US4526112A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Heat exchanger method and apparatus
Assignee: Heat Exchanger Industries Inc
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Filing: 1984-11-14
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Granted: 1985-07-02
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Expires: 2004-11-14
Abstract
Abstract Exhaust gas treatment method and apparatus extract heat from an exhaust gas by operating in a water-condensing mode which allows more heat to be recovered, removes particulate matter and condensed acid from the exhaust gas, and washes heat exchange surfaces to keep them clean and wet to improve heat transfer. Systems for heating water, air, and both water and air are disclosed. Methods of constructing and assembling improved heat exchangers are disclosed.
Inventors
- 👤 Donald F. Warner
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 04:55
CPC Classifications
F; F28; F28D; F28D7/00; F28D7/08; F28D7/082; F28D7/085; B; B01; B01D; B01D53/00; B01D53/002; B01D53/34; B01D53/46; B01D53/48; B01D53/50; B01D53/507; F23; F23J; F23J15/00; F23J15/06; F28D21/00; F28D21/0001; F28D21/0003; F28D21/001; F28D7/16; F28D7/1615; F28D7/1623; F28F; F28F19/00; F28F19/02; F28F19/04; F28F9/00; F28F9/007; F28F9/013; F28F9/0131; Y; Y02; Y02E; Y02E20/00; Y02E20/30
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
234 words
The method of recovering heat energy from an exhaust gas by heating a fluid wherein said exhaust gas includes water vapor condensable at and below a water vapor condensation temperature and a corrosive constituent than said water vapor condensation temperature, said method comprising the steps of passing said exhaust gas successively through a first heat exchanger and a second heat exchanger, said second heat exchanger containing corrosion-protection material having a material limit operating temperature exceeding said corrosive condensation temperature, the flow rates and temperatures of said exhaust gas and said fluid being arranged so that passage of said exhaust gas through said first heat exchanger cools said exhaust gas from a first temperature to a second temperature which is below said material limit operating temperature but above said corrosive condensation temperature, passage of said exhaust gas through said second heat exchanger cools said exhaust gas from a temperature above said corrosive condensation temperature to a third temperature below said water vapor condensation temperature, and passage of said fluid through said second heat exchanger heats said fluid from a temperature below said water vapor condensation temperature to a fourth temperature which is above said corrosive condensation temperature but below said material limit operating temperature, whereby condensation of both water vapor and said corrosive constituent continuously occur within said second heat exchanger and neither water vapor nor said corrosive constituent condense within said first heat exchanger.
Claim 2
Independent Claim
234 words
The method of recovering heat energy from an exhaust gas by heating a fluid wherein said exhaust gas includes water vapor condensable at and below a water vapor condensation temperature and a corrosive constituent than said water vapor condensation temperature, said method comprising the steps of passing said exhaust gas successively through a first heat exchanger and a second heat exchanger, said second heat exchanger containing corrosion-protection material having a material limit operating temperature exceeding said corrosive condensation temperature, the flow rates and temperatures of said exhaust gas and said fluid being arranged so that passage of said exhaust gas through said first heat exchanger cools said exhaust gas from a first temperature to a second temperature which is below said material limit operating temperature but above said corrosive condensation temperature, passage of said exhaust gas through said second heat exchanger cools said exhaust gas from a temperature above said corrosive condensation temperature to a third temperature below said water vapor condensation temperature, and passage of said fluid through said second heat exchanger heats said fluid from a temperature below said water vapor condensation temperature to a fourth temperature which is above said corrosive condensation temperature but below said material limit operating temperature, whereby condensation of both water vapor and said corrosive constituent continuously occur within said second heat exchanger and neither water vapor nor said corrosive constituent condense within said first heat exchanger.
Claim 3
Dependent Claim
15 words
The method of claim 1 wherein said first temperature exceeds said material limit operating temperature.
Claim 4
Dependent Claim
29 words
The method of claim 1 wherein passage of said fluid through said first heat exchanger heats said fluid to a temperature which is above said material limit operating temperature.
Claim 5
Dependent Claim
53 words
The method of claim 1 wherein said fluid is air and which method includes the step of applying said exhaust gas to said first heat exchanger from a fuel-burning means which produces said exhaust gas, and the step of applying air heated by first heat exchanger as combustion air to said fuel-burning means.
Claim 6
Dependent Claim
40 words
The method of claim 1 wherein the step of passing said exhaust gas through said second heat exchanger comprises passing said exhaust gas in heat exchange relationship generally perpendicularly to and between generally horizontally extending tubes of a tube nest.
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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) | 1988-07-01 | 1988-12-31 | 1989-07-02 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1992-07-01 | 1992-12-31 | 1993-07-02 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1996-07-01 | 1996-12-31 | 1997-07-02 | $7700.00 | Window Closed / Lapsed |