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公开(公告)号:FR2580951B1
公开(公告)日:1990-05-11
申请号:FR8516282
申请日:1985-11-04
Applicant: TAMPELLA OY AB
Inventor: HAMALA SIRPA , KENAKKALA TIMO , JANKA PENTTI , RUOHOLA TUOMO , LEHTIMAKI MARTTI
IPC: B01D53/14 , B01D53/50 , B01D53/75 , B01D53/81 , C01B17/60 , C01F11/46 , C01F11/48 , B01D53/34 , C01B17/48
Abstract: The invention relates to a process and apparatus for causing the sulfur dioxide of flue gases to react to form solid sulfates and sulfites which can be separated from the flue gases. Sulfur dioxide containing flue gases (16) are directed according to the invention into one end of an oblong reaction zone (4), in addition to which pulverous calcium compounds and water are directed separately into the reaction zone at several points, and finally from the opposite end a flue gas suspension is withdrawn and directed to dust separation (5). By feeding the pulverous reagent and the water separately into the reactor 4, the problems involved in the preparing, handling and spraying of an aqueous slurry are avoided, in addition to which the retention time and the reaction conditions can be regulated easily in the oblong reactor 4.
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公开(公告)号:RO93451A2
公开(公告)日:1987-12-31
申请号:RO12071685
申请日:1985-11-08
Applicant: INST FIZICA TEHNOLOGIA APARATE , TAMPELLA OY AB
Inventor: FLOREA VICTOR , HAMALA SIRPA , GANCIU-PETCU MIHAI , KENAKKALA TIMO , EFTIMIE NICUSOR , IANKA PENTTI , RUOHOLA TUOMO , LEHTIMAKI MARTTI
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公开(公告)号:LV5586A3
公开(公告)日:1994-05-10
申请号:LV920548
申请日:1992-12-29
Applicant: TAMPELLA OY AB
Inventor: HAMALA SIRPA , KENAKKALA TIMO , JANKA PENTTI , RUOHOLA TUOMO , LEHTIMAKI MARTTI
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公开(公告)号:IT1185834B
公开(公告)日:1987-11-18
申请号:IT6794485
申请日:1985-11-08
Applicant: TAMPELLA OY AB
Inventor: HAMALA SIRPA , KENAKKALA TIMO , JANKA PENTTI , RUOHOLA TUOMO , LEHTIMAKI MARTTI
Abstract: The invention relates to a process and apparatus for causing the sulfur dioxide of flue gases to react to form solid sulfates and sulfites which can be separated from the flue gases. Sulfur dioxide containing flue gases (16) are directed according to the invention into one end of an oblong reaction zone (4), in addition to which pulverous calcium compounds and water are directed separately into the reaction zone at several points, and finally from the opposite end a flue gas suspension is withdrawn and directed to dust separation (5). By feeding the pulverous reagent and the water separately into the reactor 4, the problems involved in the preparing, handling and spraying of an aqueous slurry are avoided, in addition to which the retention time and the reaction conditions can be regulated easily in the oblong reactor 4.
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