Reaction Kinetics of Membrane Separation Anaerobic Digestion
Reaction Kinetics of Membrane Separation Anaerobic Digestion
批准号:
04650500
负责人:
AYA Hidenori
金额:
$1.28万
依托单位国家:
日本
项目类别:
Grant-in-Aid for General Scientific Research (C)
财政年份:
1992
资助国家:
日本
项目状态:
已结题
起止时间:
1992 至 1994
中文摘要
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英文摘要
Membrane separation anaerobic digestion is a process that consists of a complete mixing digester and membrane separation units that separates mixed liqueur to permeate and concentrate. The former one is discharged and the later is returned to the digester. The combined process is a kind of immobilized bioreactor that holds all of biomass and undigested solid. Treated permeate contains COD of less than 500 mg/L.There is not any organic solid accumulation nor inorganic solid that is liquefied and passes through membrane. Experiments were conducted by semi-batch reactors of which volume was 20L at 35゚C to determine reaction kinetics of real sewage sludge digestion. After feeding substrate, small amount of permeate was withdrawn through membrane at proper interval. VFA concentration of each sample was measured by gas chromatogram. Reaction velocity of VFA was estimated by using pure VFA solution as substrate. Employing those parameters obtained, a reaction model of the process was produced. Disintegration of VFA was estimated to follow first order reaction. Hydrolysis of organic solid in sewage sludge was also first order reaction on the condition that velocity of acidification was not a limiting factor. When first order reaction of biomass autolysis was introduced, change of VFA concentration in the permeate fitted well to the reaction model. Disintegrated biomass seemed to be used as substrate by the proposed model and observed stable concentration ratio of inorganic substance. To confirm this fact, digested sludge was stabilized by high temperature and was fed to the digesters. Gas production was observed, but amount of it was smaller than that of flesh sludge. The experiment indicated a new process of complete disintegration of sewage sludge.
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斉藤雄一郎: "下水汚泥の膜分離嫌気性消化〜基質投与後のVFA経時変化" 土木学会第48回年次学術講演会概要集. 2. 1336-1337 (1993)
Yuichiro Saito:“污水污泥的膜分离厌氧消化 - 底物施用后 VFA 的时间过程”日本土木工程师学会第 48 届年度学术会议摘要 2. 1336-1337 (1993)。
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綾,日出教: "下水汚泥の膜分離嫌気性消化、 基質投与後のVFA濃度経時変化" 土木学会第48回年次学術講演会概要集第2部. 1336-1337 (1993)
Aya, Hideyoshi:“污水污泥的膜分离厌氧消化和底物施用后 VFA 浓度的时间变化” 日本土木工程学会第 48 届年度学术会议摘要,第 2 部分。 1336-1337 (1993)
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斉藤 雄一郎: "下水汚泥の膜分離嫌気性消化〜基質投与後のVFA経時変化" 土木学会第48回年次学術講演会概要集. 2. 1336-1337 (1993)
Yuichiro Saito:“污水污泥的膜分离厌氧消化 - 底物施用后 VFA 的时间过程”日本土木工程师学会第 48 届年度学术会议摘要 2. 1336-1337 (1993)。
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綾,日出教: "Applications of Membrane Separation Activated Sludge Process(MAS)" Second Japan and Holland Work Shop on Water Environment.1-6 (1993)
Aya, Hidekyori:“膜分离活性污泥法(MAS)的应用”第二届日本和荷兰水环境研讨会.1-6(1993)
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土木学会第47回年次学術講演会概要集. 2. 898-899 (1992)
日本土木工程学会第 47 届年会学术会议摘要 2. 898-899 (1992)
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共 15 条
Numerical Simulation of Horizontal Sedimentation Tanks
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批准号:10650545
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项目类别:Grant-in-Aid for Scientific Research (C)
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资助金额:$1.22万
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财政年份:1998
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负责人:AYA Hidenori
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依托单位:
Water Treatment by Submerged Membrane Separation in Sedimentation Tank with Powdered Activated Carbon Dosage
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批准号:07650644
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项目类别:Grant-in-Aid for Scientific Research (C)
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资助金额:$1.34万
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财政年份:1995
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负责人:AYA Hidenori
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依托单位:
Two Phase Anaerobic Digestion in Membrane Separated Bio-Reactor
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批准号:63550400
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项目类别:Grant-in-Aid for General Scientific Research (C)
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资助金额:$1.02万
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财政年份:1988
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负责人:AYA Hidenori
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依托单位:
海外基金