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    • 81. 发明专利
    • Method of controlling the concentration of dissolved oxygen
    • 控制溶解氧的浓度的方法
    • JPS57122789A
    • 1982-07-30
    • JP633281
    • 1981-01-21
    • Hitachi Ltd
    • SHIMIZU NORIOYAMAGUCHI TETSUOSAITOU SETSUOUENO MASAOOTAHARA YOUJI
    • C02F3/12C12M1/36C12N1/00
    • Y02W10/15
    • PURPOSE: In the aerobic cultivation of a microorganism, the oxygen dissolved in the culture mixture is properly controlled through three stage operations, namely the control of the rotation of the stirrer in the first stage, of the oxygen partial pressure of the aeration gas in the second and of the aeration rate in the third.
      CONSTITUTION: A germ seed is charged into the cultivation tank 1 and the substrate is fed from the tank 2 through pump 8 to the tank 1. At this time, signals from the D0 sensor 9, the oxygen partial pressure meter 5 and the aeration rate meter 6 are processed in the control computer 4 and another signal is sent to the oxygen separator 3, the stirrer 2 or the pressure controller 11 in accordance with the control programs to control the stirrer rotation, the oxygen partial pressure in the aeration gas or the aeration rate. Thus, when D0 in the culture mixture is lowered, the rotation of the stirrer is increased as the first stage, when the D0 comes to the upper limit of set value, the oxygen partial pressure in the aeration gas is raised as the second stage, and further, when coming to the next upper limit, the aeration rate is increased as the third stage.
      COPYRIGHT: (C)1982,JPO&Japio
    • 目的:在微生物的好氧培养中,溶解在培养混合物中的氧通过三步操作(即控制第一阶段搅拌器旋转的控制)适当地控制曝气气体的氧分压 第二和曝气率在第三。 构成:将种子种子装入培养槽1中,将基质从罐2通过泵8送入罐1.此时,来自D0传感器9,氧气分压计5和通气量的信号 仪表6在控制计算机4中处理,并且根据控制程序将另一个信号发送到氧气分离器3,搅拌器2或压力控制器11,以控制搅拌器旋转,曝气气体中的氧分压或 曝气率 因此,当培养混合物中的D0降低时,搅拌器的旋转作为第一阶段增加,当D0达到设定值的上限时,曝气气体中的氧分压作为第二阶段升高, 此外,当达到下一个上限时,曝气速率作为第三阶段增加。
    • 84. 发明专利
    • REMOVAL OF CARBON DIOXIDE GAS IN CULTURE BATH
    • JPS5692783A
    • 1981-07-27
    • JP16832479
    • 1979-12-26
    • HITACHI LTD
    • YAMAGUCHI TETSUOSAITOU SETSUOSHIMIZU NORIOUENO MASAOOTAHARA YOUJI
    • C12N1/00
    • PURPOSE:To separate and remove carbon dioxide gas in a culture bath continuously and securely, by blowing a gas into a culture solution, separating mixed fluid of liquid and the gas blended with a remaining gas into liquid and gas, removing carbon dioxide gas, and returning the regenerated culture solution to the culture bath. CONSTITUTION:Sterilized air is continuously blown to the bottom of the foam column 2 equipped on the outside of the culture bath 1, so that the density of a mixed fluid of liquid and a gas in the foam column is made smaller than that of a mixed fluid of liquid and a gas in the culture bath. Consequently, the culture solution enters through the racking pipe 11 to the the foam column 2, and rises in the foam column 2. Carbon dioxide gas in the culture solution transfers to air during the movement of the culture solution. The mixed fluid of liquid and a gas in introduced into the gas separating bath 3, and carbon dioxide is separated and discharged from the exhaust pipe 14 to out of the system. While the culture solution with carbon dioxide removed is returned from the return pipe 15 set at the bottom of the gas separating bath 3 to the interior of the culture bath 1 by the head difference between the inner liquid in the culture bath 1 and the separating bath 3.
    • 86. 发明专利
    • CONCENTRATING DEVICE FOR SLUDGE POLLUTED WITH MICROBE
    • JPS55134618A
    • 1980-10-20
    • JP4092979
    • 1979-04-06
    • HITACHI LTD
    • HAGA RIYOUICHIISHIDA MASAHIKOOTAHARA YOUJI
    • C02F3/08B01D33/17B01D33/21C02F11/12
    • PURPOSE:To concentrate sludge polluted with microbes by a simple mechanism, efficiency and at low cost by a method wherein a porous material with elasticity and a water absorbing property, which has continuous bubbles, is used at a filtration tank. CONSTITUTION:A disc body 1, whose lower portion is immersed in sludge slurry 8 polluted with microbes and which rotates, sucks moisture in the slurry into a filtration layer 2 by means of a capillary phenomenon of the filtration layer 2 during immersion, and concentrated sludge is attached on the surface of the filtration tank 2. The disc body 1 is further revolved, a portion sticking the concentrated sludge is pulled out on the surface of a slurry liquid, moisture is absorbed to the filtration tank 2 from the concentrated sludge during the time when the disc body is turned and moved, and the concentrated sludge is continuously dehydrated. The concentrated sludge dehydrated as mentioned above is scraped off by means of a scraper 4 contacting with the disc body 1, falls and is discharged outside the system by means of the discharge channel 4. The filtration tank 2 after the concentrated sludge is scraped off is compressed by means of a liquid press roll 6, and filtered water is collected to a waste channel 7 and discharged.
    • 87. 发明专利
    • METHOD AND APPARATUS FOR EXHAUST WATER TREATMENT
    • JPS5599393A
    • 1980-07-29
    • JP603879
    • 1979-01-24
    • HITACHI LTDHITACHI METALS LTD
    • ISHIBASHI HITOSHINISHIMURA YUUSAKUOTAHARA YOUJIKUBOTA SHIYOUJI
    • C02F3/34C12R1/01
    • PURPOSE:To improve the nitration and denitrification efficiency, by carrying out sticking growth of microorganism on the surface of solid effectively, at the time of removing nitrogen amount from waste water containing BOD and nitrogen compounds by using nitration fungus and denitrification fungus. CONSTITUTION:The organic waste water 2 containing BOD and nitrogen compounds, is entered the reaction vessel 1 and is passed flowing between anaerobic zone parallel board groups 15b. On this occasion, the above water 2 is entered the gas supply part 6 of the next room after carryig out BOD oxidation reaction and denitrification reaction on the surface of the groups 15b by sticking-grown microorganism. The water 2 is risen with the air bubbles 5a discharged from the part 6 and is overflowed to the next room from the upper tip part of the partition board 14 taking in oxygen and then, is passed through the aerobic zone parallel board groups 15a. On this occasion, pH of the water is measured by the pH sensor 18 and pH is regulated at 7.5-8.5 by supplying neutralizing agent from the supply opening 21. The above water is joined to the exhaust water at the exhaust water supply part 3 again after carrying out nitration reaction on the surface of the parallel boards by sticking-grown microorganism. The treating water 13 is discharged through the settling separation vessel 16.