process and apparatus which enables the paraffin dehydrogenation reactor to run at reduced H2/HC ratio without requiring an investment in a resized compressor or resized turboexpanders or separators in the cold box.

First claim

The invention claimed is:

1. A process for recovering hydrogen from dehydrogenation reactor effluent, the process comprising:
passing a feed stream comprising hydrocarbons and hydrogen to a dehydrogenation reactor maintained at dehydrogenation conditions to provide a dehydrogenation reactor effluent;
passing the dehydrogenation reactor effluent to a reactor effluent compressor to provide a compressed hydrocarbon stream;
passing the compressed hydrocarbon stream to a cold box separation unit to provide a liquid hydrocarbon product stream and a recycle hydrogen stream;
splitting the recycle hydrogen stream upstream of a cold combined feed exchanger located in the separation unit; and
passing a return portion of the recycle hydrogen stream to the reactor effluent compressor.

2. The process of claim 1 , further comprising mixing the return portion of the recycle hydrogen stream with the dehydrogenation reactor effluent to provide an enriched stream and passing the enriched stream to the reactor effluent compressor.

3. The process of claim 2 , wherein hydrogen to hydrocarbon ratio of the enriched stream is higher than hydrogen to hydrocarbon ratio of the dehydrogenation reactor effluent.

4. The process of claim 1 , further comprising splitting the recycle hydrogen stream into the return portion and a charge portion of the recycle hydrogen stream.

5. The process of claim 4 , wherein the return portion is 20-99 wt % of the recycle hydrogen stream and the charge portion is 1-80 wt % of the recycle hydrogen stream.

6. The process of claim 4 , further comprising mixing the charge portion of the recycle hydrogen stream with a hydrocarbons stream upstream of the cold combined feed exchanger to provide the feed stream for the dehydrogenation reactor.

7. The process of claim 6 , further comprising exchanging heat between the feed stream and the compressed hydrocarbon stream in the cold combined feed exchanger.

8. The process of claim 1 , wherein hydrogen to hydrocarbon ratio of the feed stream is in the range of 0.01 to 0.4.

9. A process for recovering hydrogen from dehydrogenation reactor effluent, the process comprising:
passing a feed stream comprising hydrocarbons and hydrogen to a dehydrogenation reactor maintained at dehydrogenation conditions to provide a dehydrogenation reactor effluent;
passing the dehydrogenation reactor effluent to a reactor effluent compressor to provide a compressed hydrocarbon stream;
passing the compressed hydrocarbon stream to a cold box separation unit to provide a liquid hydrocarbon product stream and a recycle hydrogen stream;
splitting the recycle hydrogen stream upstream of a cold combined feed exchanger located in the separation unit; and
mixing a return portion of the recycle hydrogen stream with the dehydrogenation reactor effluent to provide an enriched stream and passing the enriched stream to the reactor effluent compressor.

10. The process of claim 9 , wherein hydrogen to hydrocarbon ratio of the enriched stream is higher than hydrogen to hydrocarbon ratio of the dehydrogenation reactor effluent.

11. The process of claim 9 , further comprising splitting the recycle hydrogen stream into the return portion and a charge portion of the recycle hydrogen stream.

12. The process of claim 11 , further comprising mixing the charge portion of the recycle hydrogen stream with a hydrocarbons stream upstream of the cold combined feed exchanger to provide the feed stream for the dehydrogenation reactor.

13. The process of claim 9 , wherein hydrogen to hydrocarbon ratio of the feed stream is in the range of 0.01 to 0.4.

14. An apparatus for recovering hydrogen from dehydrogenation reactor effluent comprising:
a dehydrogenation reactor operating under dehydrogenation conditions configured to selectively dehydrogenate a feed stream comprising hydrocarbons and hydrogen and provide a dehydrogenation reactor effluent;
a reactor effluent compressor in fluid communication with the dehydrogenation reactor via the dehydrogenation reactor effluent and configured to compress the dehydrogenation reactor effluent to provide a compressed hydrocarbon stream;
a cold box separation unit comprising of a cold combined feed exchanger in fluid communication with the reactor effluent compressor via the compressed hydrocarbon stream and configured to provide a liquid hydrocarbon product stream and a recycle hydrogen stream;
a split is present upstream of the cold combined feed exchanger to divide the recycle hydrogen stream; and
the reactor effluent compressor is in fluid communication with the cold box separation unit via a return portion of the recycle hydrogen stream.

15. The apparatus of claim 14 , wherein the cold box separation unit comprises of a plurality of heat exchangers including the cold combined feed exchanger, and a plurality of separation vessels and expanders.

16. The apparatus of claim 15 , wherein the cold combined feed exchanger is in fluid communication with the reactor effluent compressor via the compressed hydrocarbon stream.

17. The apparatus of claim 15 , wherein the split is to divide the recycle hydrogen stream into the return portion and a charge portion.

18. The apparatus of claim 15 , wherein the reactor effluent compressor is in fluid communication with the cold combined feed exchanger via the return portion of the recycle hydrogen stream.

19. The apparatus of claim 15 , wherein the dehydrogenation reactor is in fluid communication with the cold combined feed exchanger via the feed stream obtained by mixing a hydrocarbons stream with the charge portion of the recycle hydrogen stream upstream of the cold combined feed exchanger.

Assignees

• Uop Llc

Inventors

• Kanyuh Adam J

Classifications

• C07C7/14808

  with non-metals as element (hydrogenation C07C7/163) · CPC title

• C01B3/506 Primary

  at low temperatures · CPC title

• C07C5/333 Primary

  Catalytic processes · CPC title

• C07C7/005

  Processes comprising at least two steps in series · CPC title

• C10G49/22 Primary

  Separation of effluents · CPC title