KR930007492A - Desulfurization Method Using Magnesium Hydroxide Slurry and Its Apparatus - Google Patents

Desulfurization Method Using Magnesium Hydroxide Slurry and Its Apparatus Download PDF

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Publication number
KR930007492A
KR930007492A KR1019910019125A KR910019125A KR930007492A KR 930007492 A KR930007492 A KR 930007492A KR 1019910019125 A KR1019910019125 A KR 1019910019125A KR 910019125 A KR910019125 A KR 910019125A KR 930007492 A KR930007492 A KR 930007492A
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KR
South Korea
Prior art keywords
magnesium hydroxide
cooling tower
tower
waste gas
cooling
Prior art date
Application number
KR1019910019125A
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Korean (ko)
Inventor
황명수
Original Assignee
이종근
삼화화성 주식회사
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Publication date
Application filed by 이종근, 삼화화성 주식회사 filed Critical 이종근
Priority to KR1019910019125A priority Critical patent/KR930007492A/en
Publication of KR930007492A publication Critical patent/KR930007492A/en

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Abstract

냉각탑과 흡수탑으로 이루어진 탈황장치에서, 냉각탑(10)벽의 외부에 냉각수 공급배관(14)이 그리고 냉각탑 벽면에 스프레이 노즐(16)의 끝단(18)이 지그재그 형태로 설치되어 있으며, 흡수탑(12) 내부에 충진층(20)이 장치되어 있고 상부에는 엘리미네이트(22)가 설치되어 있으며 충진층에서 수산화마그네슘 슬러리와 폐가스가 접촉됨을 특징으로 하는 수산화마그네슘 슬러리를 이용한 탈황장치, 폐가스중의 아황산가스는 냉각탑(10)외벽에 설치된 냉각수 공급배관(14)과 연결된 스프레이 노즐(16)을 통해 스프레이 노즐의 끝단(18)에서 약 5m의 스프레이 입도 도달거리로 냉각수를 냉각탑의 내부에 공급하여 폐가스 유입구(24)를 통해 들어온 폐가스를 약 35-40℃의 온도까지 냉각하고, 흡수탑(12)에서 저액기비의 수산화마그네슘 슬러리 희석용액을 디스트리뷰터를 통해 분사하여 충진탑에서 흡수함.In the desulfurization apparatus consisting of a cooling tower and an absorption tower, a cooling water supply pipe 14 is disposed outside the wall of the cooling tower 10 and an end 18 of the spray nozzle 16 is installed in a zigzag form on the wall of the cooling tower. 12) Desulfurization apparatus using magnesium hydroxide slurry, characterized in that the magnesium hydroxide slurry and the waste gas in contact with the filling layer 20 is installed inside, and the laminate 22 is installed on the upper portion, the waste gas in the waste gas Sulfur dioxide gas is supplied through the spray nozzle 16 connected to the cooling water supply pipe 14 installed on the outer wall of the cooling tower 10 to the inside of the cooling tower at a spray particle size of about 5 m from the end 18 of the spray nozzle. The waste gas introduced through the inlet port 24 is cooled to a temperature of about 35-40 ° C., and the low liquid ratio magnesium hydroxide slurry dilution solution is removed from the absorption tower 12. By injection through absorbs in the packed column.

Description

수산화 마그네슘 슬러리를 이용한 탈황방법 및 그 장치.Desulfurization method and apparatus using magnesium hydroxide slurry.

본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음Since this is an open matter, no full text was included.

첨부도면은 이 발명에 따른 수산화마그네슘 슬러리를 이용한 탈황장치의 개략도임.The accompanying drawings are schematic diagrams of a desulfurization apparatus using a magnesium hydroxide slurry according to the present invention.

Claims (2)

냉각탑과 흡수탑으로 이루어진 탈황장치에서, 냉각탑(10)벽의 외부에 냉각수 공급배관(14)이 그리고 냉각 탑 벽면에 스프레이 노즐(16)의 끝단(18)이 지그재그 형태로 설치되어 있으며, 흡수탑(12) 내부에 충진층(20)이 장치되어 있고 상부에는 엘리미네이트(22)가 설치되어 있으며 충진층에서 수산화마그네슘 슬러리와 폐가스가 접촉됨을 특징으로 하는 수산화마그네슘 슬러리를 이용한 탈황장치.In the desulfurization device consisting of a cooling tower and an absorption tower, the cooling water supply pipe 14 is installed outside the wall of the cooling tower 10 and the end 18 of the spray nozzle 16 is provided in a zigzag form on the cooling tower wall. (12) Desulfurization apparatus using a magnesium hydroxide slurry, characterized in that the filling layer (20) is provided inside, the elimination (22) is installed on the upper portion, and the magnesium hydroxide slurry and waste gas in contact with the filling layer. 냉각탑(10) 외벽에 설치된 냉각수 공급배관(14)과 연결된 스프레이 노즐(16)을 통해 스프레이 노즐의 끝단(18)에서 약 5m의 스프레이 입도 도달거리로 냉각수를 냉각탑의 내부에 공급하여 폐가스 유입구(24)를 통해 들어온 폐가스를 약 35-40℃의 온도까지 냉각하고, 흡수탑(12)에서 저액기비의 수산화마그네슘 슬러리 희석용액을 디스트리뷰터를 통해 분사하여 충진탑에서 아황산가스를 흡수하는 단계로 이루어진 수산화마그네슘 슬러리를 이용한 탈황방법.Through the spray nozzle 16 connected to the cooling water supply pipe 14 installed on the outer wall of the cooling tower 10, the cooling water is supplied to the inside of the cooling tower at a spray particle size reach of about 5 m from the end 18 of the spray nozzle, thereby providing a waste gas inlet 24. Magnesium hydroxide consisting of cooling the waste gas to the temperature of about 35-40 ℃ and absorbing the sulfur dioxide dilution solution of the low liquid ratio of the magnesium hydroxide slurry through the distributor in the absorption tower 12 to absorb the sulfite gas from the packing tower. Desulfurization method using slurry. ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.※ Note: The disclosure is based on the initial application.
KR1019910019125A 1991-10-30 1991-10-30 Desulfurization Method Using Magnesium Hydroxide Slurry and Its Apparatus KR930007492A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1019910019125A KR930007492A (en) 1991-10-30 1991-10-30 Desulfurization Method Using Magnesium Hydroxide Slurry and Its Apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR1019910019125A KR930007492A (en) 1991-10-30 1991-10-30 Desulfurization Method Using Magnesium Hydroxide Slurry and Its Apparatus

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KR930007492A true KR930007492A (en) 1993-05-20

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100364412B1 (en) * 2000-04-17 2002-12-11 삼성전기주식회사 Deflection yoke
KR100851555B1 (en) * 2006-02-06 2008-08-11 주식회사 얼라이브텍 METHOD FOR REMOVING SOx WITH BRUCITE SLURRY
KR100851556B1 (en) * 2008-05-26 2008-08-11 주식회사 얼라이브텍 METHOD FOR REMOVING SOx WITH BRUCITE SLURRY

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100364412B1 (en) * 2000-04-17 2002-12-11 삼성전기주식회사 Deflection yoke
KR100851555B1 (en) * 2006-02-06 2008-08-11 주식회사 얼라이브텍 METHOD FOR REMOVING SOx WITH BRUCITE SLURRY
KR100851556B1 (en) * 2008-05-26 2008-08-11 주식회사 얼라이브텍 METHOD FOR REMOVING SOx WITH BRUCITE SLURRY

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