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公开(公告)号:FI81024B
公开(公告)日:1990-05-31
申请号:FI872072
申请日:1987-05-11
Applicant: TAMPELLA OY AB
Inventor: HAEMAELAE SIRPA , HEIKKILAE MATTI , LAINE JOUKO , KOKKONEN KARI , KENAKKALA TIMO
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公开(公告)号:DD270015A5
公开(公告)日:1989-07-19
申请号:DD31567688
申请日:1988-05-11
Applicant: TAMPELLA OY AB
Inventor: HAEMAELAE SIRPA , HEIKKILAE MATTI , LAINE JOUKO , KOKKONEN KARI , KENAKKALA TIMO
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公开(公告)号:FI78845B
公开(公告)日:1989-06-30
申请号:FI851622
申请日:1985-04-24
Applicant: TAMPELLA OY AB
Inventor: HAEMAELAE SIRPA
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64.
公开(公告)号:GB2174081B
公开(公告)日:1988-11-23
申请号:GB8527453
申请日:1985-11-07
Applicant: TAMPELLA OY AB
Inventor: HAEMAELAE SIRPA , KENAKKALA TIMO , JANKA PENTTI , RUOHOLA TUOMO , LEHTIMAEKI 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separately into the reaction zone at several points, and finally from the opposite end a flue gas suspension is withdrawn and directed to dust separation (5).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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公开(公告)号:FI872072A
公开(公告)日:1988-11-12
申请号:FI872072
申请日:1987-05-11
Applicant: TAMPELLA OY AB
Inventor: HAEMAELAE SIRPA , HEIKKILAE MATTI , LAINE JOUKO , KOKKONEN KARI , KENAKKALA TIMO
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公开(公告)号:FI872061A
公开(公告)日:1988-11-12
申请号:FI872061
申请日:1987-05-11
Applicant: TAMPELLA OY AB
Inventor: LAINE JOUKO , HAEMAELAE SIRPA , JAERVINEN KIMMO , KENAKKALA TIMO
IPC: B01D20060101 , B01D53/34 , B01D
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公开(公告)号:FI872072A0
公开(公告)日:1987-05-11
申请号:FI872072
申请日:1987-05-11
Applicant: TAMPELLA OY AB
Inventor: HAEMAELAE SIRPA , HEIKKILAE MATTI , LAINE JOUKO , KOKKONEN KARI , KENAKKALA TIMO
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公开(公告)号:DD240839A5
公开(公告)日:1986-11-19
申请号:DD28203985
申请日:1985-10-24
Applicant: TAMPELLA OY AB
Inventor: HAEMAELAE SIRPA
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公开(公告)号:SE8505271L
公开(公告)日:1986-10-25
申请号:SE8505271
申请日:1985-11-07
Applicant: TAMPELLA OY AB
Inventor: HAEMAELAE SIRPA , KENAKKALA TIMO , JANKA PENTTI , RUOHOLA TUOMO , LEHTIMAEKI MARTTI
IPC: B01D53/14 , B01D53/50 , B01D53/75 , B01D53/81 , C01B17/60 , C01F11/46 , C01F11/48 , B01D53/34 , B01D53/10
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:ZA858478B
公开(公告)日:1986-07-30
申请号:ZA858478
申请日:1985-11-05
Applicant: TAMPELLA OY AB
Inventor: JANKA PENTTI , HAEMAELAE SIRPA , KENAKKALA TIMO , RUOHOLA TUOMO , LEHTIMAEKI 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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