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US4325713A Expired / Lapsed US ⏱️ 0.0 years remaining

Air pollution control process and apparatus

Assignee: WOLF RIDGE Corp A CORP OF Co
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Filing: 1978-07-31
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Granted: 1982-04-20
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Expires: 1998-07-31
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Abstract

Abstract Improved combination wet absorber/spray-dry dry wastes collection air pollution control process and apparatus therefor, employing aqueous solutions of sodium or ammonium alkali sorbents injected in an absorber through which SO x -containing flue or process gases containing fly ash are passed. Fly ash is collected in the absorber wherein the alkali reacts with the SO x to form sodium and ammonium sulfur oxide salts liquor containing collected fly ash in slurry form, which is passed back upstream and injected into a spray dryer through which the gases pass. The heat of the gases in the spray dryer dries the slurry to a powder of salts and fly ash which is removed. The spray dryer simultaneously provides some added preliminary SO x removal.

Inventors

  • 👤 Harvey S. Rosenberg
  • 👤 Joseph M. Genco

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 05:06
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/50; B01D53/501

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 312 words
Method of removal of SO x and fly ash particulates from hot flue gases comprising: (a) passing said hot flue gases through a flue gases pretreatment and waste products dry collection zone; (b) introducing an aqueous reaction products liquor containing ammonium or sodium sulfur oxide salts and at least a portion of said fly ash in a slurry form into said hot flue gases in a first portion of said pretreatment-dry collection zone in a finely divided condition and at a solids content sufficient to permit evaporation of substantially all of the water content of said liquor and produce dried particles of ammonium and sodium sulfur oxide salts; (c) removing a first, major portion of said dried salts particles in association with fly ash in a second portion of said pretreatment-dry collection zone to produce a partially cleaned flue gas containing a minor portion of said dried salts particles, and said fly ash; (d) introducing said partially cleaned flue gas containing said fly ash into a reaction zone; (e) contacting said partially cleaned flue gas containing said fly ash in said reaction zone with an aqueous ammonium or sodium alkali SO x sorbent liquor selected from NH 4 OH, (NH 4 ) 2 CO 3 , NH 4 HCO 3 , NaOH, Na 2 CO 3 , NaHCO 3 and mixtures thereof for a time sufficient: (i) to react SO 2 and SO 3 in said partially cleaned flue gas therewith to form said reaction products liquor and fly ash slurry; (ii) to collect dried salts particles and said fly ash from said partially cleaned flue gas, and (iii) to form substantially clean flue gas; (f) exhausting said clean flue gas from said reaction zone; and (g) passing reaction product liquor containing at least a portion of said fly ash in slurry form from said reaction zone to said pretreatment-dry collection zone.
Claim 2
Dependent Claim 312 words
Method of removal of SO x and fly ash particulates from hot flue gases comprising: (a) passing said hot flue gases through a flue gases pretreatment and waste products dry collection zone; (b) introducing an aqueous reaction products liquor containing ammonium or sodium sulfur oxide salts and at least a portion of said fly ash in a slurry form into said hot flue gases in a first portion of said pretreatment-dry collection zone in a finely divided condition and at a solids content sufficient to permit evaporation of substantially all of the water content of said liquor and produce dried particles of ammonium and sodium sulfur oxide salts; (c) removing a first, major portion of said dried salts particles in association with fly ash in a second portion of said pretreatment-dry collection zone to produce a partially cleaned flue gas containing a minor portion of said dried salts particles, and said fly ash; (d) introducing said partially cleaned flue gas containing said fly ash into a reaction zone; (e) contacting said partially cleaned flue gas containing said fly ash in said reaction zone with an aqueous ammonium or sodium alkali SO x sorbent liquor selected from NH 4 OH, (NH 4 ) 2 CO 3 , NH 4 HCO 3 , NaOH, Na 2 CO 3 , NaHCO 3 and mixtures thereof for a time sufficient: (i) to react SO 2 and SO 3 in said partially cleaned flue gas therewith to form said reaction products liquor and fly ash slurry; (ii) to collect dried salts particles and said fly ash from said partially cleaned flue gas, and (iii) to form substantially clean flue gas; (f) exhausting said clean flue gas from said reaction zone; and (g) passing reaction product liquor containing at least a portion of said fly ash in slurry form from said reaction zone to said pretreatment-dry collection zone.
Claim 3
Dependent Claim 29 words
A process as in claim 1 wherein: (a) the solids content ratio of said reaction products liquor bleed stream is maintained between about 5-50 weight percent in said liquor.
Claim 4
Dependent Claim 44 words
A process as in claim 2 wherein: (a) the temperature of dirty flue gases entering said pretreatment-collection zone is maintained in the range of about 275°-800° F.; (b) and the average temperature of said partly cleaned flue gas is maintained between about 100°-180° F.
Claim 5
Dependent Claim 57 words
A process as in claim 3 which includes: (a) recycling a portion of said reaction products liquor to said reaction zone to maintain the average residence time of said sorbent alkali in said reaction zone sufficient to utilize more than 80% of said alkali values, and to maintain said solids content level in said reaction products liquor.
Claim 6
Dependent Claim 51 words
A process as in claim 4 which includes: (a) passing said reaction product liquor and fly ash slurry to a settling zone; and (b) separating at least a portion of said fly ash particulates entrained in said liquor from said slurry prior to passing said liquor to said pretreatment-dry collection zone.
Claim 7
Dependent Claim 30 words
A process as in claim 5 which includes: (a) oxidizing sulfite values in said reaction product liquor to sulfate prior to passing said reaction product liquor to said pretreatment-collection zone.

References Cited (Backward Citations)

US2231309A Cited
US3533748A Cited
US3929968A Cited
US4039304A Cited
US4039304B1 Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1985-04-19 1985-10-19 1986-04-20 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1989-04-19 1989-10-19 1990-04-20 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1993-04-19 1993-10-19 1994-04-20 $7700.00 Window Closed / Lapsed

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