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    • 5. 发明专利
    • System for utilizing biomass
    • 利用生物量的系统
    • JP2006191876A
    • 2006-07-27
    • JP2005007968
    • 2005-01-14
    • Mitsubishi Heavy Ind Ltd三菱重工業株式会社
    • SUGATA KIYOSHIAMARI TAKESHI
    • A01G9/18A01G7/00A01G7/02A01G9/24A01G11/00A01N59/00A01N59/04B09B3/00C09K17/02C09K101/00C10B53/02
    • Y02A40/268Y02E50/14Y02E50/30Y02P20/124Y02P20/129Y02P60/147Y02W30/20Y02W30/78
    • PROBLEM TO BE SOLVED: To provide a system for utilizing biomass in which problems in protected horticulture are solved and at the same time, prevention of global warming by discharge suppression of carbon dioxide, effective utilization of resources and reduction of wastes are made possible by combining facilities for protected horticulture with carbonization and gasification treatment facilities.
      SOLUTION: The system is equipped with a carbonizing furnace 13 for producing a carbonized product 14 and a degradation gas 15 by carrying out carbonization and gasification treatment of a wood-based biomass 10, a waste heat boiler 16 for burning the degradation gas 15 and recovering heat energy, facilities 50 for protected horticulture for carrying out culture of plants under conditions in which culturing environment is controlled by partition from the outside. In the system, a combustion discharge gas 39 discharged from the waste heat boiler 16 is introduced into the facilities 50 for protected horticulture and CO
      2 concentration in the facilities 50 for protected horticulture is preferably detected and combustion discharge gas introduction amount is controlled based on the detected CO
      2 concentration.
      COPYRIGHT: (C)2006,JPO&NCIPI
    • 要解决的问题:提供一种利用生物质的系统,其中解决了保护园艺问题,同时,通过排放二氧化碳排放,有效利用资源和减少废物来防止全球变暖 可以通过将受保护的园艺设施与碳化和气化处理设施相结合。 解决方案:该系统配备有用于通过进行木质生物质10的碳化和气化处理来生产碳化产物14和降解气体15的碳化炉13,用于燃烧劣化气体的废热锅炉16 并且回收热能,用于保护园艺的设施50用于在从外部分配控制培养环境的条件下进行植物培养。 在该系统中,从废热锅炉16排出的燃烧排放气体39被引入用于保护园艺的设备50中,并且优选检测用于保护园艺的设备50中的CO 2 浓度,并且燃烧放出气体 基于检测到的CO 2 浓度控制引入量。 版权所有(C)2006,JPO&NCIPI
    • 6. 发明专利
    • Methane fermentation tank
    • 甲烷发酵罐
    • JP2003039099A
    • 2003-02-12
    • JP2001227717
    • 2001-07-27
    • Mitsubishi Heavy Ind Ltd三菱重工業株式会社
    • UKAI NOBUYUKIOMURA TOMOAKISUGATA KIYOSHISHINDO YOSHITAKEMIZUTANI HIROSHI
    • C02F11/04B01F3/12B01F7/04
    • Y02E50/343
    • PROBLEM TO BE SOLVED: To provide a methane fermentation tank which enables methane fermentation to be conducted while effectively removing a gas from a high- concentration sludge such as a dewatered sludge. SOLUTION: This methane fermentation tank is a horizontal anaerobic tank for conducting methane fermentation by taking thereinto a high-concentration sludge and has a sludge intake section formed at its one side and a sludge outlet section formed at the other side. In the tank, a multistage agitation blade is installed along the direction from the intake section to the outlet section so that the rotary displacement of the agitation blade develops a transfer power in the direction from the intake section to the outlet section. At the upper part of the tank, a gas reservoir space connected to a gas draw route is formed.
    • 要解决的问题:提供能够在有效地从高浓度污泥如脱水污泥中除去气体的同时进行甲烷发酵的甲烷发酵罐。 解决方案:该甲烷发酵罐是一种水平厌氧罐,用于通过吸入高浓度污泥进行甲烷发酵,并在其一侧形成污泥进料部分,在另一侧形成污泥出口部分。 在储罐中,沿着从进气段到出口部分的方向安装多级搅拌叶片,使得搅拌叶片的旋转位移在从进气部分到出口部分的方向上产生传递力。 在罐的上部形成有连接到气体抽吸路线的气体储存空间。
    • 7. 发明专利
    • METHOD AND EQUIPMENT FOR ANAEROBIC DIGESTION OF ORGANIC SLUDGE
    • JP2002307098A
    • 2002-10-22
    • JP2001115281
    • 2001-04-13
    • MITSUBISHI HEAVY IND LTD
    • OMURA TOMOAKIUKAI NOBUYUKISUGATA KIYOSHI
    • C12M1/00B09B3/00C02F11/02C02F11/04C12N1/00
    • PROBLEM TO BE SOLVED: To provide an anaerobic digestion equipment for organic sludge, which can decrease the installation space of a methane fermentation device in a broad sense, where solubilization, acid production, and the methane fermentation are carried out, and reduce the entire time for digestion and methane fermentation from the start of feed to the digestion equipment up to discharge therefrom. SOLUTION: In this anaerobic digestion method of organic sludge for carrying out a sludge treatment while sequentially performing digestion treatments comprising solubilization, acid production, and methane fermentation of organic sludge, such as surplus sludge, dewatered sludge, and waste water, a plurality of stages of digestion treatment areas are arranged so as to be mutually communicated almost in series. In order to stepwise change the organic acids to lower molecular compounds along the flow direction of the organic sludge and to complete a gasification process of the methane fermentation in the final treatment area, the sludge is allowed to move gradually from upperstream treatment areas to downstream treatment areas by an extrusion flow, the capacity or the number of stages is set in inverse proportion to the rate required for the digestion of each treatment area, in other words, when the digestion rate is high, a small capacity is set, and when the rate is low, a large capacity or a plurality of stages are set.