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US3839849A Expired / Lapsed US ⏱️ 0.0 years remaining

Wet type desulfurization system for flue gas

Assignee: Individual
•
Filing: 1972-08-16
•
Granted: 1974-10-08
•
Expires: 1992-08-16
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Abstract

Abstract An improved apparatus of a wet type for desulfurization of flue gas is provided which purges sulfureous pollutants from the flue gas, wherein an absorption process of the flue gas in a purifying liquid at a low temperature and the subsequent heating process of the purified gas to allow it to diffuse into the atmosphere effectively are carried into effect by utilizing the heat energy of the flue gas.

Inventors

  • 👤 G Maniya

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 07:26
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/14; B01D53/1456

Claims Analysis

Total Claims: 4
Claim 1
Independent Claim 306 words
A wet type desulfurization system for a stream of flue gas involving sulfurous gases, comprising a plurality of serially interconnected heat exchangers; means for passing the flue gas through said heat exchangers, whereby the temperature of said flue gas is successively reduced to about 70* C; a cooling tower means receiving said temperature reduced flue gas from the last of the serially interconnected heat exchangers for further cooling said flue gas to a temperature of about 30* C, whereby the gas is pre-desulphurized; an absorbing tower connected to the cooling tower and receiving the flue gas at the temperature of about 30* C; a refrigerated purifying liquid introduced into said absorbing tower in direct contact with said flue gas, thereby purifying the flue gas and reducing the temperature thereof to about 10* C; a heater in the path of the purified gas from the absorption tower for raising the temperature of the purified flue gases whereby the heated purified gases may diffuse into the atmosphere; a first absorption refrigerator comprising a first condenser, a first evaporator and a first absorber and a first regenerator; a heat pump absorption refrigerator comprising a second condenser, a second evaporator and a second absorber and a second generator; means for conducting heat from at least one of the heat exchangers to the first regenerator, whereby the first evaporator is cooled; means for conducting said purifying liquid through said first evaporator for refrigerating said purifying liquid to a temperature of about 0* C; means for conducting the heat from at least one of said heat exchangers to said second regenerator whereby said second evaporator is cooled, a coolant liquid circulated between the second evaporator and at least one of the heat exchangers for removing heat from said heat exchanger; and means for conducting heat from the second absorber to said heater.
Claim 2
Dependent Claim 306 words
A wet type desulfurization system for a stream of flue gas involving sulfurous gases, comprising a plurality of serially interconnected heat exchangers; means for passing the flue gas through said heat exchangers, whereby the temperature of said flue gas is successively reduced to about 70* C; a cooling tower means receiving said temperature reduced flue gas from the last of the serially interconnected heat exchangers for further cooling said flue gas to a temperature of about 30* C, whereby the gas is pre-desulphurized; an absorbing tower connected to the cooling tower and receiving the flue gas at the temperature of about 30* C; a refrigerated purifying liquid introduced into said absorbing tower in direct contact with said flue gas, thereby purifying the flue gas and reducing the temperature thereof to about 10* C; a heater in the path of the purified gas from the absorption tower for raising the temperature of the purified flue gases whereby the heated purified gases may diffuse into the atmosphere; a first absorption refrigerator comprising a first condenser, a first evaporator and a first absorber and a first regenerator; a heat pump absorption refrigerator comprising a second condenser, a second evaporator and a second absorber and a second generator; means for conducting heat from at least one of the heat exchangers to the first regenerator, whereby the first evaporator is cooled; means for conducting said purifying liquid through said first evaporator for refrigerating said purifying liquid to a temperature of about 0* C; means for conducting the heat from at least one of said heat exchangers to said second regenerator whereby said second evaporator is cooled, a coolant liquid circulated between the second evaporator and at least one of the heat exchangers for removing heat from said heat exchanger; and means for conducting heat from the second absorber to said heater.
Claim 3
Dependent Claim 58 words
A system as recited in claim 1 wherein the refrigerant in the first absorption refrigerator comprises an aqueous solution of ammonia; wherein the refrigerant in said heat pump absorption refrigerator comprises an aqueous solution of lithium bromide; and further comprising a blower connected between said absorbing tower and said heater for conducting said purified gas to said heater.
Claim 4
Dependent Claim 47 words
A system as recited in claim 1, further comprising a refrigerant turbine; means connected to at least one of said heat exchangers for conducting the heat from said heat exchanger to drive said turbine; a third refrigerator driven by said turbine for further cooling said purifying liquids.

References Cited (Backward Citations)

US2410457A Cited
US2785879A Cited
US3277179A Cited
US3153914A Cited
US3198441A Cited
US3423078A Cited
US3447492A Cited
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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) 1977-10-07 1978-04-08 1978-10-08 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1981-10-07 1982-04-08 1982-10-08 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1985-10-07 1986-04-08 1986-10-08 $7700.00 Window Closed / Lapsed

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