US4781241A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Heat exchanger for fuel cell power plant reformer
Assignee: UTC Power Corp
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Filing: 1987-08-27
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Granted: 1988-11-01
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Expires: 2007-08-27
Abstract
Abstract A heat exchanger uses the heat from processed fuel gas from a reformer for a fuel cell to superheat steam, to preheat raw fuel prior to entering the reformer and to heat a water-steam coolant mixture from the fuel cells. The processed fuel gas temperature is thus lowered to a level useful in the fuel cell reaction. The four temperature adjustments are accomplished in a single heat exchanger with only three heat transfer cores. The heat exchanger is preheated by circulating coolant and purge steam from the power section during startup of the latter.
Inventors
- 👤 Robert Misage
- 👤 Glenn W. Scheffler
- 👤 Herbert J. Setzer
- 👤 Paul R. Margiott
- 👤 Edmund K. Parenti, Jr.
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-25 06:03
CPC Classifications
F; F28; F28D; F28D7/00; F28D7/0066; F28D7/0083; F22; F22B; F22B33/00; F22B33/18; F28D7/08; F28D7/082; F28D7/085; H; H01; H01M; H01M8/00; H01M8/04; H01M8/04007; H01M8/04029; H01M8/06; H01M8/0606; H01M8/0612; Y; Y02; Y02E; Y02E60/00; Y02E60/30; Y02E60/50
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
225 words
A method of operating a heat exchanger in a fuel cell power plant, said method comprising the steps of: (a) providing a single heat exchanger housing having an inlet end, and outlet end and a medial portion between said inlet and outlet ends; (b) flowing reformed fuel from a reformer through said housing from said inlet end to said outlet end; (c) flowing raw hydrocarbon fuel through said housing from said outlet end to said inlet end in heat exchange relationship with said reformed fuel; (d) flowing coolant water from a power section of the power plant through said housing from said outlet end to said medial portion in heat exchange relationship with said reformed fuel; (e) flowing steam from the power plant through said housing from said medial portion to said inlet end in heat exchange relationship with said reformed fuel; and (f) said reformed fuel entering said inlet end at reformer temperatures and exiting said outlet end at power plant power section temperatures, said raw hydrocarbon fuel entering said outlet end at near ambient temperatures and exiting said inlet end at reformer temperatures, said coolant water entering said outlet end at power section temperatures and exiting said medial portion as two phase water-steam mixture, and said steam entering said medial portion at steam separator temperatures and exiting said inlet end at reformer temperatures.
Claim 2
Independent Claim
225 words
A method of operating a heat exchanger in a fuel cell power plant, said method comprising the steps of: (a) providing a single heat exchanger housing having an inlet end, and outlet end and a medial portion between said inlet and outlet ends; (b) flowing reformed fuel from a reformer through said housing from said inlet end to said outlet end; (c) flowing raw hydrocarbon fuel through said housing from said outlet end to said inlet end in heat exchange relationship with said reformed fuel; (d) flowing coolant water from a power section of the power plant through said housing from said outlet end to said medial portion in heat exchange relationship with said reformed fuel; (e) flowing steam from the power plant through said housing from said medial portion to said inlet end in heat exchange relationship with said reformed fuel; and (f) said reformed fuel entering said inlet end at reformer temperatures and exiting said outlet end at power plant power section temperatures, said raw hydrocarbon fuel entering said outlet end at near ambient temperatures and exiting said inlet end at reformer temperatures, said coolant water entering said outlet end at power section temperatures and exiting said medial portion as two phase water-steam mixture, and said steam entering said medial portion at steam separator temperatures and exiting said inlet end at reformer temperatures.
Claim 3
Dependent Claim
28 words
The method of claim 1 further including the preliminary steps of preheating said housing with coolant water and purging steam during startup of the power plant power section.
Claim 4
Dependent Claim
34 words
The method of claim 2 wherein said preheating steps are operable to elevate the temperature in said housing sufficiently to evaporate any moisture left therein from a prior operating cycle of the power plant.
Claim 5
Dependent Claim
419 words
A heat exchanger assembly for use in controlling fluid temperatures in a fuel cell power plant, said heat exchanger assembly comprising: (a) a single housing; (b) means forming an inlet in said housing for recirculating hot reformed gases from a fuel reformer in the power plant in an inlet side of said housing; (c) means forming an outlet in said housing for exiting the reformed fuel gases from an outlet side of said housing; (d) means forming a flow path in said housing for the reformed fuel gases from said inlet side to said outlet side along which flow path the reformed fuel gases move through said housing; (e) first conduit means in said housing extending from said outlet side to said inlet side of said housing, said first conduit means being operable to direct raw hydrocarbon fuel through said housing from said outlet side to said inlet side in heat exchange relationship with the reformed fuel gases, and said first conduit means including means for exiting the raw hydrocarbon fuel from said housing at said inlet side thereof; (f) second conduit means in said housing extending between said outlet side of said housing to a medial portion of said housing between said outlet and inlet sides thereof, said second conduit means being operable to duct coolant water from the power plant power section through said housing from said outlet side thereof to said medial portion thereof in heat exchange relationship with the reformed fuel gases, said second conduit means including means for exiting the coolant water from said housing at said medial portion thereof; and (g) third conduit means in said housing extending from said medial portion of said housing to said inlet side of said housing, said third conduit means being operable to duct steam from said medial portion of said housing to said inlet side thereof in heat exchange relationship with the reformed fuel gases, and said third conduit means further including means for exiting the steam from said housing at said inlet side thereof; and (h) said heat exchanger assembly being operable to lower the temperature of the reformed fuel gases from reformer temperatures to fuel cell power section operating temperatures, to raise the temperature of the raw hydrocarbon fuel to reformer temperatures, to raise the temperature of the coolant water sufficiently to convert the coolant water to a two phase water-steam mixture, and to raise the temperature of the steam to reformer temperatures with all of the temperature changes occurring within said single housing.
Claim 6
Dependent Claim
419 words
A heat exchanger assembly for use in controlling fluid temperatures in a fuel cell power plant, said heat exchanger assembly comprising: (a) a single housing; (b) means forming an inlet in said housing for recirculating hot reformed gases from a fuel reformer in the power plant in an inlet side of said housing; (c) means forming an outlet in said housing for exiting the reformed fuel gases from an outlet side of said housing; (d) means forming a flow path in said housing for the reformed fuel gases from said inlet side to said outlet side along which flow path the reformed fuel gases move through said housing; (e) first conduit means in said housing extending from said outlet side to said inlet side of said housing, said first conduit means being operable to direct raw hydrocarbon fuel through said housing from said outlet side to said inlet side in heat exchange relationship with the reformed fuel gases, and said first conduit means including means for exiting the raw hydrocarbon fuel from said housing at said inlet side thereof; (f) second conduit means in said housing extending between said outlet side of said housing to a medial portion of said housing between said outlet and inlet sides thereof, said second conduit means being operable to duct coolant water from the power plant power section through said housing from said outlet side thereof to said medial portion thereof in heat exchange relationship with the reformed fuel gases, said second conduit means including means for exiting the coolant water from said housing at said medial portion thereof; and (g) third conduit means in said housing extending from said medial portion of said housing to said inlet side of said housing, said third conduit means being operable to duct steam from said medial portion of said housing to said inlet side thereof in heat exchange relationship with the reformed fuel gases, and said third conduit means further including means for exiting the steam from said housing at said inlet side thereof; and (h) said heat exchanger assembly being operable to lower the temperature of the reformed fuel gases from reformer temperatures to fuel cell power section operating temperatures, to raise the temperature of the raw hydrocarbon fuel to reformer temperatures, to raise the temperature of the coolant water sufficiently to convert the coolant water to a two phase water-steam mixture, and to raise the temperature of the steam to reformer temperatures with all of the temperature changes occurring within said single housing.
Claim 7
Dependent Claim
29 words
The heat exchanger assembly of claim 4 further including heat exchange fin plates disposed in said flow path and interconnecting all of said first, second and third conduit means.
Claim 8
Dependent Claim
78 words
The heat exchanger assembly of claim 4 further comprising: a manifold and flow reversal chamber in said housing on one side of said flow path, which manifold and flow reversal chamber contains inlet and outlet manifolds and first flow reversal portions for said first, second and third conduit means; and a flow reversal chamber on the opposite side of said flow path in said housing containing second flow reversal portions of said first, second and third conduit means.
Claim 9
Dependent Claim
57 words
The heat exchanger assembly of claim 6 wherein said first and second flow reversal portions of said third conduit means comprise U-shaped portions of said third conduit means, said first flow reversal portions of said third conduit means being disposed in planes which are perpendicular to the planes in which said second flow reversal portions are disposed.
References Cited (Backward Citations)
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1991-11-01 | 1992-05-02 | 1992-11-01 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1995-11-01 | 1996-05-02 | 1996-11-01 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1999-11-01 | 2000-05-02 | 2000-11-01 | $7700.00 | Window Closed / Lapsed |