Combined Digestion of Landfill Leachate with Septage by an Upflow Anaerobic Sludge Blanket Process

碩士 === 逢甲大學 === 土木及水利工程研究所 === 87 === This study examines the performance and treatment efficiency in digesting landfill leachate with septage . The leachate and septage, both from Taichung City which having a population of 800,000, were combined and treated by anaerobic digestion. Two...

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Main Authors: Feng-Yuan Chang, 張逢源
Other Authors: Chiu-Yue Lin
Format: Others
Language:zh-TW
Published: 1999
Online Access:http://ndltd.ncl.edu.tw/handle/79282899707388677314
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spelling ndltd-TW-087FCU000170472016-02-03T04:32:24Z http://ndltd.ncl.edu.tw/handle/79282899707388677314 Combined Digestion of Landfill Leachate with Septage by an Upflow Anaerobic Sludge Blanket Process 以上流式厭氧污泥床法進行垃圾滲出水與化糞池污泥之合併處理 Feng-Yuan Chang 張逢源 碩士 逢甲大學 土木及水利工程研究所 87 This study examines the performance and treatment efficiency in digesting landfill leachate with septage . The leachate and septage, both from Taichung City which having a population of 800,000, were combined and treated by anaerobic digestion. Two lab-scale UASB reactors ( 13.5 L working volume for each ) were used and operated at 35± 1 ℃. Reactor A treated septage and leachate were mixed at the ratio of 3:1, 2:1 and 1:1 on the basis of total solids COD and in Reactor B septage were treated. The hydraulic retention time was 1.5 days. The feeding solids concentrations were high to 11540~13693 mg/L as total solids. According to experimental results, a successful operation of high-solids UASB system was obtained. The removal efficiencies of reactor B were usually better than reactor A. For reactor A, a higher ratio of septage ( Run 3:1 ) increased the removal efficiencies of total COD, ammonia nitrogen and total phosphorus ( T-P ), volatile solids ( VS ), carbohydrate and proteins. The COD removal reached 50.7% for Reactor A, respectively. The weight of granular sludge accumulation rates were and 11~52 mg VSS/day in the Reactor A and B, respectively. The sludge discharge rates were 0.45~0.75 and 0.31~0.43 L/day for the Reactor A and B, respectively. The granulation rates were 1.4~9.4 and 3.3~5.9μm/day for the granules of Reactor A and B, respectively. The granule sizes of bed sludge were 0.718~0.948 and 0.783~0.846 mm for the Reactor A and B, respectively. Batch test with serum bottles was used to study the effects of heavy metal ions on the VFA degradation and methane production. For Reactor A, the anaerobic biogranule’s acidogenic activities increase by 38 ~ 61%, for each gram of the biomass that comes into contact with 0.09~2.50 mg of Mn, Ni, Zn, Cu and Fe. For Reactor B, the anaerobic biogranule’s acidogenic activities increase by 50~105%, for each gram of the biomass that comes into contact with 0.09~2.48 mg of Mn, Ni, Zn, Cu and Fe . The kinetic parameters of the Reactor A was respectively Vmax 10.85 mg-COD/mg VS-day,Ks 21028 mg-COD/L,Yg 0.1 mg-VS/mg-COD,Kd 0.51 1/day. Chiu-Yue Lin 林秋裕 1999 學位論文 ; thesis 140 zh-TW
collection NDLTD
language zh-TW
format Others
sources NDLTD
description 碩士 === 逢甲大學 === 土木及水利工程研究所 === 87 === This study examines the performance and treatment efficiency in digesting landfill leachate with septage . The leachate and septage, both from Taichung City which having a population of 800,000, were combined and treated by anaerobic digestion. Two lab-scale UASB reactors ( 13.5 L working volume for each ) were used and operated at 35± 1 ℃. Reactor A treated septage and leachate were mixed at the ratio of 3:1, 2:1 and 1:1 on the basis of total solids COD and in Reactor B septage were treated. The hydraulic retention time was 1.5 days. The feeding solids concentrations were high to 11540~13693 mg/L as total solids. According to experimental results, a successful operation of high-solids UASB system was obtained. The removal efficiencies of reactor B were usually better than reactor A. For reactor A, a higher ratio of septage ( Run 3:1 ) increased the removal efficiencies of total COD, ammonia nitrogen and total phosphorus ( T-P ), volatile solids ( VS ), carbohydrate and proteins. The COD removal reached 50.7% for Reactor A, respectively. The weight of granular sludge accumulation rates were and 11~52 mg VSS/day in the Reactor A and B, respectively. The sludge discharge rates were 0.45~0.75 and 0.31~0.43 L/day for the Reactor A and B, respectively. The granulation rates were 1.4~9.4 and 3.3~5.9μm/day for the granules of Reactor A and B, respectively. The granule sizes of bed sludge were 0.718~0.948 and 0.783~0.846 mm for the Reactor A and B, respectively. Batch test with serum bottles was used to study the effects of heavy metal ions on the VFA degradation and methane production. For Reactor A, the anaerobic biogranule’s acidogenic activities increase by 38 ~ 61%, for each gram of the biomass that comes into contact with 0.09~2.50 mg of Mn, Ni, Zn, Cu and Fe. For Reactor B, the anaerobic biogranule’s acidogenic activities increase by 50~105%, for each gram of the biomass that comes into contact with 0.09~2.48 mg of Mn, Ni, Zn, Cu and Fe . The kinetic parameters of the Reactor A was respectively Vmax 10.85 mg-COD/mg VS-day,Ks 21028 mg-COD/L,Yg 0.1 mg-VS/mg-COD,Kd 0.51 1/day.
author2 Chiu-Yue Lin
author_facet Chiu-Yue Lin
Feng-Yuan Chang
張逢源
author Feng-Yuan Chang
張逢源
spellingShingle Feng-Yuan Chang
張逢源
Combined Digestion of Landfill Leachate with Septage by an Upflow Anaerobic Sludge Blanket Process
author_sort Feng-Yuan Chang
title Combined Digestion of Landfill Leachate with Septage by an Upflow Anaerobic Sludge Blanket Process
title_short Combined Digestion of Landfill Leachate with Septage by an Upflow Anaerobic Sludge Blanket Process
title_full Combined Digestion of Landfill Leachate with Septage by an Upflow Anaerobic Sludge Blanket Process
title_fullStr Combined Digestion of Landfill Leachate with Septage by an Upflow Anaerobic Sludge Blanket Process
title_full_unstemmed Combined Digestion of Landfill Leachate with Septage by an Upflow Anaerobic Sludge Blanket Process
title_sort combined digestion of landfill leachate with septage by an upflow anaerobic sludge blanket process
publishDate 1999
url http://ndltd.ncl.edu.tw/handle/79282899707388677314
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