• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    1325324 Sewage treatment UNION CARBIDE CORP 1 July 1970 [2 July 1969] 31858/70 Heading C1C Water having a BOD is treated by mixing with a biomass and feed gas comprising at least 50% oxygen (by volume) simultaneously continuously recirculating one of such fluids against the other fluid forms in a first gaseous oxygenation stage to form first oxygenated liquidsolid and first unconsumed oxygen-containing gas comprising at least 35% oxygen; discharging said first unconsumed oxygen-containing gas from the first stage and mixing the discharged gas with liquid-solid simultaneously continuously recirculating one of such fluids against the other fluids in at least one further gaseous oxygenation stage to form at least a second oxygenated liquid-solid and second unconsumed oxygen-containing gas of lower oxygen purity and content than the first gas, and discharging the second gas from the second stage; and regulating the flow of oxygen-containing gas and/or liquid-solid and regulating the mixing and gas-liquid contact energy input to the first and all succeeding gaseous oxygen stages such that: (a) at least 60% (by volume) of the oxygen in said feed gas is consumed in the liquid-solid of all stages, (b) between 0À04 and 0À24 kg.- moles per hour of oxygen are introduced to the first stage per one kilowatt of mixing and gasliquid contact energy used in all stages, and (c) the gas discharged from the final gaseous oxygenation stage wherein unconsumed oxygen gas from the preceding stage has been contacted with aqueous liquid-solid, comprises more than 21% and less than 80% oxygen.
    公开号:SU988185A3
    申请号:SU701450902
    申请日:1970-07-01
    公开日:1983-01-07
    发明作者:Рубен Мс Уиртер Джон
    申请人:Юнион Карбид Корпорейшн (Фирма)；
    IPC主号:
    专利说明:

    3988
    : the oxidizable substances are maximally at the first stage and gradually decrease as the gaseous oxygen flows through the stages. The gas, which has the maximum degree of oxygen purity, is in contact with the waste water in the first stage, and according to what the maximum transfer rate of oxygen takes place here, is capable of ensuring a high oxygen demand at this stage. The total contact time, providing a significant degree of sludge recovery, is less than 180 minutes. This time is satisfactory for municipal wastewater containing approximately 300 ppm of biochemically oxidizable substances. For wastewater with a higher content of biochemically oxidizable substances, a longer contact time is required to obtain a relatively clean liquid stream. Dissolved oxygen is quickly consumed by the biomass in the first stage, so that its content can be significant.
    The content of biochemically oxidizable substances in the source water (MIC), g / million
    MIC of purified water Degree of purification by BOD,% Recycled sludge, g / million
    The content of dissolved oxygen in stages, g / million:
    first second third
    Analysis of the oxidation gas in stages,%:
    first second third
    Total kW energy consumption
    权利要求:
    Claims (2)
    [1]
    1. Zhukov A.I. and others. Sewer industrial enterprises. N., State Publishing House of Literature on Construction,. "Architecture and Building Materials." 1962,
    with. 256-257.
    [2]
    2.Water supply and sewage. Issue 2, 1963, p. 128-129.
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    同族专利:
    公开号 | 公开日
    MY7700097A|1977-12-31|
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    PL80965B1|1975-08-30|
    FI54463C|1978-12-11|
    RO59586A|1976-04-15|
    BE752083A|1970-12-16|
    DK131561B|1975-08-04|
    DE2032480C3|1979-08-16|
    SE376901B|1975-06-16|
    BR7020198D0|1973-02-13|
    NO128271B|1973-10-22|
    HK74276A|1976-12-03|
    DK131561C|1976-01-05|
    CH533576A|1973-02-15|
    IL34836A|1981-10-30|
    DE2032480B2|1973-06-07|
    AR192861A1|1973-03-21|
    ES409647A1|1976-01-01|
    NL7009741A|1971-01-05|
    CS156475B2|1974-07-24|
    ZA704500B|1971-11-24|
    CH540857A|1973-10-15|
    US3547815A|1970-12-15|
    IL34836D0|1970-09-17|
    NL160791B|1979-07-16|
    JPS4919584B1|1974-05-18|
    HU168462B|1976-04-28|
    YU246178A|1982-06-30|
    FI54463B|1978-08-31|
    GB1325324A|1973-08-01|
    NL160791C|1979-12-17|
    ES381328A1|1973-04-16|
    FR2054078A5|1971-04-16|
    YU165770A|1982-02-28|
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    引用文献:
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    US3963609A|1973-04-02|1976-06-15|Union Carbide Corporation|Integral circular wastewater treatment process|
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    US3915854A|1973-04-16|1975-10-28|Wilbur N Torpey|Wastewater treatment|
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    US4080287A|1976-10-20|1978-03-21|Union Carbide Corporation|Activated carbon treatment of oxygenated wastewater|
    DE2800035C2|1978-01-02|1985-06-13|Passavant-Werke AG & Co KG, 6209 Aarbergen|Process and device for wastewater purification|
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    US4206047A|1978-07-13|1980-06-03|Houdaille Industries, Inc.|Multi-stage systems for waste water oxidation|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    US83850069A| true| 1969-07-02|1969-07-02|
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