IP Library Granted Patent US 9,457,313
Granted Patent B2
US 9,457,313 · App. 13/548,827 · Granted Oct 4, 2016

Membrane technology for use in a power generation process

Inventors: Richard W. Baker (Palo Alto, CA); Timothy C. Merkel (Menlo Park, CA); Johannes G. Wijmans (Menlo Park, CA)
Assignee: Membrane Technology and Research, Inc.
B01D53/22B01D53/62F02C3/34F23C9/00B01D2256/22B01D2257/102B01D2257/104B01D2257/504B01D2258/0283F23L2900/07001Y02C10/04Y02C10/10Y02E20/16Y02E20/322
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Quick Facts
Patent No.
US 9,457,313
App. No.
13/548,827
Granted
Oct 4, 2016
Kind
B2
Abstract

Disclosed herein is a power generation process in which a portion of the carbon dioxide generated by gaseous fuel combustion is recycled back to the power generation process, either pre-combustion, post-combustion, or both. The power generation process of the invention may be a combined cycle process or a traditional power generation process. The process utilizes sweep-based membrane separation.

Claims (18)

1. A process for controlling carbon dioxide exhaust from combustion of a gaseous fuel, comprising:

(a) performing a combustion step by combusting a mixture comprising a gaseous fuel and an oxygen-containing gas in a combustor, thereby generating a combustor exhaust stream comprising carbon dioxide and nitrogen;

(b) routing the combustor exhaust stream as at least a portion of a working gas stream to a gas turbine, thereby generating electrical power and creating a turbine exhaust stream;

(c) providing a first membrane having a first feed side and a first permeate side, and being selectively permeable to carbon dioxide over nitrogen and to carbon dioxide over oxygen;

(d) passing at least a portion of the turbine exhaust stream across the first feed side;

(e) withdrawing from the first permeate side a partially concentrated carbon dioxide first permeate stream;

(f) withdrawing from the first feed side a carbon dioxide-depleted first residue stream;

(g) providing a second membrane having a second feed side and a second permeate side, and being selectively permeable to carbon dioxide over nitrogen and to carbon dioxide over oxygen;

(h) passing the first residue stream across the second feed side;

(i) passing air, oxygen-enriched air, or oxygen as a sweep stream across the second permeate side;

(j) withdrawing from the second feed side a second residue stream that is depleted in carbon dioxide compared to the first residue stream;

(k) withdrawing from the second permeate side a second permeate stream comprising oxygen and carbon dioxide; and

(l) passing at least a portion of the second permeate stream to a location between the combustor and the gas turbine as part of the working gas stream.

2. The process of claim 1 , wherein the oxygen-containing gas comprises at least 15 volume % oxygen.

3. The process of claim 1 , wherein the combustor exhaust stream comprises at least 2 volume % oxygen.

4. The process of claim 1 , wherein the process recovers at least 80 volume % of the carbon dioxide generated by the combustion step into the partially concentrated carbon dioxide first permeate stream.

5. The process of claim 1 , wherein the partially concentrated carbon dioxide first permeate stream contains at least 20 volume % carbon dioxide.

6. The process of claim 1 , wherein the first membrane and the second membrane exhibit a selectivity for carbon dioxide over oxygen of at least 10.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 5, 2014
From: WIJMANS, JOHANNES G; MERKEL, TIMOTHY C.; BAKER, RICHARD W.
To: MEMBRANE TECHNOLOGY AND RESEARCH, INC.
Reel/Frame 033042/0115 →
Continuity (3)
Continuation In Part 13115726 · May 25, 2011
Continuation In Part 13122136
Related Publication 20120272657A1 · Nov 1, 2012