Membrane-assisted process to produce ammonia

• US 5,455,016 A
• Filed: 08/31/1994
• Issued: 10/03/1995
• Est. Priority Date: 08/31/1994
• Status: Expired due to Fees

• Current Assignee: Air Products and Chemicals Incorporated (Linde Plc)
• Original Assignee: Air Products and Chemicals Incorporated (Linde Plc)
• Inventors: Kellogg, Lyndon J. Jr., Choe, Jun S.
• Primary Examiner(s): LANGEL, WAYNE A
• Application Number:
  US08/299,184
• Time in Patent Office: 398 Days
• Field of Search: 427/359, 95/47
• US Class Current: 423/359
• CPC Class Codes: C01C 1/0405 from N2 and H2 in presence of a catalyst
• CPC Class Codes: C01C 1/0476 Purge gas treatment, e.g. for removal of inert gases or recovery of H2
• CPC Class Codes: Y02P 20/129 Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
• CPC Class Codes: Y02P 20/52 using catalysts, e.g. selective catalysts

Abstract

A membrane-assisted process to produce ammonia is set forth wherein the recycle stream from the ammonia process containing primarily unreacted hydrogen and nitrogen but also containing inerts and unrecovered ammonia is separated in a first ammonia-selective membrane separator into a permeate stream enriched in ammonia and a non-permeate stream enriched in hydrogen, nitrogen and the inerts which is recycled to the reactor feed. A key to the present invention is that the permeate stream enriched in ammonia is recycled to the reactor effluent.

In one embodiment of the present invention, the purge stream from the ammonia process (which represents that portion of the recycle stream which must removed from the process in order to prevent the build-up of the inerts in the process) is separated in a second ammonia-selective membrane separator into a permeate stream enriched in ammonia which is recycled to the reactor feed and a non-permeate stream enriched in hydrogen, nitrogen and the inerts which can be further processed for hydrogen recovery. A key to this embodiment is that a portion of the reactor feed is used to sweep the permeate side of the second membrane separator.

Claims

1. A membrane-assisted process to produce ammonia comprising:

(a) introducing a feed stream comprising hydrogen and nitrogen into a reactor in order to synthesize ammonia;

(b) withdrawing from the reactor a reactor effluent comprising ammonia, unreacted hydrogen, unreacted nitrogen and inerts comprising methane and argon;

(c) introducing the reactor effluent into a separation system wherein the reactor effluent is separated into a plurality of streams comprising;

(i) a product stream enriched in ammonia;

(ii) a gaseous recycle stream enriched in hydrogen, nitrogen and the inerts; and

(iii) a gaseous purge stream enriched in hydrogen, nitrogen and the inerts;

(d) introducing at least a portion of the gaseous recycle stream into a first membrane separator comprising a high pressure side separated from a low pressure side by a semi-permeable membrane which is selective for the permeation of ammonia wherein;

(i) the gaseous recycle stream is more specifically introduced into the high pressure side of the first membrane separator;

(ii) a non-permeate recycle stream further enriched in hydrogen and nitrogen is withdrawn from the high pressure side of the first membrane separator and subsequently recycled to the feed stream in step (a); and

(iii) a permeate recycle stream enriched in ammonia is withdrawn from the low pressure side of the first membrane separator as a crude ammonia product;

(e) recycling at least a portion of the crude ammonia product to reactor effluent in step (b);

(f) introducing at least a portion of the gaseous purge stream into a second membrane separator comprising a high pressure side separated from a low pressure side by a semi-permeable membrane which is selective for the permeation of ammonia wherein;

(i) the gaseous purge stream is more specifically introduced into the high pressure side of the second membrane separator;

(ii) a portion of the feed stream from step (a) is introduced into the low pressure side of the second membrane separator as a sweep stream;

(iii) a non-permeate purge stream further enriched in the inerts is withdrawn from the high pressure side of the second membrane separator; and

(iv) a permeate purge stream is withdrawn from the low pressure side of the second membrane separator and recycled to the reactor feed in step (a).

2. The process of claim 1 wherein the non-permeate purge stream withdrawn in step (f)(iii) is processed for hydrogen recovery.