METHOD OF CEMENT OR CONCRETE PRODUCTION

    公开(公告)号:CS126390A2

    公开(公告)日:1991-08-13

    申请号:CS126390

    申请日:1990-03-15

    Applicant: TAMPELLA OY AB

    Abstract: A method of producing cement or concrete, comprising the step of adding fly ash to the cement or concrete at the production stage, the fly ash containing lime and reaction products from the reaction occurring between lime and sulphur oxides in connection with the desulphuration of flue gases. To avoid the disadvantageous effects of calcium sulphite and entringite reactions and to increase the used amount of fly ash containing desulphuration waste, the calcium sulphite is oxidized by hydrogen peroxide either before the production of cement or concrete or during the production.

    52.
    发明专利
    未知

    公开(公告)号:FI81558B

    公开(公告)日:1990-07-31

    申请号:FI891284

    申请日:1989-03-17

    Applicant: TAMPELLA OY AB

    Abstract: A method of producing cement or concrete, comprising the step of adding fly ash to the cement or concrete at the production stage, the fly ash containing lime and reaction products from the reaction occurring between lime and sulphur oxides in connection with the desulphuration of flue gases. To avoid the disadvantageous effects of calcium sulphite and entringite reactions and to increase the used amount of fly ash containing desulphuration waste, the calcium sulphite is oxidized by hydrogen peroxide either before the production of cement or concrete or during the production.

    59.
    发明专利
    未知

    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

    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separately into the reaction zone at several points, and finally from the opposite end a flue gas suspension is withdrawn and directed to dust separation (5).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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