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    • 1. 发明专利
    • Ash treatment method
    • ASH治疗方法
    • JP2003010814A
    • 2003-01-14
    • JP2001203080
    • 2001-07-04
    • Ebara Corp株式会社荏原製作所
    • MARUYAMA SHINSAKUUCHIDA TAKAHARUTSUDA SEIICHI
    • F23J1/00B01D11/02B09B3/00B09B5/00F27D17/00
    • Y02P10/283
    • PROBLEM TO BE SOLVED: To provide a method for obtaining a recyclable solid content by concentrating a heavy metal and by lowering the chloride ion concentration in the solid content of an exhaust gas generating from a melting furnace of fly ash. SOLUTION: The fly ash from an incineration furnace and/or the fly ash (a) from the melting furnace are continuously cleaned by washing the ashes with water, mechanically rubbing the surfaces of the ash a each other into slurry 1, and then subjecting the slurry 1 the solid/liquid separation process (2) to transfer salts to the water side (d) and remove the salts. The solid content (c) is melted at the melting furnace 4 into a molten solid content (g). The dust scattered in the exhaust gas (f) from the furnace 4 is captured 5 and mixed with water so that the dust is cleaned and makes into slurry 8. After that, the slurry (8) is subjected to the solid/liquid separation process 9 and the salts are transferred to the water side (m) and removed. Thus the solid content (p) enriched with the heavy metal is obtained and the exhaust gas (f) is captured by a dust collector after adding a neutralizing agent to the exhaust gas (f). The solid content is melted at the melting furnace 4, preferably in a reductive atmosphere.
    • 要解决的问题:提供一种通过浓缩重金属获得可回收固体含量的方法,并且通过降低由飞灰熔化炉产生的废气的固体含量中的氯离子浓度。 解决方案:来自焚烧炉和/或来自熔化炉的飞灰(a)的飞灰通过用水洗涤灰分并将灰分相互机械地摩擦成浆料1而连续清洗,然后使 浆料1固/液分离过程(2)将盐转移到水侧(d)并除去盐。 将固体成分(c)在熔融炉4熔融成熔融固体成分(g)。 捕获从炉4排出的废气(f)中的粉尘5并与水混合,使得灰尘被清洗并制成浆料8.之后,对浆液(8)进行固/液分离处理 9并将盐转移到水侧(m)并除去。 从而获得富含重金属的固体含量(p),并且在向排气(f)中加入中和剂之后,废气(f)被集尘器捕获。 固体含量在熔化炉4熔化,优选在还原性气氛中熔化。
    • 5. 发明专利
    • METHOD FOR SEPARATING AND REMOVING NON-FERROUS METALS IN WASTE
    • JP2000026924A
    • 2000-01-25
    • JP21027698
    • 1998-07-10
    • EBARA CORP
    • UCHIDA TAKAHARUHASHIMOTO HIROYUKINAGAI HIROSHI
    • B09B3/00C22B7/00C22B7/02
    • PROBLEM TO BE SOLVED: To provide a method for separating and removing non-ferrous metals from waste which is capable of efficiently separating the non-ferrous metals in the waste and decomposing org. chlorine compds. without the generation of dioxin. SOLUTION: The method for separating and removing the non-ferrous metals from the waste consists in mixing the waste and the org. chlorine compds. in such a manner that the total molar number of the non-ferrous metals in the waste and the chlorine molar number in the org. chlorine compds. attain 1:1 to 5, more particularly 1:2 in conversion. The non-ferrous metals in the waste are brought into reaction with the chlorine and carbon in the org. chlorine compds. under a reducing atmosphere under which the quantity of the oxygen existing during the reaction stage attains the theoretical quantity necessary for conversion of all the carbon-components in the supplied org. chlorine compds. to CO or below at a reaction temp. of 500 to 1200 deg.C, by which the non-ferrous metals are evaporated away in the form of metal chlorides. One or more kinds among vinyl chloride, vinylidene chloride, PCB, CNP, PCP, 2, 4, 5-T, 2, 4-D, PCDD and PCDF are usable as the org. chlorine compds.
    • 8. 发明专利
    • DETOXICATING METHOD OF INCINERATION FLY ASH
    • JP2001121103A
    • 2001-05-08
    • JP29936799
    • 1999-10-21
    • EBARA CORP
    • KARAKI RYOTAROUCHIDA TAKAHARU
    • B09B3/00
    • PROBLEM TO BE SOLVED: To provide a detoxicating method of incineration fly ash, which is capable of volatizing and separating heavy metals in the incineration fly ash. SOLUTION: The detoxicating method of the incineration fly ash has a 1st process for mixing waste polyvinyl chloride with the incineration fly ash containing one or more kinds of the heavy metals in the mixing ratio of (1:100) to (2:1), preferably (1:10) to (1:1) and heating at 200-600 deg.C and a 2nd process for heating the treated residue in the 1st process to 600-1,000 deg.C to oxidize to volatize and separate the heavy metals in the incineration fly ash, the heavy metals can be selected from lead (Pb), cadmium (Cd), mercury (Hg), arsenic (As), selenium (Se), antimony (Sb) and zinc (Zn) and the heating and oxidizing treatment in the 2nd process is performed preferably by controlling the concentration of oxygen in a reaction furnace so that the concentration of carbon in the incineration fly ash after the treatment is about 0.01-5%.