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    • 95. 发明专利
    • ANAEROBIC DIGESTION TREATMENT APPARATUS
    • JPS60147298A
    • 1985-08-03
    • JP521884
    • 1984-01-12
    • MITSUBISHI ELECTRIC CORP
    • MAEDA MITSUOHORIUCHI KOUICHI
    • C02F11/04
    • PURPOSE:To enhance a digestion treatment speed without reducing a charging load amount, by providing a microorganism recovery apparatus and a microorganism return means for returning microbial cells recovered by said microorganism recovery apparatus to a digestion tank. CONSTITUTION:Sludge separated in a separation tank 4 is sent to the sludge chamber of a microorganism recovery appartus 10 through an extraction path 14a. The taxis inducing substance of a microbial cell is sent to the recovered cell chamber 13 of the microorganism recovery apparatus 10 through a feed path 14b to induce the transmission of the microbial cell through a cell permeable separation membrane while the microbial cell in a sludge chamber 12 is separated into the recovered cell chamber 13 through the cell permeable separation membrane 11. The microbial cell separated into the recovered cell chaber 13 is returned to a digestion tank 1 by a return path 8f and the residual sludge is discharged through a discharge path 8g. Furthermore, as the material of the cell permeable separation membrane 11, a porous polymer membrane, a porous ceramic membrane or a porous glas membrane are used.
    • 96. 发明专利
    • Sludge digestion device
    • SLUDGE DIGESTION DEVICE
    • JPS58223499A
    • 1983-12-26
    • JP10497382
    • 1982-06-18
    • Mitsubishi Electric CorpSorao ObaraYoshizumi OgishimaEtsuro Yoshida
    • OGISHIMA YOSHIZUMIYOSHIDA ETSUROUOBARA SORAOMAEDA MITSUOYOTSUMOTO HATSUOTANAKA HISAO
    • C02F1/24C02F11/04
    • Y02E50/343
    • PURPOSE: To prevent the hindrance of the activity of anaerobes and to reduce the size of a titled device, by using the digester gas generated from a digestion tank as a gas for floating in a sludge concentrating device of a sludge digestion device consisting of the sludge concentrating device and the digestion tank.
      CONSTITUTION: Raw sludge is introduced by a pump 15a through an introducing pipeline 5 into a floatation tank 17. On the other hand, the pressurized water dissolved under pressure with the digester gas pressurized with a compressor 28 in a pressurization tank 23 is introduced through an introducing pipeline 24 into the tank 17, where the pressure is released therefrom to develop fine foam. The foam sticks on the raw sludge and concentrates and floats the sludge. The floating sludge is put with a skimmer 21 into a storage chamber 20 for concn. sludge, from which the sludge is discharged by a pump 15b into a digestion tank 12. The liquid separated by flotation is discharged through a pipeline 7 and the waste gas is released with a blower 27 from a gas release pipeline 26 connected to a top plate 22.
      COPYRIGHT: (C)1983,JPO&Japio
    • 目的:为了防止厌氧菌的活性受阻和减小标题装置的尺寸,通过使用由消化槽产生的蒸煮器气体作为漂浮在由污泥组成的污泥消化装置的污泥浓缩装置中的气体 浓缩装置和消化罐。 构成:原料污泥由泵15a通过导入管道5引入浮选槽17.另一方面,在加压槽23中用压缩机28加压的蒸煮器气体在压力下溶解的加压水通过 将管道24引入槽17中,在该槽17中释放压力以形成细小的泡沫。 泡沫粘在原污泥上,浓缩并漂浮污泥。 浮选污泥用撇渣器21放入储存室20中。 污泥通过泵15b排放到消化罐12中。通过浮选分离的液体通过管道7排出,废气由鼓风机27从连接到顶板的气体释放管道26释放 22。
    • 97. 发明专利
    • Method for monitoring and controlling dissolved oxygen in aeration tank
    • 监测和控制气罐中溶解氧的方法
    • JPS58219994A
    • 1983-12-21
    • JP10365182
    • 1982-06-14
    • Mitsubishi Electric Corp
    • MAEDA MITSUOHIROTSUJI JIYUNJINAKAHORI ICHIROUTONEGAWA HISASHI
    • C02F3/12
    • Y02W10/15
    • PURPOSE: To control and monitor dissolved oxygen in an aeration tank so as to make the level thereof constant, by operating and estimating dissolved oxygen at the water sampling point in the aeration tank from the activated sludge concn. measured value, the dissolved oxygen concn. measured value and a water sampling amount measured value of a liquid to be measured.
      CONSTITUTION: Liquids to be measured of each circuits 1aW1c in an aeration tank 1 are successively introduced into a water receiving tank 16 by the actions of a sampling pump 15 and valves 17aW17c successively operated on the basis of the indication of a operation panel 19. In the next step, automatic measurement is carried out by a dissolved oxygen metar 10 and an activated sludge densitometer 11 and respective measured values are inputted to an operator 12. A water sampling amount and a constant are respectively inputted to the operator 12 from a water sampling flowmeter 20 and a constant setting device 13c. The operator 12 operates dissolved oxygen at the water sampling points from these input values. The result of this operation is operates an air sending amount control valve 4 through an indication controller 14a to control dissolved oxygen to a constant level.
      COPYRIGHT: (C)1983,JPO&Japio
    • 目的:控制和监测曝气池中的溶解氧,以使其水平恒定,通过在活性污泥浓缩池中对曝气池中取水点的溶解氧进行操作和估算。 测量值,溶解氧浓度。 测量值和待测液体的水采样量测量值。 构成:曝气池1中的每个回路1a-1c的待测量液体通过取样泵15和阀17a-17c的动作被依次引入到接收容器16中,阀17a-17c基于操作指示 在下一步骤中,通过溶解氧元10和活性污泥密度计11进行自动测量,并将相应的测量值输入到操作者12.水采样量和常数分别输入到操作者12 来自取水流量计20和恒定设定装置13c。 操作者12从这些输入值在水采样点操作溶解氧。 该操作的结果通过指示控制器14a操作送风量控制阀4以将溶解氧控制到恒定水平。
    • 98. 发明专利
    • Apparatus for intermittent feeding of ozone
    • 臭氧的间歇进料装置
    • JPS58213602A
    • 1983-12-12
    • JP9652782
    • 1982-06-04
    • Mitsubishi Electric Corp
    • NAKAYAMA SHIGEKIMAEDA MITSUOUSUI AKIRASASAKI TOSHIHIKO
    • B01D53/04C01B13/10C02F1/78
    • PURPOSE: To enable the uniform desorption of ozone with time and the stable distribution of ozone, by carrying out the vacuum desorption intermittently during the desorption period, and raising the temperature of the ozone adsorbent in the adsorption column to a specific level during the interruption period of the vacuum desorpiton.
      CONSTITUTION: Oxygen is supplied from the oxygen source 2 constantly at a specific pressure to the circulation system consisting of the circulation blower 3, the ozonizer 1, and the ozone adsorption column 4, and the generated ozone is adsorbed to the adsorbent in the column 4 cooled by the cooling source 5. When the amount of adsorbed ozone reaches the saturation level of the adsorbent, the operation is changed to the desorption stage. The change-over valves 8-1, 8-2, 8-3 and 8-4 are closed, the change- over valve 8-7 is opened, and the water jet ejector 7 is operated to such the ozone from the column and produce concentrated ozonized water. When the pressure in the column 4 is decreased by the progress of desorption, the valve 8-7 is closed by the signal of the pressure sensor 9, and the valves 8-5 and 8-6 are opened to heat the adsorbent by the heat source 6. When the inner pressure of the column reaches a specific level, the valve 8-7 is opened again by the signal of the sensor 9. The above operations are repeated.
      COPYRIGHT: (C)1983,JPO&Japio
    • 目的:通过在解吸期间间歇地进行真空脱附,能够使臭氧随时间的均匀解吸和臭氧的稳定分布,并使吸附塔内的臭氧吸附剂的温度在中断期间提高到一个特定的水平 的真空解体。 构成:氧气从氧气源2以一定的压力恒定地供给由循环鼓风机3,臭氧发生器1和臭氧吸附塔4构成的循环系统,所产生的臭氧被吸附在塔4中的吸附剂上 冷却源5冷却。当臭氧吸附量达到吸附剂的饱和水平时,操作变为解吸阶段。 转换阀8-1,8-2,8-3和8-4关闭,转换阀8-7打开,喷水喷射器7对来自塔的臭氧进行操作, 产生浓缩的臭氧水。 当柱4中的压力随着解吸的进行而降低时,阀8-7被压力传感器9的信号封闭,阀8-5和8-6被打开以通过热量加热吸附剂 当列的内部压力达到特定水平时,阀8-7再次被传感器9的信号打开。重复上述操作。