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    • 3. 发明专利
    • Waste cleaning method
    • 废水清洗方法
    • JP2003334512A
    • 2003-11-25
    • JP2002143924
    • 2002-05-20
    • Kubota Corp株式会社クボタ
    • HORII YASUOISHIHARA TATSUHIROHIROSE YOICHIRO
    • B08B3/04B09B1/00B09B3/00
    • PROBLEM TO BE SOLVED: To provide a waste cleaning method which enables the discharge of washing wastewater after waste is washed while making the concentration thereof almost constant to reduce the amount of washing water to be used.
      SOLUTION: The washing wastewater B discharged from a washing apparatus 2 after utilized in the washing of waste is sent to a storage tank 11 and waste is washed in the washing apparatus 2 until the electric conductivity of washing wastewater B flowing through a circulating route 12 rises to reach a set value while circulating the washing wastewater B by returning the washing wastewater B in the storage tank 11 through the circulating route 12. The washing wastewater B the electric conductivity of which reaches the set value is discharged to the outside of the storage tank 11 to be sent to treatment facilities 14 while new washing water A is supplied to the washing apparatus 2.
      COPYRIGHT: (C)2004,JPO
    • 要解决的问题:提供一种废物清洗方法,其能够使废水洗涤后的洗涤废水排出,同时使其浓度几乎恒定,以减少所用洗涤水的量。 解决方案:洗涤设备2在洗涤废物中后排出的洗涤废水B被送到储罐11,废物在洗涤设备2中洗涤,直到洗涤废水B的电导率流过循环 通过循环路径12将洗涤废水B返回到储存罐11中,使路线12上升到达设定值,同时循环洗涤废水B.其电导率达到设定值的洗涤废水B排出到 储存罐11被送到处理设备14,同时将新的洗涤水A供应到洗涤装置2.版权所有(C)2004,JPO
    • 4. 发明专利
    • Circulation-reusing method for medicament in waste disposal
    • 废物处理药物循环回收方法
    • JP2005028310A
    • 2005-02-03
    • JP2003271663
    • 2003-07-08
    • Kubota Corp株式会社クボタ
    • NAKAGAWA KOICHIISHIHARA TATSUHIROHORII YASUO
    • B09B1/00C25B1/26
    • PROBLEM TO BE SOLVED: To provide a circulation-reusing method for medicaments in a waste disposal, by which a pH adjuster and a disinfectant used in an incineration facility and leachate treatment facility can be circulation-reused.
      SOLUTION: The landfill of a flying ash treatment object discharged from the incineration facility 1 is carried out in an ultimate disposal place 8. The leachate discharged from the ultimate disposal place 8 is treated at the leachate treatment facility 9, and a by-product salt 14 produced at the leachate treatment facility 9 is electrolytically treated with an electrolysis device 24 to reproduce NaOH, HCl, and NaOCl, which are reused in the leachate treatment facility or the incineration facility as pH adjusters or disinfectants 22 and 23.
      COPYRIGHT: (C)2005,JPO&NCIPI
    • 要解决的问题:提供一种用于废物处理中的药物的循环再利用方法,通过该循环再利用方法可以循环重复利用焚化设备中使用的pH调节剂和消毒剂和渗滤液处理设备。 解决方案:焚化设备1排放的飞灰处理物的垃圾填埋场是在最终处置场所8进行的。从最终处置场所8排出的渗滤液在渗滤液处理设备9处理, 在渗滤液处理设备9中产生的产物盐14用电解装置24进行电解处理,以再生NaOH,HCl和NaOCl,其在浸出液处理设施或焚化设备中重新用作pH调节剂或消毒剂22和23。 P>版权所有(C)2005,JPO&NCIPI
    • 5. 发明专利
    • Method for operating waste reclamation disposal facility
    • 操作垃圾回收处理设备的方法
    • JP2005021832A
    • 2005-01-27
    • JP2003191541
    • 2003-07-04
    • Kubota Corp株式会社クボタ
    • OKUNO YASUHIRONAKAGAWA KOICHISASAKI TOMOHIKOISHIHARA TATSUHIROHORII YASUO
    • B09B1/00C02F1/00
    • PROBLEM TO BE SOLVED: To provide a method for operating a waste reclamation disposal facility by which the treatment efficiency of the water to be treated in the treatment facility and the efficiency of reclamation operation are improved.
      SOLUTION: A coated area A in which the upper part is covered with a roof 5 is formed on a part of the reclamation region in a reclamation disposal site 2. The roof 5 is provided with sprinkling equipment 6 for performing artificial sprinkling to the covered area A. The remaining reclamation region other than the covered area A is formed as an open area B free from the roof 5. At the time when a leachate flowed out from the open area B by a natural rainfall to the open area B and a leachate flowed out from the coated area A by artificial water sprinkling to the covered area A are fed as the water to be treated from the reclamation disposal site 2 to the treatment facility 3, the artificial sprinkling water quantity is controlled, and the quantity of the leachate fed from the covered area A to the treatment facility 3 is increased or decreased. Thus, the variation in the quantity of the water to be treated owing to the change in the quantity of the natural rain-fall can be suppressed. Further, waste is reclaimed in the covered area A at snow fall, so that the efficiency of the reclamation operation can be improved.
      COPYRIGHT: (C)2005,JPO&NCIPI
    • 要解决的问题:提供一种操作废物回收处理设备的方法,通过该方法可以提高处理设施中待处理的水的处理效率和提高回收效率。 解决方案:在回收处理场所2的一部分填埋区域上形成有上部覆盖有屋顶5的涂覆区域A.屋顶5设置有喷洒设备6,用于进行人造喷洒 覆盖区域A.除了覆盖区域A之外的剩余的填海区域形成为没有屋顶5的开放区域B.当渗滤液从露天区域B通过自然降雨流出到开放区域B时 将通过人造水喷洒到覆盖区域A的涂布区域A的渗滤液作为被处理水从填埋处置场地2供给到处理设备3,控制人造喷水量, 从覆盖区域A向处理设备3供给的渗滤液的增加或减少。 因此,可以抑制由于自然降雨量的变化而被处理的水量的变化。 此外,在落雪时在覆盖区域A中回收废物,从而可以提高回收作业的效率。 版权所有(C)2005,JPO&NCIPI
    • 6. 发明专利
    • Method and equipment for pretreating oil containing aromatic chlorinated organic compound
    • 用于预处理含有芳香族有机化合物的油的方法和设备
    • JP2005305252A
    • 2005-11-04
    • JP2004123588
    • 2004-04-20
    • Kubota Corp株式会社クボタ
    • OKADA KOICHIISHIHARA TATSUHIROSHIOYAMA MASAHIKOSHIRAI ATSUHIKO
    • B01D21/00B01D3/10
    • PROBLEM TO BE SOLVED: To provide a pretreating method for decomposing the PCB-containing oil to be treated, in which impurities exerting bad influences on the reaction to be utilized when the oil to be treated is decomposed are removed from the oil to be treated to stabilize the reaction.
      SOLUTION: The oil 1 to be treated is withdrawn from a vessel 2 by using an oil withdrawing unit 11. A solid mixed in the withdrawn oil is settled, separated and removed in a precipitation tank 12. The solid-removed oil is stored temporarily in a storage tank 13 to stabilize the composition of the solid-removed oil. The composition-stabilized oil is distilled under reduced pressure in a reduced-pressure distillation unit 14 so that low-boiling point compounds 55 are separated/removed from the composition-stabilized oil.
      COPYRIGHT: (C)2006,JPO&NCIPI
    • 要解决的问题:提供一种用于分解待处理的含PCB油的预处理方法,其中当待处理的油分解时,对待使用的反应产生不良影响的杂质从油中除去至 治疗以稳定反应。 解决方案:通过使用抽油单元11将待处理的油1从容器2中取出。将在抽出的油中混合的固体在沉淀槽12中沉淀,分离和除去。固体除去的油是 临时储存在储罐13中以稳定固体除去的油的组成。 将组合物稳定的油在减压蒸馏单元14中减压蒸馏,使得低沸点化合物55从组合物稳定的油中分离/除去。 版权所有(C)2006,JPO&NCIPI