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    • 51. 发明专利
    • Production of hydrogen from organic waste
    • 从有机废物中生产氢
    • JPS5950002A
    • 1984-03-22
    • JP16008582
    • 1982-09-13
    • Mitsubishi Electric Corp
    • MAEDA MITSUOHORIUCHI KOUICHI
    • C01B3/02C01B3/00C02F11/04
    • PURPOSE: To improve the energy density and utilization rate as compared to methane fermentation by bringing a product obtd. by the acid fermentation of org. waste into a photocatalyst in the presence of light to produce hydrogen.
      CONSTITUTION: Org. waste is charged into an acid fermentation vessel 1b from a duct 4. It is kept at 30W60°C with warm water subjected to heat exchange in a heat exchanger 3 between a warm water duct 9 and a circulating duct 8, and acid fermentation is carried out while agitating the waste with hydrogen fed from a circulatng blower 11a. A fermented product in the vessel 1b is charged into a hydrogen producing vessel 13 through a duct 5 and brought into contact with a photocatalyst 14. At the same time, sunbeams 17 are irradiated through a light transmitting roof 15 to generate hydrogen. Part of the hydrogen is fed to aerators 16 through a blower 11b. Waste liquor after the reaction is fed to a solid-liq. separation vessel 19 through an outflow path 18, and the separated liq. is discharged from a discharge path 20. The remaining solid is returned to the vessel 13 through a duct 22.
      COPYRIGHT: (C)1984,JPO&Japio
    • 目的:提高与甲烷发酵相比的能量密度和利用率。 通过组织的酸发酵。 在光存在下浪费光催化剂以产生氢。 组成:组织。 将废物从管道4装入酸性发酵容器1b中。在热水管道9和循环管道8之间的热交换器3中进行热交换的温水和酸蒸气保持在30-60℃, 在从循环鼓风机11a供给的氢气搅拌废物的同时进行发酵。 将容器1b中的发酵产物通过导管5装入氢气制造容器13中并与光催化剂14接触。同时,通过透光屋顶15照射阳光17以产生氢。 一部分氢气通过鼓风机11b进入曝气器16。 反应后的废液进料到固体液体中。 分离容器19通过流出路径18和分离的液体。 从排出路径20排出。剩余的固体通过管道22返回到容器13。
    • 55. 发明专利
    • SYSTEM FOR PURIFICATION OF WATER WITH ACTIVE SLUDGE
    • JPS5876189A
    • 1983-05-09
    • JP17387581
    • 1981-10-30
    • OGISHIMA YOSHIZUMIYOSHIDA ETSUROMITSUBISHI ELECTRIC CORP
    • OGISHIMA YOSHIZUMIYOSHIDA ETSUROUHIROTSUJI JIYUNJIMAEDA MITSUONAKAHORI ICHIROUMAEDA KAZUO
    • C02F3/12
    • PURPOSE:To stabilize the quality of purified water, while holding the total amount of sludge in the system at a predetermined value, in purifying sewage or the like, by setting the total amount of sludge at first, and using the set value and an estimated value for the total amount of sludge obtained from information at a specified point to set the amount of excess sludge to be withdrawn. CONSTITUTION:From the output of an MLSS meter 6 inserted into an aerating cell 1, the total amont of sludge is calculated by an arithmetic circuit 7 for the total amount of sludge. On the other hand, an estimated value for the total amount of sludge is calculated by an arithmetic circuit 8 taking into consideration the quality of water to be purified, the property of sludge, the amount of air blow and the amount of excess sludge to the withdrawn. The set value of the total amount of sludge from the arithmetic circuit 8 and the estimated value for the total amount of sludge from the arithmetic circuit 7 are inputted to an arithmetic circuit 9 to determine the amount of excess sludge to be withdrawn. In addition, the outputs of a flow meter 11 for excess sludge and a densitometer 10 for excess sludge are processed by an arithmetic unit 12 to calculate the actual amount of excess sludge to be withdrawn. The output of the arithmetic unit 12 and the output of the arithmetic circuit 9 are inputted to a controller 13 for withdrawing excess sludge, withdrawal is performed by the operation of an excess sludge-withdrawing pump 4, and the total amount of sludge is held constant.