US4333992A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method for producing steam from the liquid in a moist gas stream
Assignee: RTX Corp
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Filing: 1980-10-30
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Granted: 1982-06-08
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Expires: 2000-10-30
Abstract
Abstract To avoid using high quality heat to boil water condensed from a moist gas stream and to increase the overall thermal efficiency in a system requiring a supply of steam obtained by boiling water condensed from a moist gas stream, the condensing of the desired amount of water is done in a combined condenser/boiler wherein the condensed out water is separated from the gas stream, reduced in temperature, and throttled to a pressure wherein it is converted to steam back in the condenser/boiler using only the heat of condensation and sensible heat from the moist gas stream during the condensing step.
Inventors
- 👤 Herbert C. Healy
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-25 08:43
CPC Classifications
B; B01; B01D; B01D1/00; B01D5/00; B01D5/0033; B01D5/0054; B01D53/00; B01D53/26; B01D53/265; H; H01; H01M; H01M8/00; H01M8/06; H01M8/0606; H01M8/0612; Y; Y02; Y02E; Y02E60/00; Y02E60/30; Y02E60/50
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
327 words
In a power producing plant comprising primary electricity generating means and cogeneration means, wherein said primary electricity generating means produces a moist gas stream containing high quality waste heat at a first pressure and first temperature which is well above the dew point of said stream, and wherein said cogeneration means derives at least part of its energy from high quality waste heat from said primary electricity generating means, and wherein said power plant requires a supply of steam, a method for removing water from said moist gas stream and converting said water to said steam required by said power plant comprising the steps of: reducing the temperature of said moist gas stream to a second temperature which is still above the dew point of said stream by using the said high quality heat within said moist gas stream to provide energy for said cogeneration means; introducing said moist gas stream at said second temperature into a condenser/boiler; condensing water from the gas stream in the condenser/boiler by cooling the gas stream to a third temperature which is below the stream's dew point without significantly reducing the pressure of the gas stream to produce liquid water at said third temperature and at a pressure which is substantially the same as the pressure of the moist gas stream entering the condenser/boiler; separating the condensed liquid water from the gas stream; reducing the temperature of the condensed liquid water from said third temperature to a lower, fourth temperature; reducing the pressure of the condensed liquid water to a second pressure such that the boiling temperature of the water is equal to or lower than said third temperature; and vaporizing the reduced pressure and reduced temperature separated liquid water in said condenser/boiler by heating said liquid at said second pressure using only the heat of condensation from the step of condensing and sensible heat from the moist gas stream passing through said condenser/boiler to produce steam at said second pressure.
Claim 2
Dependent Claim
327 words
In a power producing plant comprising primary electricity generating means and cogeneration means, wherein said primary electricity generating means produces a moist gas stream containing high quality waste heat at a first pressure and first temperature which is well above the dew point of said stream, and wherein said cogeneration means derives at least part of its energy from high quality waste heat from said primary electricity generating means, and wherein said power plant requires a supply of steam, a method for removing water from said moist gas stream and converting said water to said steam required by said power plant comprising the steps of: reducing the temperature of said moist gas stream to a second temperature which is still above the dew point of said stream by using the said high quality heat within said moist gas stream to provide energy for said cogeneration means; introducing said moist gas stream at said second temperature into a condenser/boiler; condensing water from the gas stream in the condenser/boiler by cooling the gas stream to a third temperature which is below the stream's dew point without significantly reducing the pressure of the gas stream to produce liquid water at said third temperature and at a pressure which is substantially the same as the pressure of the moist gas stream entering the condenser/boiler; separating the condensed liquid water from the gas stream; reducing the temperature of the condensed liquid water from said third temperature to a lower, fourth temperature; reducing the pressure of the condensed liquid water to a second pressure such that the boiling temperature of the water is equal to or lower than said third temperature; and vaporizing the reduced pressure and reduced temperature separated liquid water in said condenser/boiler by heating said liquid at said second pressure using only the heat of condensation from the step of condensing and sensible heat from the moist gas stream passing through said condenser/boiler to produce steam at said second pressure.
Claim 3
Dependent Claim
24 words
The method according to claim 1 wherein essentially all the moisture in said moist gas stream is condensed to a liquid in said condenser/boiler.
Claim 4
Dependent Claim
21 words
The method according to claim 2 wherein said second temperature is just above the dew point of said moist gas stream.
Claim 5
Dependent Claim
48 words
The method according to claim 3 wherein said step of separating produces a substantially dry gas stream, and some of the high quality heat in said moist gas stream, prior to its being introduced into said condenser/boiler, is used to increase the temperature of said dry gas stream.
Claim 6
Dependent Claim
16 words
The method according to claim 2 wherein the steam produced in the condenser/boiler is superheated steam.
Claim 7
Dependent Claim
143 words
The method according to claim 1, 2, 3, 4 or 5 wherein said primary electricity generating means is a pressurized fuel cell power plant including a plurality of fuel cells and a fuel reactor requiring pressurized steam for the conversion of hydrocarbons to pressurized hydrogen fuel used in the fuel cells, said fuel cells having fuel gas spaces and oxidant gas spaces, and said moist gas stream is the exhaust gas stream from said fuel gas spaces, and said method includes the additional steps of: compressing the oxidant for said fuel cells in a first compressor driven by energy in the exhaust gas stream from said oxidant gas spaces; compressing said steam produced in said vaporizing step in a second compressor driven by energy in the exhaust gas stream from said oxidant gas spaces; and delivering said compressed steam into said fuel reactor.
Claim 8
Dependent Claim
31 words
The method according to claim 6 wherein said fuel cells utilize molten carbonate electrolyte, including the step of circulating said dry gas stream through the oxidant gas spaces of said cells.
References Cited (Backward Citations)
US4001041A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1985-06-07 | 1985-12-07 | 1986-06-08 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1989-06-07 | 1989-12-07 | 1990-06-08 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1993-06-07 | 1993-12-07 | 1994-06-08 | $7700.00 | Window Closed / Lapsed |