Clear liquor scrubbing magnesium-enhanced lime flue gas desulfurization system

• US 5,340,547 A
• Filed: 01/19/1993
• Issued: 08/23/1994
• Est. Priority Date: 11/22/1991
• Status: Expired due to Fees

• Current Assignee: Electric Power Research Institute
• Original Assignee: Electric Power Research Institute
• Inventors: Burke, John, Gray, Sterling, Moser, Robert E., Wilhelm, James H.
• Primary Examiner(s): NOT, DEFINED
• Assistant Examiner(s): Trembley, T. A.
• Application Number:
  US07/986,068
• Time in Patent Office: 581 Days
• Field of Search: 422/105, 422/110, 422/111, 422/177, 422/168, 423/243.1, 423/243.08, 423/243.11
• US Class Current: 422/177
• CPC Class Codes: B01D 53/501 by treating the gases with a solution or a suspension of an alkali or earth-alkali or ammonium compound

Abstract

An improved magnesium-enhanced lime flue gas desulfurization system is provided which produces the high sulfur dioxide removal level of previous magnesium-enhanced lime flue gas desulfurization systems and additionally produce waste solids that have significantly better properties and are more easily dewatered than the solids produced by known systems. The magnesium-enhanced lime flue gas desulfurization system of the present invention includes a crystallizer-clarifier reaction tank (CCRT) which receives scrubber effluent and functions as a combined reaction tank and thickener. Clear liquor from the CCRT is sent to a scrubber to scrub the flue gas, and a portion of the CCRT--thickened solids are directed to a high pH premix slurry tank (PMST) where the crystallization environment can be controlled by reagent addition and pH. The PMST contents are circulated to the CCRT and are separated to produce a waste solids fraction that is easily dewatered. A fines removal system may also be employed to reduce the presence of fine solids and promote large crystal solids.

Claims

1. A magnesium-enhanced lime flue gas desulfurization system wherein sulfur dioxide is removed from a supply of sulfur dioxide-containing gas by scrubbing in the presence of aqueous magnesium and lime to produce easily dewatered calcium sulfite waste solids, said system comprising:

(a) scrubber means for receiving a supply of sulfur dioxide-containing gas and contacting said sulfur dioxide-containing gas with an aqueous liquid, said scrubber means including a first discharge outlet for scrubbed gas and a second discharge outlet for scrubber effluent;

(b) crystallizer-clarifier reaction tank means fluidically connected to said scrubber means for receiving scrubber effluent and for separating said scrubber effluent into a clear liquor fraction and a thickened solids fraction;

(c) premix slurry tank means fluidically connected to said crystallizer clarifier reaction tank means for receiving and crystallizing said thickened solids fraction, wherein said premix slurry tank means includes reagent addition means for adding reagent to said premix slurry tank means;

pH control means for controlling crystal formation and growth, an inlet for receiving said thickened solids fraction from the crystallizer-clarifier reaction tank means and an outlet for directing crystallized solids back to said crystallizer-clarifier reaction tank means; and

(d) solids dewatering means for separating solids recirculated through said crystallizer-clarifier reaction tank means and for producing an aqueous liquid fraction for circulation through the system to said scrubber means and to contact said sulfur dioxide-containing gas.

2. The magnesium-enhanced lime flue gas desulfurization system of claim 1, wherein said crystallizer-clarifier reaction tank means includes a reaction zone, a clarifying zone and a thickening zone, and said scrubber effluent is received in said reaction zone and said thickened solids fraction is discharged from said thickening zone to said premix slurry tank means.

3. The magnesium-enhanced lime flue gas desulfurization system of claim 2, wherein said clarifying zone is fluidically connected to said scrubber means to direct said clear liquor fraction to said scrubber means.

4. The magnesium-enhanced lime flue gas desulfurization system of claim 1, wherein said reagent addition means includes reagent control means for adding only desired quantities of reagents to said premix slurry tank means to produce optimum crystal size and shape.

5. The magnesium-enhanced lime flue gas desulfurization system of claim 4, wherein said pH control means includes slurry pump means for regulating the flow of said thickened solids fraction to said premix slurry tank means to main the pH of said premix slurry tank means within the range of 9.5-12.

7. The magnesium-enhanced lime flue gas desulfurization system of claim 1, further including fines removal means fluidically interposed between said crystallizer-clarifier reaction tank means and said scrubber means for removing fine solids from the fractions produced by the crystallizer-clarifier reaction tank means.

8. The magnesium-enhanced lime flue gas desulfurization system of claim 7, wherein said fines removal means is further fluidically connected to said premix slurry tank means.

6. The magnesium-enhanced lime flue gas desulfurization system 4, wherein said pH control means includes valve means for regulating the flow of said thickened solids fraction to said premix slurry tank to maintain the pH of said premix slurry tank within the range of 9.5-12.