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    • 9. 发明公开
    • ADSORBENT FOR GASEOUS CHEMICAL SUBSTANCE AND APPARATUS FOR ADSORBING AND REMOVING USING THE SAME
    • 吸附剂吸附和距离,这种吸附剂气态化学物质和设备
    • EP1195195A1
    • 2002-04-10
    • EP00917302.2
    • 2000-04-13
    • Daikin Industries, Ltd.
    • TAMURA, YoshioSHINODA, Yasuyoshi
    • B01J20/18B01D53/06
    • B01J20/28045B01D53/02B01D53/06B01D2253/1085B01D2253/25B01D2253/3425B01D2257/40B01D2257/406B01D2257/70B01D2259/4009B01J20/18B01J2220/42F24F3/1423F24F2203/1036F24F2203/1048F24F2203/1056F24F2203/1068F24F2203/1088
    • A gaseous chemical substance adsorbent formed of a honeycomb-like laminate carrying a zeolite having an SiO 2 /Al 2 O 3 mole-ratio of greater than 70 and a zeolite having a mole-ratio of from 5 to 70. A rotor (2) formed from the gaseous chemical substance adsorbent in an approximately cylindrical form so that a gas passes through in an axial direction, the rotor being connected to gas-guiding portions (8), (12), and (15) formed by circumferentially partitioning the rotor (2) into an adsorbing portion, a regenerating portion, and a cooling portion in this order at both axial sides thereof, wherein a gas to be treated containing gaseous chemical substances is fed to the adsorbing portion (16); a regeneration gas is fed to the regenerating portion (17) after being heated by heating means (11); and a cooling gas is fed to the cooling portion (18). The rotor 2 is rotated from the adsorbing portion (16) to the regenerating portion (17), and subsequently to the cooling portion (18), whereby the gaseous chemical substances adsorbed in the adsorbing portion (16) are desorbed by heating in the regenerating portion (17) and are cooled to a temperature suitable for adsorption in the cooling portion (18).
    • FORMED承载具有大于70的SiO2 / Al2O3的摩尔比和具有5至70的摩尔比的沸石的沸石的蜂窝状的层压板的气态化学物质的吸附剂的转子(2)从该气态FORMED 在大致圆筒状的化学物质吸附剂所以做了气体通过在轴向方向上,所述转子被连接至(8),(12)和(15)通过沿周向分割转子FORMED引导气体部分(2)代入 在在两个轴向侧以该顺序吸附部,再生部和冷却部分,其worin气体待处理的含气态化学物质被供给到吸附部(16); 再生气体通过加热装置加热后供给到再生部(17)(11); 和冷却气体被供给到冷却部(18)。 转子2被从吸附部(16)到再生部分(17)旋转,并且随后向冷却部分(18),由此所述气态化学物质在吸附部(16)吸附的通过加热在再生解吸 在部分(17),并冷却至适合于吸附在冷却部分(18)的温度。