[특허]Flue gas desulfurization apparatus

Flue gas desulfurization apparatus 원문보기

IPC분류정보
국가/구분	United States(US) Patent 등록
국제특허분류(IPC7판)	B01D-053/50 B01D-053/75 C01F-011/46
출원번호	US-0590466 (2015-01-06)
등록번호	US-9504957 (2016-11-29)
발명자 / 주소	Liu, Kunlei Remias, Joseph E.
출원인 / 주소	UNIVERSITY OF KENTUCKY RESEARCH FOUNDATION
대리인 / 주소	King & Schickli, PLLC
인용정보	피인용 횟수 : 0 인용 특허 : 47

초록 ▼

An apparatus is provided for removing sulfur oxides from a flue gas stream. That apparatus includes an absorber tower having an upper section and a lower section. A packed bed unit is provided in the upper section of the absorber tower. A first recycling circuit is provided for recycling lime water to the lower section of the absorber. Further the apparatus includes a second recycling circuit for recycling caustic solution to the packed bed unit.

대표청구항 ▼

1. An apparatus for removing sulfur oxides from a flue gas stream, comprising: an absorber tower including a reaction chamber;a liquid collection tray dividing said reaction chamber into a lower section and an upper section;a packed bed unit in said upper sectiona first circuit for circulating a first solution through said lower section in a first direction, wherein the first solution is selected from a group of solutions consisting of limewater, a limestone slurry and combinations thereof;a second circuit for circulating a second solution through said upper section and said packed bed unit in said first direction, wherein said second solution is a caustic solution, wherein said second circuit further includes a slurry tank and a solids/wetcake separator;a flue gas inlet in communication with said lower section and a treated flue gas outlet in communication with said upper section whereby a flue gas stream passes in a second direction through said lower section past said liquid collection tray and then through said upper section including said packed bed unit. 2. The apparatus of claim 1, wherein said caustic solution comprises a soluble calcium compound in combination with an alkali caustic reagent at an operating pH of between 6 and 7.5. 3. The apparatus of claim 2, wherein said alkali caustic reagent is selected from a group consisting of sodium hydroxide, potassium hydroxide, sodium carbonate/bicarbonate, potassium carbonate/bicarbonate and mixtures thereof. 4. The apparatus of claim 3, wherein said first solution has an operating pH between 2.5 and 7. 5. The apparatus of claim 1, wherein said liquid collection tray collects said caustic solution while allowing passage of flue gas. 6. The apparatus of claim 5, further including a sump at a bottom of said lower section. 7. The apparatus of claim 6, wherein said first circuit includes at least one first spray head, a first inlet in communication with said sump and at least one first pump for circulating said first solution from said sump to said at least one first spray head. 8. The apparatus of claim 7, wherein said second circuit includes at least one second spray head, a second inlet in communication with said liquid collection tray and at least one second pump for circulating said caustic solution from said liquid collection tray to said at least one second spray head overlying said packed bed unit. 9. The apparatus of claim 8, wherein lime or limestone is added to a sulfur rich caustic solution in said slurry tank to convert said soluble sulfur to gypsum and said gypsum and other solids are then removed from said caustic solution by said solution/wetcake separator before circulating said caustic solution back to said at least one second spray head. 10. The apparatus of claim 9, further including a caustic solution source connected to said second circuit between said solids/wetcake separator and said at least one second spray head. 11. The apparatus of claim 10, further including a gypsum discharge circuit including a third inlet in communication with said sump, at least one third pump, at least one solids separator and an outlet in communication with said at least one first spray head whereby gypsum is separated from said first solution and said first solution is returned to said lower section of said absorber tower. 12. The apparatus of claim 11, wherein said absorber tower further includes an oxidation air inlet in communication with said lower section and with said slurry tank. 13. The apparatus of claim 12, further including a first solution makeup circuit including a water source, a source of lime or limestone, a mill for milling said lime or limestone, a second slurry tank for receiving water and lime or limestone from said sources and creating said first solution, a fourth pump for pumping and an outlet for delivering said first solution to said lower section of said absorber tower. 14. A method of removing sulfur oxides from a flue gas stream, comprising; delivering a flue gas stream to an absorber tower including a lower section and an upper section;treating said flue gas stream with a countercurrent stream of a first solution of limewater or limestone slurry in said lower section;subsequently passing said flue gas through a packed bed unit while contacting said flue gas with a caustic solution in said upper section; anddischarging treated flue gas from said absorber tower. 15. The method of claim 14, including collecting said caustic solution in a liquid collecting tray at a bottom of said upper section. 16. The method of claim 15, further including removing sulfur from said caustic solution collected by said liquid collection tray. 17. The method of claim 16, including recirculating said caustic solution through said upper section through a second spray head above said packed bed unit. 18. The method of claim 17, wherein said sulfur is removed from said caustic solution by reacting said soluble sulfur with calcium hydroxide to produce gypsum and then separating said gypsum from said caustic solution. 19. The method of claim 18, including recirculating said first solution through said lower section to a first spray head below said liquid collection tray.

이 특허에 인용된 특허 (47)

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