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Conversion regular patterns of acetic acid,propionic acid and butyric acid in UASB reactor 被引量:6
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作者 LIUMin RENNan-qi +2 位作者 CHENYing ZHUWen-fang DINGJie 《Journal of Environmental Sciences》 SCIE EI CAS CSCD 2004年第3期387-391,共5页
On the basis of continuous tests and batch tests, conversion regular patterns of acetate, propionate and butyrate in activated sludge at different heights of the UASB reactor were conducted. Results indicated that the... On the basis of continuous tests and batch tests, conversion regular patterns of acetate, propionate and butyrate in activated sludge at different heights of the UASB reactor were conducted. Results indicated that the conversion capacity of the microbe is decided by the substrate characteristic when sole VFA is used as the only substrate. But when mixed substrates are used,the conversion regulations would have changed accordingly. Relationships of different substrates vary according to their locations. In the whole reactor, propionate's conversion is restrained by acetate and butyrate of high concentration. On the top and at the bottom of the reactor, conversion of acetate, but butyrate, is restrained by propionate. And in the midst, acetate's conversion is accelerated by propionate while that of butyrate is restrained. It is proved, based on the analysis of specific conversion rate, that the space distribution of the microbe is the main factor that affects substrates' conversion. The ethanol type fermentation of the acidogenic phase is the optimal acid type fermentation for the two phase anaerobic process. 展开更多
关键词 conversion regular pattern VFAs specific conversion rate uasb reactor
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Population dynamics on anaerobic sludge granulation in UASB reactors
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《Journal of Environmental Sciences》 SCIE EI CAS CSCD 1993年第3期323-335,共13页
Three UASB reactors were operated to investigate the population dynamics of anaerobic sludge granulation. It is found that the increase of bacterial population relates to the bacterial status in anaerobic food chain a... Three UASB reactors were operated to investigate the population dynamics of anaerobic sludge granulation. It is found that the increase of bacterial population relates to the bacterial status in anaerobic food chain and relates to sludge organic loading rates. In order to form granular sludge, it is necessary to have sufficient amount of different groups of bacteria in the sludge. In our experiment, the population of fermentative bacteria, propionate degraders, butyrate degraders and methanogens is about 107-8, 105-7, 105-7 and 105-7 cells/ml respectively at the appearance of granular sludge. Filamentous methanogenic bacteria are found to be the important species in sludge granulation. Based on the results obtained, a descriptive model is proposed to describe the microbial characteristics of granulation. 展开更多
关键词 uasb reactor granular sludge sludge granulation.
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Application of UASB Reactor in Leachate Treatment of Beijing Asuwei Waste Sanitary Landfill Site 被引量:1
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作者 Du Wei Lu Xufei +4 位作者 Zhang Qingxi Zhu Jiagen Wang Jin’an Zhang Weijun Wang Chengjun 《Meteorological and Environmental Research》 CAS 2017年第1期36-37,41,共3页
The UASB reactor was used to reconstruct leachate treatment project of Beijing Asuwei Waste Sanitary Landfill Site,and the commissioning with the UASB reactor was executed.Water quality indicators were determined in t... The UASB reactor was used to reconstruct leachate treatment project of Beijing Asuwei Waste Sanitary Landfill Site,and the commissioning with the UASB reactor was executed.Water quality indicators were determined in the debugging process,and the results showed that the VFA content in the anaerobic tank was controlled within 600 mg/L,which indicated that the water quality did not have the acidified phenomenon.The COD removal efficiency was 50%approximately and NH_3-N concentration showed as light decline when operation stability in anaerobic system. 展开更多
关键词 WASTE LEACHATE treatment uasb reactor DEBUGGING process COD removal rate China
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Economic Analysis of a Large UASB Reactor Producing Biogas from Baggase Wash Water
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作者 V. K. Jain Surinder S. Sambi +1 位作者 Surendra Kumar   Shashi 《Journal of Sustainable Bioenergy Systems》 2014年第1期68-74,共7页
This paper concerns with the treatment of bagasse wash water, which is generated after washing the stored bagasse before its use in the paper manufacture. The bagasse wash water, treated earlier in open lagoons, is no... This paper concerns with the treatment of bagasse wash water, which is generated after washing the stored bagasse before its use in the paper manufacture. The bagasse wash water, treated earlier in open lagoons, is now treated by the anaerobic process using UASB reactor. This study, based upon an operating unit, shows that the UASB reactor reduces COD of wash water by 85% - 90%, and results in significant emission reductions. Economic analysis carried out by using financial indicators such as DSCR, Payback period and IRR reveals very attractive rate of returns and thus, greatly reduces the risks in financing such projects by the financial institutions. 展开更多
关键词 uasb reactor BAGASSE WASH Water BIOGAS ECONOMIC Analysis
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Biological sulfate removal from acrylic fiber manufacturing wastewater using a two-stage UASB reactor 被引量:11
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作者 Jin Li Jun Wang Zhaokun Luan Zhongguang Ji Lian Yu 《Journal of Environmental Sciences》 SCIE EI CAS CSCD 2012年第2期343-350,共8页
A two-stage UASB reactor was employed to remove sulfate from acrylic fiber manufacturing wastewater.Mesophilic operation(35±0.5℃) was performed with hydraulic retention time(HRT) varied between 28 and 40 hr.... A two-stage UASB reactor was employed to remove sulfate from acrylic fiber manufacturing wastewater.Mesophilic operation(35±0.5℃) was performed with hydraulic retention time(HRT) varied between 28 and 40 hr.Mixed liquor suspended solids(MLSS) in the reactor was maintained about 8000 mg/L.The results indicated that sulfate removal was enhanced with increasing the ratio of COD/SO24-.At low COD/SO42-,the growth of the sulfate-reducing bacteria(SRB) was carbon-limited.The optimal sulfate removal efficiencies were 75% when the HRT was no less than 38 hr.Sulfidogenesis mainly happened in the sulfate-reducing stage,while methanogenesis in the methane-producing stage.Microbes in sulfate-reducing stage performed granulation better than that in methaneproducing stage.Higher extracellular polymeric substances(EPS) content in sulfate-reducing stage helped to adhere and connect the flocculent sludge particles together.SRB accounted for about 31% both in sulfate-reducing stage and methane-producing stage at COD/SO42-ratio of 0.5,while it dropped dramatically from 34% in sulfate-reducing stage to 10% in methane-producing stage corresponding to the COD/SO42-ratio of 4.7.SRB and MPA were predominant in sulfate-reducing stage and methane-producing stage respectively. 展开更多
关键词 a two-stage uasb reactor sulfidogenesis GRANULE fluorescence in situ hybridization(FISH)
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Formation process and properties of hydrogen-producing granular sludge in UASB reactor 被引量:1
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作者 Lili Yin Shuang Liu +3 位作者 Mengyi Wang Wencong Ju Donghui Wei Wenzhe Li 《International Journal of Agricultural and Biological Engineering》 SCIE EI CAS 2018年第5期224-229,共6页
The granular sludge of microbial fermentation systems includes various biomass-degrading enzymes and different microflora,which have significant impacts on the degradation of biomass and the stability of the system.An... The granular sludge of microbial fermentation systems includes various biomass-degrading enzymes and different microflora,which have significant impacts on the degradation of biomass and the stability of the system.An up-flow anaerobic sludge blanket(UASB)reactor was used to grow hydrogen-producing granular sludge.The results showed that the formation of the granular sludge underwent four stages,i.e.,flocculation of the sludge,formation of the flocculent sludge,swelling of the flocculent sludge,and formation of the granular sludge.The formed granular sludge mostly had regular spherical and ellipsoidal shapes with a fractal dimension of 2.08±0.4;the settling velocities were 0.84 cm/s to 1.96 cm/s in water,the porosity was 0.67-0.95.The shear sensitivity(Kss)of the granular sludge was 0.1152.The granular sludge had a culture cycle of approximately 70 d and a hydrogen yield of 1.09 mol H2/mol glucose. 展开更多
关键词 anaerobic fermentation uasb reactor granular sludge HYDROGEN
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Impact of roxarsone on the UASB reactor performance and its degradation 被引量:1
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作者 Mengchuan Shui Feng Ji +4 位作者 Rui Tang Shoujun Yuan Xinmin Zhan Wei Wang Zhenhu Hu 《Frontiers of Environmental Science & Engineering》 SCIE EI CAS CSCD 2016年第6期149-157,共9页
Roxarsone (3-nitro-4-hydroxyphenylarsonic acid, ROX) has been widely used for decades as an organoarsenic feed additive to control intestinal parasites and improve feed efficiency in animal production. However, most... Roxarsone (3-nitro-4-hydroxyphenylarsonic acid, ROX) has been widely used for decades as an organoarsenic feed additive to control intestinal parasites and improve feed efficiency in animal production. However, most of the ROX is excreted into the manure, causing arsenic contamination in wastewater. The arsenic compounds are toxic to microorganisms, but the influence of continuous ROX loading on upflow anaerobic sludge blanket (UASB) reactor is still unknown. In this study, the impact of ROX and its degradation products on the performance of the UASB reactor and the degradation and speciation of ROX in the reactor were investigated. The UASB reactor (hydraulic retention time: 1.75 d) was operated using synthetic wastewater supplemented with ROX for a period of 260 days. With continuous ROX addition at 25.0 mg.L-1, severe inhibition to methanogenic activity occurred after 87 days operation accompanied with an accumulation of volatile fatty acids (VFAs) and a decline in pH. The decrease of added ROX concentration to 13.2 mg.L-1 did not mediate the inhibition. As(III), As (V), MMA(V), DMA(V), HAPA and an unknown arsenic compound were detected in the reactor, and a possible biotransformation pathway of ROX was proposed. Mass balance analysis of arsenic indicated that 60%-70% of the arsenic was discharged into the effluent, and 30%-40% was precipitated in the reactor. The results from this study suggest that we need to pay attention to the stability in the UASB reactors treating organoarsenic-contaminated manure and wastewater, and the effluent and sludge from the reactor tO avoid diffusion of arsenic contamination. 展开更多
关键词 Anaerobic digestion Anaerobic granular sludge (AGS) Arsenic species Impact Roxarsone (ROX) uasb reactor
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UASB和MBR组合工艺处理生活垃圾焚烧发电厂渗滤液的研究
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作者 张灏 《中国资源综合利用》 2024年第2期198-201,共4页
上升式厌氧污泥床(Upward Anaerobic Sludge Bed,UASB)和膜生物反应器(Membrane Bio-Reactor,MBR)是目前较为流行的渗滤液处理技术,其组合工艺可有效处理渗滤液。生活垃圾焚烧发电厂可以综合运用两种技术,提升渗滤液处理能力,降低渗滤... 上升式厌氧污泥床(Upward Anaerobic Sludge Bed,UASB)和膜生物反应器(Membrane Bio-Reactor,MBR)是目前较为流行的渗滤液处理技术,其组合工艺可有效处理渗滤液。生活垃圾焚烧发电厂可以综合运用两种技术,提升渗滤液处理能力,降低渗滤液对环境的危害。本文结合生活垃圾焚烧发电厂渗滤液产生量与设计进出水水质,设计渗滤液处理工艺,确定关键构筑物和设备参数,然后开展应用案例分析,验证渗滤液处理效果。经现场测试,UASB和MBR组合工艺可有效降低渗滤液的氨氮浓度,明显改善出水水质。 展开更多
关键词 上升式厌氧污泥床(uasb) 膜生物反应器(MBR) 组合工艺 生活垃圾焚烧发电厂 渗滤液 处理
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UASB反应器中颗粒污泥的沉降性能与终端沉降速度 被引量:26
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作者 刘永红 贺延龄 +1 位作者 李耀中 杨树成 《环境科学学报》 CAS CSCD 北大核心 2005年第2期176-179,共4页
从流体力学角度,通过建立沉降速度模型探讨了UASB反应器中颗粒污泥的沉降性能与终端沉降速度.计算结果表明,(1)绝大多数颗粒污泥的沉降过程属于过渡区(1<Re<100)而非层流区,其沉降速度与直径成正比,可用Allen公式进行计算;(2)颗... 从流体力学角度,通过建立沉降速度模型探讨了UASB反应器中颗粒污泥的沉降性能与终端沉降速度.计算结果表明,(1)绝大多数颗粒污泥的沉降过程属于过渡区(1<Re<100)而非层流区,其沉降速度与直径成正比,可用Allen公式进行计算;(2)颗粒污泥的终端沉降速度远高于厌氧反应器中废水的上流速度,其良好的沉降性能解决了在高负荷情况下污泥的流失问题.所建模型能较好地反映实际条件下的情况,为厌氧反应器的工艺设计与正常运行提供理论依据. 展开更多
关键词 颗粒污泥 uasb反应器 沉降性能 厌氧反应器 废水 沉降速度 高负荷 沉降过程 正常运行 计算结果
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UASB反应器中影响污泥颗粒化的工程因素 被引量:15
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作者 郭养浩 孟春 +3 位作者 石贤爱 邱宏端 陈剑峰 吴陵 《生物工程学报》 CAS CSCD 北大核心 1997年第1期76-82,共7页
研究了具有不同微生物群系的接种污泥、流动方式和流速对上流式厌氧污泥床(UASB)反应器中活性污泥粒化的影响。颗粒化过程包括:微生物絮凝体的形成、亚核的形成,亚核增长和颗粒成熟四个阶段。微絮凝体的形成取决于酸化菌的作用... 研究了具有不同微生物群系的接种污泥、流动方式和流速对上流式厌氧污泥床(UASB)反应器中活性污泥粒化的影响。颗粒化过程包括:微生物絮凝体的形成、亚核的形成,亚核增长和颗粒成熟四个阶段。微絮凝体的形成取决于酸化菌的作用。流体的动量传递和流体对悬浮物的剪切作用是影响亚核形成的关键性工程因素。为此提出最低流速概念,即形成污泥膨胀床的最低流速。合适的进料速率、污泥负荷。 展开更多
关键词 上流式 厌氧污泥床 反应器 污泥颗粒化 废水处理
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厌氧氨氧化工艺在UASB反应器中的启动运行研究 被引量:35
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作者 左剑恶 杨洋 +1 位作者 蒙爱红 有沈平 《上海环境科学》 CAS CSSCI CSCD 北大核心 2003年第10期665-669,共5页
利用UASB反应器进行了厌氧氨氧化工艺的启动运行研究。以自配高氮低碳废水为进水,普通厌氧污泥为接种污泥,在温度35℃,pH7.5~8.0的条件下连续运行220d,成功实现了厌氧氨氧化工艺的启动,氨氮容积负荷为0.43kg/(m^3·d)时,氨氮的去... 利用UASB反应器进行了厌氧氨氧化工艺的启动运行研究。以自配高氮低碳废水为进水,普通厌氧污泥为接种污泥,在温度35℃,pH7.5~8.0的条件下连续运行220d,成功实现了厌氧氨氧化工艺的启动,氨氮容积负荷为0.43kg/(m^3·d)时,氨氮的去除率最高达88.3%,扫描电镜的观察结果表明,厌氧氨氧化污泥中的细菌以形状不规则的短杆菌为主。 展开更多
关键词 厌氧氨氧化工艺 uasb反应器 温度 污泥 负荷 氨氮 短杆菌 啤酒废水 废水处理
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进水浓度对UASB颗粒污泥形成的影响研究 被引量:10
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作者 竺建荣 夏晓红 +1 位作者 胡纪萃 顾夏声 《环境科学》 EI CAS CSSCI CSCD 北大核心 1992年第6期33-38,共6页
采用人工葡萄糖配水,在相同的操作条件下,研究了进水浓度对UASB反应器颗粒污泥形成的影响。试验结果表明,9000mg/L COD的高浓度进水能够培养出良好的颗粒污泥,颗粒直径1.0—2.5mm(大多为2.0mm),SVI 16.03 ml/g,沉降性能良好.颗粒化过程... 采用人工葡萄糖配水,在相同的操作条件下,研究了进水浓度对UASB反应器颗粒污泥形成的影响。试验结果表明,9000mg/L COD的高浓度进水能够培养出良好的颗粒污泥,颗粒直径1.0—2.5mm(大多为2.0mm),SVI 16.03 ml/g,沉降性能良好.颗粒化过程在二个多月的试验周期内基本完成。反应器容积负荷达30.8kg COD/m^3·d,COD去除率大于85%.而采用1000mg/L COD的低浓度进水,也能培养出颗粒污泥但过程较慢,颗粒直径较小,约0.5—1.5mm,反应器容积负荷最高为10.2kg COD/m^3·d,COD去除率约75%。本文还就处理实际废水时的操作控制技术进行了分析讨论。 展开更多
关键词 反应器 污泥 颗粒化 COD 厌氧处理
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UASB反应器处理酒精废液颗粒污泥形成过程的研究 被引量:19
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作者 陈玉谷 李艳 +2 位作者 王庭放 万秀林 张云昭 《环境科学学报》 CAS CSSCI CSCD 北大核心 1994年第1期113-118,共6页
采用中温(351℃)UASB反应器处理酒精废液,通过启动、运行,成功地培养出了颗粒污泥,取得了良好的处理效果。试验在运行的不同时间对反应器污泥中不同营养类群细菌进行了分类计数;分析了颗粒污泥形成中细菌数量的变化规律;... 采用中温(351℃)UASB反应器处理酒精废液,通过启动、运行,成功地培养出了颗粒污泥,取得了良好的处理效果。试验在运行的不同时间对反应器污泥中不同营养类群细菌进行了分类计数;分析了颗粒污泥形成中细菌数量的变化规律;并通过扫描电镜观察了颗粒污泥的表面情况. 展开更多
关键词 酒精废液 颗粒污泥 uasb反应器
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UASB反应器处理淀粉废水试验研究 被引量:20
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作者 张振家 王太平 +1 位作者 张虹 张扬 《工业水处理》 CAS CSCD 2002年第1期28-30,共3页
利用UASB反应器中温条件下处理高浓度淀粉废水 ,在COD容积负荷保持在 10kg/ (m3 ·d)时 ,COD去除率可达到 90 %以上。试验结果还充分证明 。
关键词 试验研究 uasb反应器 淀粉废水 中温消化 微量元素 废水处理
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厌氧UASB-好氧工艺处理染料废水的研究 被引量:31
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作者 竺建荣 杨艳茹 +1 位作者 安虎仁 钱易 《环境科学》 CAS CSSCI CSCD 北大核心 1994年第4期31-34,共4页
报道厌氧-好氧工艺处理染料废水的试验结果。厌氧段采用UASB反应器,好氧段采用普通活性污泥法。试验结果表明,进水COD1150—1300mg/L、色度500倍的染料废水,在厌氧段停留6—10h,可获得60%以上的CO... 报道厌氧-好氧工艺处理染料废水的试验结果。厌氧段采用UASB反应器,好氧段采用普通活性污泥法。试验结果表明,进水COD1150—1300mg/L、色度500倍的染料废水,在厌氧段停留6—10h,可获得60%以上的COD去除率,色度降到50—100倍。后续曝气6h,总COD去除率可达85%-90%,色度降至20倍左右。进出水的光谱分析揭示,染料废水的脱色主要发生在厌氧段.并且通过生物降解作用来实现。从这些结果得出,UASB-好氧工艺是处理染料废水的一种经济有效的方法。 展开更多
关键词 染料废水 uasb反应器 活性污泥 好氧工艺
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外循环UASB的结构与设计方法 被引量:12
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作者 方战强 陈中豪 +2 位作者 胡勇有 马林 唐一 《工业水处理》 CAS CSCD 2003年第4期72-75,共4页
阐述了外循环升流式厌氧污泥床反应器(UASB)的整体结构和分部结构及其主要作用,以某化工厂的废水处理工程为实例,对各部分的具体参数、设计方法、工艺特点,作了详尽的介绍。用此方法设计建成的外循环UASB反应器在30~35℃时,采用污水处... 阐述了外循环升流式厌氧污泥床反应器(UASB)的整体结构和分部结构及其主要作用,以某化工厂的废水处理工程为实例,对各部分的具体参数、设计方法、工艺特点,作了详尽的介绍。用此方法设计建成的外循环UASB反应器在30~35℃时,采用污水处理厂的消化污泥接种,启动一个多月,在污泥区就形成了1~2mm的颗粒污泥,COD去除率>90%,并可有效分离出直径>5×10-3cm的沼气气泡,证明该设计方法是切实可行的。 展开更多
关键词 外循环uasb 反应器 颗粒污泥 有机容积负荷 污水处理
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UASB启动过程中污泥颗粒化的形成机制 被引量:10
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作者 初里冰 张兴文 +1 位作者 杨凤林 李晓惠 《环境科学与技术》 CAS CSCD 北大核心 2005年第2期22-23,113,共3页
以好氧消化污泥接种启动UASB反应器过程大致分为三个阶段:适应驯化阶段、颗粒污泥的形成阶段和成熟阶段。反应器的容积负荷由0.56 g COD/L/d逐渐增加到4.4 g COD/L/d,溶解性COD的去除率80%。扫描电镜观察培养的颗粒污泥以丝状菌为主。
关键词 uasb反应器 启动 颗粒污泥
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低基质浓度下UASB厌氧氨氧化的脱氮性能及颗粒污泥特性 被引量:7
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作者 王俊敏 王淑莹 +5 位作者 霍明昕 张树军 马斌 甘一萍 杨武 彭永臻 《化工学报》 EI CAS CSCD 北大核心 2011年第10期2914-2919,共6页
采用升流式厌氧污泥床(up-flow anaerobic sludge blanket,UASB)反应器,通过逐步提高进水流量,考察低基质(NH+4-N为16.6 mg.L-1,NO-2-N为19.8 mg.L-1)条件下,厌氧氨氧化(anaerobic ammoniumoxidation,ANAMMOX)反应器的运行性能。实验结... 采用升流式厌氧污泥床(up-flow anaerobic sludge blanket,UASB)反应器,通过逐步提高进水流量,考察低基质(NH+4-N为16.6 mg.L-1,NO-2-N为19.8 mg.L-1)条件下,厌氧氨氧化(anaerobic ammoniumoxidation,ANAMMOX)反应器的运行性能。实验结果表明:在低基质浓度条件下可以实现高效ANAMMOX脱氮并形成颗粒污泥。反应器对NH+4-N和NO-2-N的平均去除率分别为93.3%和94.6%;逐步将UASB反应器的水力停留时间(hydraulic retention time,HRT)由1.26 h缩短至0.14 h,获得的容积氮去除速率为5.73 kgN.m-3.d-1;在此工况下获得的厌氧氨氧化污泥颗粒呈红褐色,粒径分布主要集中在0.5~0.9 mm,平均粒径为0.73 mm。 展开更多
关键词 低基质浓度 ANAMMOX uasb反应器 颗粒污泥
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UASB反应器处理城镇有机垃圾浸出液的研究 被引量:9
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作者 刘国涛 彭绪亚 +2 位作者 袁荣焕 罗伟 周晓臣 《中国给水排水》 CAS CSCD 北大核心 2006年第11期40-44,共5页
采用UASB反应器处理城镇有机垃圾经两相厌氧消化产生的浸出液.在水温为28~35℃时,采用处理城镇有机垃圾的单级厌氧消化反应器的消化污泥进行接种,38 d内便完成了UASB反应器的启动.在运行期间,当进水COD为10 100~11100mg/L、负荷为8.5... 采用UASB反应器处理城镇有机垃圾经两相厌氧消化产生的浸出液.在水温为28~35℃时,采用处理城镇有机垃圾的单级厌氧消化反应器的消化污泥进行接种,38 d内便完成了UASB反应器的启动.在运行期间,当进水COD为10 100~11100mg/L、负荷为8.5~9.5kgCOD/(m^3·d)时,对COD的去除率为88%~95%,出水COD浓度为575~1 609 mg/L;UASB系统运行稳定,具有较强的酸、碱缓冲能力,未出现氨氮与脂肪酸的积累和抑制现象;产气量为0.19~0.44L/gCOD,CH4含量可达75%以上,具有较高的利用价值. 展开更多
关键词 有机垃圾 两相厌氧消化 uasb反应器 垃圾浸出液 产甲烷
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UASB反应器中产甲烷菌对温度胁迫的响应 被引量:10
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作者 张立国 班巧英 李建政 《中国环境科学》 EI CAS CSCD 北大核心 2016年第4期1082-1086,共5页
采用间歇培养方式探讨了升流式厌氧污泥床(UASB)反应器中不同营养类型产甲烷菌对温度胁迫的响应规律.研究结果表明,产甲烷螺旋菌(Methanospirillum)是该反应器的主要氢营养型产甲烷菌,而主要乙酸营养型产甲烷菌为产甲烷丝状菌(Meth... 采用间歇培养方式探讨了升流式厌氧污泥床(UASB)反应器中不同营养类型产甲烷菌对温度胁迫的响应规律.研究结果表明,产甲烷螺旋菌(Methanospirillum)是该反应器的主要氢营养型产甲烷菌,而主要乙酸营养型产甲烷菌为产甲烷丝状菌(Methanosaeta).在35℃条件下,氢营养型和乙酸营养型产甲烷菌的累计甲烷产量分别为24.7,11.7mL,而最大产甲烷速率分别为0.74,0.18m L/h.当温度从35℃分别降低至30,25,20,15℃时,导致氢营养型产甲烷菌的累计产甲烷量分别减少了14.2%,34.0%,47.0%,57.5%,而乙酸营养型产甲烷菌的累计产甲烷量分别减少了5.1%,23.9%,45.3%,95.7%.由此可见,在20~30℃时氢营养型产甲烷菌对温度胁迫更加敏感,而在15℃以下时乙酸营养营养型产甲烷菌对温度胁迫更加敏感. 展开更多
关键词 uasb反应器 产甲烷菌 温度胁迫 产甲烷量
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