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    • 3. 发明专利
    • Heating treatment method
    • 加热处理方法
    • JPH11277031A
    • 1999-10-12
    • JP10220498
    • 1998-03-30
    • Mitsubishi Heavy Ind Ltd三菱重工業株式会社
    • SHIMIZU HIROSHIIWASHITA KOICHIROSUGITA SATORU
    • B09B3/00
    • PROBLEM TO BE SOLVED: To provide a heating treatment method of a powder or a liquid, which can miniaturize the equipment and perform the treatment operation highly effectively.
      SOLUTION: In a heating treatment method, a treatment part 10a to heat a powder or a liquid is separated from a heating part 10b burning fuel to heat the powder or the liquid to prevent the fuel and combustion air or combustion gas generated by combustion of the fuel from mixing into the inside of the treatment part 10a or a gas D1 derived from the treatment part 10a, and substances separated and formed in the gas D1 by heating the powder or the liquid, or substances newly formed by chemical reaction caused by heating is recovered in high concentration.
      COPYRIGHT: (C)1999,JPO
    • 要解决的问题:提供粉末或液体的加热处理方法,其可以使设备小型化并且高效地进行处理操作。 解决方案:在加热处理方法中,将加热粉末或液体的处理部分10a从燃烧燃料的加热部分10b分离以加热粉末或液体,以防止由燃烧产生的燃料和燃烧气体 燃料从混合进入处理部分10a的内部或来自处理部分10a的气体D1,通过加热粉末或液体或通过加热引起的化学反应新形成的物质在气体D1中分离形成的物质是 高浓度回收。
    • 6. 发明专利
    • TREATMENT OF SLUDGE CONTAINING ARSENIC
    • JP2000296400A
    • 2000-10-24
    • JP10401799
    • 1999-04-12
    • MITSUBISHI HEAVY IND LTD
    • SUGITA SATORUSHIMIZU HIROSHIIWASHITA KOICHIROBABA HIROSHIKAMIYOSHI HIDEKINISHIDA MORIMASA
    • C02F11/00C02F1/52C02F1/66C02F9/00C02F11/06C02F11/14
    • PROBLEM TO BE SOLVED: To eliminate the possibility of re-elution of arsenic from the calcined material when disposed as waste, or volatilization of arsenic compounds during the calcination treatment by adding a calcium compound to a separated arsenic-containing sludge slurry resulting from solid-liquid separation in arsenic-removal treatment of wastewater, subjecting the obtained material to dehydration and drying and thereafter subjecting the dried material to calcination treatment to form a calcined material. SOLUTION: This treatment process comprises: introducing wastewater into a first reaction vessel 1; adding slurryed slaked lime 12a to the wastewater and adjusting the pH of the resulting wastewater to >=12, to convert arsenic ion and other heavy metals into hydroxides, to form flocs and to generate an arsenic-containing sludge slurry; then in a first coagulating sedimentation tank 2, subjecting the flocs, (i.e., arsenic-containing sludge slurry) formed in the first reaction vessel 1 to sedimentation separation; subsequently, receiving the concentrated arsenic-containing sludge slurry subjected to sedimentation separation in the first coagulating sedimentation tank 2, in a sludge storage tank 5; adding slurryed slaked lime 12b similar to the slurryed slaked lime 12a to the concentrated sludge slurry, mixing them and storing the resulting sludge in the sludge storage tank 5; then dehydrating the sludge supplied from the storage tank 5 with a dehydrator 6 to form a cake; drying the cake with a dryer 7 to form a dried solid material; and calcining the dried solid material in a calcination furnace 8 to form a calcined material.