发明名称 |
SOLID-LIQUID SEPARATION METHOD IN METHANE FERMENTATION TREATMENT OF WASTE WATER |
摘要 |
<p>PURPOSE:To prevent a lowering of filtering capacity due to clogging and to secure stable membrane permeating flow velocity by setting the pore size and filtering pressure of an inorg. filter membrane used in a method for the methane fermentation of waste water to specific ranges. CONSTITUTION:The inorg. particles composed of aluminum oxide or silicon oxide used in the solid-liquid separation of the liquid after the methane fermentation treatment of waste water are sintered to prepare a filter membrane having a pore size of 0.05-0.2mum. Further, filtering pressure is set to 0.1-1kgf/cm<2>. Since this inorg. filter membrane perfectly hold anaerobic bacteria such as methane bacteria, a lowering of the filtering capacity of the filter membrane due to the clogging of the filter membrane with a particle component is prevented. Since this filter membrane has a fine pore size increasing permeation flow velocity under low pressure, energy consumption is reduced and stable membrane permeation flow velocity is secured.</p> |
申请公布号 |
JPH0275395(A) |
申请公布日期 |
1990.03.15 |
申请号 |
JP19880227956 |
申请日期 |
1988.09.12 |
申请人 |
AGENCY OF IND SCIENCE & TECHNOL |
发明人 |
YAZAWA TETSUO;TANAKA HIROSHI;EGUCHI KIYOHISA;HAKUBUN EISUKE;TOYA YUKIO;SHIMIZU YASUTOSHI;MUTSUSHIRO MINORU |
分类号 |
C02F1/44;C02F3/28;C02F11/04 |
主分类号 |
C02F1/44 |
代理机构 |
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代理人 |
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主权项 |
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地址 |
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