Controlled CO preferential oxidation

• US 5,637,415 A
• Filed: 08/30/1996
• Issued: 06/10/1997
• Est. Priority Date: 08/30/1996
• Status: Expired due to Fees

• Current Assignee: General Motors Corporation (General Motors Company)
• Original Assignee: General Motors Corporation (General Motors Company)
• Inventors: Hoch, Martin M., Meltser, Mark A.
• Primary Examiner(s): Skapars, Anthony
• Application Number:
  US08/706,315
• Time in Patent Office: 284 Days
• Field of Search: 429/12, 429/13, 429/17, 429/19, 423/246, 423/247, 423/248, 422/168, 422/177
• US Class Current: 429/412
• CPC Class Codes: H01M 8/0662 Treatment of gaseous reactants or gaseous residues, e.g. cleaning
• CPC Class Codes: Y02E 60/50 Fuel cells

Abstract

Method for controlling the supply of air to a PROX reactor for the preferential oxidation in the presence of hydrogen wherein the concentration of the hydrogen entering and exiting the PROX reactor is monitored, the difference therebetween correlated to the amount of air needed to minimize such difference, and based thereon the air supply to the PROX reactor adjusted to provide such amount and minimize such difference.

Claims

1. In a method of operating a H₂ --O₂ fuel cell system comprising the principle steps of (1) providing a hydrogen-rich fuel gas having a first carbon monoxide, CO, content sufficient to poison the fuel cell'"'"'s anode, and (2) subjecting said fuel gas to a preferential oxidation reaction for selectively oxidizing said CO with O₂ in the presence of said hydrogen to produce a feed stream for said fuel cell which has a second carbon monoxide content less than said first content, the improvement comprising controlling the flow rate of said O₂ to said preferential oxidation reaction so as to optimize the consumption of said carbon monoxide from said fuel gas while minimizing the consumption of H₂ therefrom by:

a. measuring the H₂ content of said fuel gas;

b. measuring the H₂ content of said feed stream;

c. determining a first actual difference, Δ

H₂^a, between the H₂ contents of said feed stream and said fuel gas;

d. determining a second control difference, Δ

H₂^c, between said first actual difference, Δ

H₂^a, and a third reference difference, Δ

H₂^r, which reference difference corresponds to an ideal difference between the H₂ contents of said feed stream and said fuel gas;

e. from said second control difference, Δ

H₂^c, determining the ideal oxygen flow rate, O₂ⁱ, needed for said preferential oxidation reaction to achieve said reference difference Δ

H₂^r ;

f. determining a fourth difference, Δ

H₂, between the actual oxygen flow rate (O₂^a) to the preferential oxidation reaction and said ideal oxygen flow rate O₂ⁱ to such reaction;

g. generating an output signal representative of the fourth difference Δ

O₂ ; and

h. modulating the flow rate of the O₂ to said preferential oxidation reaction in response to said output signal to achieve said ideal oxygen flow rate O₂ⁱ.

2. The process according to claim 1 wherein said preferential oxidation reaction is conducted substantially isothermally on a catalyst maintained at a substantially constant temperature.