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US5146755A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for reducing flue gas acid vapor emissions and energy recovery

Assignee: Individual
•
Filing: 1991-01-25
•
Granted: 1992-09-15
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Expires: 2011-01-25
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Abstract

Abstract Acidic vapors from hot flue gases are condensed and collected. The waste heat therefrom is recovered and used to produce additional electrical power.

Inventors

  • 👤 Fawzy T. Abdelmalek

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 08:47
CPC Classifications
F; F28; F28D; F28D15/00; F28D15/02; F28D15/0266; B; B01; B01D; B01D53/00; B01D53/002; B01D53/24; B01D53/32; B03; B03C; B03C3/00; B03C3/019; C; C01; C01B; C01B17/00; C01B17/48; C01B17/50; C01B17/60; F23; F23J; F23J15/00; F23J15/006; F25; F25B; F25B11/00; F25B11/02; F25B11/04; F23J2215/00; F23J2215/20; F23J2217/00; F23J2217/10; F23J2217/102; F23J2219/00; F23J2219/70; F25B2400/00; F25B2400/14; F25B2400/141; Y; Y02; Y02E; Y02E20/00; Y02E20/32; Y02P; Y02P20/00; Y02P20/10; Y02P20/129

Claims Analysis

Total Claims: 3
Claim 1
Independent Claim 209 words
In combination, an electric power plant having a continuous emission of boiler flue gases; a conduit for conducting the flue gas emissions; a heat exchange system for absorbing heat from the flue gas to allow for flue gas condensation and collection, and for supplying that absorbed heat to a flow of liquid refrigerant to vaporize and superheat the refrigerant; an expander through which the superheated refrigerant gas expands at lower pressure and lower saturation temperature, and drives an impeller for the generation of power; a condenser for further cooling and condensing the saturated refrigerant gas at constant pressure; a refrigerant pump for pressurizing and recycling the refrigerant back through the heat exchange system from the condenser; a second refrigerant pump through which flows a portion of the refrigerant condensate under pressure from the condenser; a steam condenser through which flows that portion of the refrigerant condensate from said second refrigerant pump to the expander; and a steam turbine which sends high pressure steam exhaust to the steam condenser; wherein heat from the steam exhaust is exchanged at the steam condenser, vaporizing that portion of the refrigerant condensate flowing therethrough and allowing said refrigerant to be recycled to the expander in gaseous form under pressure from said second refrigerant pump.
Claim 2
Dependent Claim 209 words
In combination, an electric power plant having a continuous emission of boiler flue gases; a conduit for conducting the flue gas emissions; a heat exchange system for absorbing heat from the flue gas to allow for flue gas condensation and collection, and for supplying that absorbed heat to a flow of liquid refrigerant to vaporize and superheat the refrigerant; an expander through which the superheated refrigerant gas expands at lower pressure and lower saturation temperature, and drives an impeller for the generation of power; a condenser for further cooling and condensing the saturated refrigerant gas at constant pressure; a refrigerant pump for pressurizing and recycling the refrigerant back through the heat exchange system from the condenser; a second refrigerant pump through which flows a portion of the refrigerant condensate under pressure from the condenser; a steam condenser through which flows that portion of the refrigerant condensate from said second refrigerant pump to the expander; and a steam turbine which sends high pressure steam exhaust to the steam condenser; wherein heat from the steam exhaust is exchanged at the steam condenser, vaporizing that portion of the refrigerant condensate flowing therethrough and allowing said refrigerant to be recycled to the expander in gaseous form under pressure from said second refrigerant pump.
Claim 3
Dependent Claim 26 words
The combination of claim 1, wherein a liquid chiller or direct expansion means is connected downstream from the refrigerant pump but before the heat exchange system.

References Cited (Backward Citations)

US4126000A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1995-09-15 1996-03-16 1996-09-15 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1999-09-15 2000-03-16 2000-09-15 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2003-09-15 2004-03-16 2004-09-15 $7700.00 Window Closed / Lapsed

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