Process for producing a hydrogen-rich gas stream from the effluent of a catalytic hydrocarbon conversion reaction zone

• US 4,482,369 A
• Filed: 05/10/1983
• Issued: 11/13/1984
• Est. Priority Date: 05/10/1983
• Status: Expired due to Fees

• Current Assignee: UOP Des Plaines IL A NY General Partnership
• Original Assignee: UOP Llc (Honeywell International Inc.)
• Inventors: James, Robert B. Jr., Carson, Don B.
• Primary Examiner(s): Sever, Frank
• Application Number:
  US06/493,180
• Time in Patent Office: 553 Days
• Field of Search: 62/38, 62/39, 62/9, 62/11, 62/18, 62/23, 62/17
• US Class Current: 62/619
• CPC Class Codes: C10G 49/22 Separation of effluents
• CPC Class Codes: Y10S 62/931 Recovery of hydrogen

Abstract

A process for the production of a hydrogen-rich gas stream from the effluent of a catalytic hydrocarbon conversion reaction zone is disclosed. A hydrogen-containing vapor phase is recovered from the effluent and subjected to cooling in order to produce a hydrogen-rich gas stream. The resulting hydrogen-rich gas stream is expanded to provide the medium used in cooling the hydrogen-containing vapor phase.

Claims

1. A process to provide a purified hydrogen-rich gas stream and to maximize recovery of C₃⁺ hydrocarbons from a catalytic hydrocarbon conversion reaction effluent containing hydrogen and hydrocarbons by treating said effluent from a catalytic hydrocarbon conversion reaction zone comprising the steps of:

(a) passing said catalytic hydrocarbon conversion reaction effluent containing hydrogen and hydrocarbons to a first vapor-liquid equilibrium zone, recovering therefrom a hydrogen-containing vapor phase and recycling a first portion thereof to said hydrocarbon conversion reaction zone;

(b) drying at least a second portion of the hydrogen-containing vapor phase by removing water therefrom and thereafter cooling the dried portion by indirect heat exchange with a hereinafter defined hydrogen-rich gas stream;

(c) passing the dried, cooled portion of the hydrogen-containing vapor phase to a second vapor-liquid equilibrium separation zone to produce a liquid stream comprising C₃⁺ light hydrocarbons, which are recovered from said process, and a purified hydrogen-rich gas stream;

(d) expanding at least a portion of said purified hydrogen-rich gas stream and thereafter subjecting it to indirect heat exchange with the dried portion of the hydrogen-containing vapor phase pursuant to step (b) above; and

,

(e) recovering said heat exchanged purified hydrogen-rich gas stream.

2. The process of claim 1 wherein the expansion of said portion of the hydrogen-rich gas stream is effecied by use of a turboexpander means.

3. The process of claim 2 wherein the turboexpander means is connected to a shaft for the production of shaft power.

4. The process of claim 3 wherein the shaft is connected to electrical power generation means and the shaft power is utilized for the production of electrical power.

5. The process of claim 4 wherein at least a portion of the electrical power produced is passed to a power grid system.

6. The process of claim 4 wherein at least a portion of the electrical power produced is utilized to drive a compressor means for the compression of a second portion of the first hydrogen-containing vapor phase.

7. The process of claim 3 wherein at least a portion of the shaft power produced is utilized to drive a compressor means for the recycling of said first portion of the hydrogen-containing vapor phase.

8. The process of claim 1 further characterized in that the catalytic hydrocarbon conversion reaction zone is a catalytic reforming reaction zone.

9. The process of claim 1 further characterized in that the catalytic hydrocarbon conversion reaction zone is a dehydrogenation reaction zone.

10. A process to produce a purified hydrogen rich gas stream and to maximize recovery of C₃⁺ hydrocarbons from a catalytic hydrocarbon reforming effluent containing hydrogen and hydrocarbons by treating said effluent from a catalyst reforming reaction zone comprising the steps of:

(a) passing said effluent to a first vapor-liquid equilibrium zone and recovering therefrom a hydrogen-containing vapor phase;

(b) subjecting a first portion of the hydrogen-containing vapor phase to compression and recycling at least part of the compressed first portion to the catalytic reforming reaction zone;

(c) drying a second portion of the hydrogen-containing vapor phase by removing water therefrom and thereafter cooling the dried portion by indirect heat exchange with a hereinafter defined purified hydrogen-rich gas stream;

(d) passing the dried, cooled portion of the hydrogen-containing vapor phase to a second vapor-liquid equilibrium separation zone to produce a liquid stream comprising C₃⁺ light hydrocarbons, which are recovered from said process, and a purified hydrogen-rich gas stream;

(e) subjecting at least a portion of said purified hydrogen-rich gas stream to an expansion and thereafter subjecting it to indirect heat exchange with the dried second portion of the hydrogen-containing vapor phase pursuant to step (c) above, and effecting the compression in step (b) above at least in part with energy resulting from said expansion of a portion of said purified hydrogen-rich gas stream; and

,

(f) recovering said heat exchanged purified hydrogen-rich gas stream.