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process for reducing the content of alkaline substances in the cement clinker and to obtain dust rich in alkaline substances in combustion plants, cement

机译:降低水泥熟料中碱性物质含量并在燃烧厂,水泥中获得富含碱性物质的粉尘的方法

摘要

946,872. Preheating cement clinker. POLYSIUS G.m.b.H. Feb. 6, 1961 [March 21, 1960], No. 4409/61. Heading F4B. [Also in Division C1] The content of alkalies, i.e. Na 2 O and K 2 O, in cement clinker is reduced and alkali-rich dusts are recovered in cement kilns operating with exhaust gas temperatures of 100-300‹C., e.g. Lepol travelling grate rotary kiln, by preheating the cement raw material by heat exchange with the hot exhaust gases, from the kiln which are withdrawn from the preheating at a point where their temperature is such that the sublimed alkalies in the gases begin to be deposited as a solid, the dust in the withdrawn gases are extracted, the dust-free gases returned to the preheating and the extracted dust is separated into an alkali-rich fraction used, e.g. as a fertilizer, and an alkali-poor fraction which is mixed with the raw material. The dusts may be separated by a wet method, e.g. by flotation in a solution saturated with alkali. Raw cement is fed via shoot 1 to travelling grate 2 and rotary kiln 5. Hot exhaust gases from 5 are fed to heating chamber 4 and through the cement on 2 to chamber 4SP1/SP which contains dust collectors 6. Gases from 6 pass via trunk 7 to drying chamber 3 and through the cement on 2 to chamber 3SP1/SP where fan 8 feeds a final dust separator 9. The dust collected is taken by conveyer belt 11 to be separated into the two fractions, the alkali poor fraction returning on to grate 2 via shoot 1. Specification 874,818 is referred to.
机译:946,872。预热水泥熟料。 POLYSIUS G.m.b.H. 1961年2月6日[1960年3月21日],编号4409/61。标题F4B。 [也在C1区]减少了水泥熟料中碱的含量,即Na 2 O和K 2 O,并在废气温度为100-300℃,例如100-300℃的水泥窑中回收了富含碱的粉尘。 Lepol移动炉排回转窑通过与热废气进行热交换对水泥原料进行预热,从窑中预热的窑在温度达到一定温度以使气体中升华的碱开始沉积时固体,抽出的气体中的粉尘被抽出,无粉尘气体返回到预热,抽出的粉尘被分离成富含碱的馏分,例如作为肥料,和与原料混合的贫碱部分。灰尘可以通过湿法分离,例如湿法分离。通过在饱和碱溶液中浮选而得。未加工的水泥经射料1送入移动炉排2和回转窑5。来自5的热废气被送入加热室4,并通过水泥2进入加热室4 1 ,该室包含集尘器6。来自6的气体通过主干7进入干燥室3,并通过水泥2进入室3 1 ,在此处风扇8送入最后的灰尘分离器9。收集的灰尘被传送带11吸收并分离。分为两部分,贫碱部分通过分支1返回炉排2。参见规格874,818。

著录项

  • 公开/公告号BE600235A

    专利类型

  • 公开/公告日1961-08-16

    原文格式PDF

  • 申请/专利权人 POLYSIUS G.M.B.H.;

    申请/专利号BE19610600235

  • 发明设计人 ERICH BADE;

    申请日1961-02-15

  • 分类号1C04BA;

  • 国家 BE

  • 入库时间 2022-08-23 18:52:43

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