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Combined process of sequencing batch reactor activated sludge process and constructed wetland for domestic wastewater treatment
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作者 魏武强 Wisaam S. Al-Rekabi 《Journal of Chongqing University》 CAS 2010年第4期201-207,共7页
By combining sequencing batch reactor (SBR) activated sludge process and constructed wetland (CW), this study is to achieve the domestic wastewater treatment. Our purpose was to determine the optimum operating paramet... By combining sequencing batch reactor (SBR) activated sludge process and constructed wetland (CW), this study is to achieve the domestic wastewater treatment. Our purpose was to determine the optimum operating parameters of the combined process. The process involved advantages and shortages of SBR and CW. Under normal temperature, the 3rd cycle (SBR’s operation cycle is 8 h: inflow for 1 h, limited aeration for 3 h, sediment for 1 h, outflow for 1 h, and idling for 2 h; CW’s hydraulic retention time (HRT) is 24.8 h and hydraulic loading is 24.5 m3/m2 d) was the best cyclic mode. The effluents can meet the standard GB/T18921-2002: "The reuse of urban recycling water: water quality standard for scenic environment use". In the 3rd cycle, the efficiency of CW was the maximum, and energy consumption of SBR was the minimum. Under the condition of low dissolved oxygen, the removing efficiency of chemical oxygen demand (COD) and ammonia was not affected obviously. Simultaneously, nitrification and denitrification phenomena occured and phosphorus was absorbed obviously. 展开更多
关键词 sequencing batch reactor activated sludge process constructed wetland energy consumption low dissolved oxygen
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Mechanism of scaling on oxidation reactor wall in TiO_2 synthesis by chloride process
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作者 周峨 袁章福 +2 位作者 王志 范先国 龚家竹 《中国有色金属学会会刊:英文版》 EI CSCD 2006年第2期426-431,共6页
The mechanism of scaling on the oxidation reactor wall in TiO2 synthesis process was investigated. The formation of wall scale is mostly due to being deposited and sintered of TiO2 particle formed in the gas phase rea... The mechanism of scaling on the oxidation reactor wall in TiO2 synthesis process was investigated. The formation of wall scale is mostly due to being deposited and sintered of TiO2 particle formed in the gas phase reaction of TiCl4 with O2. The gas-phase oxidation of TiCl4 was in a high temperature tubular flow reactor with quartz and ceramic rods put in center respectively. Scale layers are formed on reactor wall and two rods. Morphology and phase composition of them were characterized by transmission electron microscope(TEM), scan electron micrographs(SEM) and X-ray diffraction(XRD). The state of reactor wall has a little effect on scaling formation. With uneven temperature distribution along axial of reactor, the higher the reaction temperature is,the thicker the scale layer and the more compact the scale structure is. 展开更多
关键词 氯化法 二氧化钛 反应堆 氧化
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聚酯降膜增黏反应过程模拟
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作者 陈世昌 曹峻华 陈文兴 《纺织学报》 北大核心 2025年第1期16-24,共9页
为促进对降膜熔融缩聚制备高分子量聚对苯二甲酸乙二醇酯(PET)增黏反应过程的理论认识,指导降膜反应器的设计与缩聚工艺优化,建立了降膜反应器串联五釜的连续聚合过程数学模型,以与工业生产数据匹配的五釜流程模拟结果为降膜反应釜入口... 为促进对降膜熔融缩聚制备高分子量聚对苯二甲酸乙二醇酯(PET)增黏反应过程的理论认识,指导降膜反应器的设计与缩聚工艺优化,建立了降膜反应器串联五釜的连续聚合过程数学模型,以与工业生产数据匹配的五釜流程模拟结果为降膜反应釜入口物料参数,考察了PET分子量与端基量等品质指标随降膜增黏反应进程的变化,讨论了降膜反应器内温度和压力对聚合产物分子量与端基量的影响规律。结果表明:随着增黏反应的进行,可顺利得到特性黏度为1.0 dL/g以上、端羧基量为16 mmol/kg的产品;所建立的降膜反应器模型能够对增黏效果进行灵敏分析,高温低压有利于提升增黏反应效率,但过低的压力导致高黏熔体变得难处理和转移,且会增加设备成本和提高工艺精确控制的难度,温度过高则会显著增加副产物的生成;对降膜反应器选择压力为0.1 kPa左右、温度区间为285~290℃进行工艺参数调优,采用优化后的连续生产工艺流程最终反应器出口PET的分子量在39000 g/mol左右;模拟结果与工业生产值吻合,可运用于分析降膜增黏反应技术应用实践。 展开更多
关键词 聚酯 液相增黏 反应器 缩聚 过程模拟 缩聚工艺
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Co_(3)S_(4)/PES催化膜反应器氧化降解水中罗丹明B
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作者 肖泽仪 孟佳欣 +2 位作者 樊森清 陈渝 陈皎皎 《工程科学与技术》 北大核心 2025年第1期225-233,共9页
基于过硫酸氢钾(PMS)的非均相高级氧化工艺(AOPs)在实际应用中一直受到PMS活化效率与活性氧物种(ROS)利用率低下的限制。本文以ZIF-67为前驱体、聚醚砜(PES)多孔膜为基底,采用金属有机框架(MOFs)模板配体交换策略,流动合成构建了Co_(3)S... 基于过硫酸氢钾(PMS)的非均相高级氧化工艺(AOPs)在实际应用中一直受到PMS活化效率与活性氧物种(ROS)利用率低下的限制。本文以ZIF-67为前驱体、聚醚砜(PES)多孔膜为基底,采用金属有机框架(MOFs)模板配体交换策略,流动合成构建了Co_(3)S_(4)/PES催化膜反应器(CMR)。通过场发射电子显微镜(FESEM)、X射线衍射(XRD)等方法对催化膜进行了表征。结果显示,平均粒径为23 nm的Co_(3)S_(4)纳米颗粒被原位合成固载在PES膜孔中,负载量为15.9%,并沿膜厚度方向均匀分布。以活化PMS降解典型芳香族有机化合物罗丹明B(RhB)为例,研究了该催化膜的催化性能及反应机理。实验结果表明,浓度为20 mg/L的RhB溶液,在初始溶液pH为7、温度为25℃以及膜通量为0.80 mL/(min·cm^(-2))(对应于停留时间0.68 s)的条件下,Co_(3)S_(4)/PES催化膜具有90%以上的降解率,表观反应速率常数为97.83 min^(-1),转化频率达到了489.15 L/(min·g^(-1)),均高出Co_(3)S_(4)粉末传统悬浮间歇处理模式两个数量级,并且Co_(3)S_(4)/PES催化膜能够保持良好的稳定性。膜孔道的分散性有效防止了Co_(3)S_(4)纳米颗粒的聚集,过膜流动反应限域在微纳尺度的膜孔道内,强化了反应物与催化剂之间的质量传递与接触,加快了PMS的活化,从而实现了单线态氧(^(1)O_(2))的高效生成,并在RhB的快速降解中起主导作用。 展开更多
关键词 催化膜反应器 高级氧化 罗丹明B 过硫酸氢钾 流动反应 ZIF-67 Co_(3)S_(4)
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基于低浓铀燃料医用同位素试验堆的^(99)Mo分离工艺研究
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作者 王海军 孙志中 +5 位作者 耿自胜 罗柯宇 邓雨 陈云明 罗宁 张劲松 《同位素》 2025年第1期22-29,共8页
医用同位素试验堆是以硝酸铀酰溶液为燃料,生产^(99)Mo具有一定优势,已成为医用同位素生产的重要方法。低浓铀燃料是研究堆发展的趋势,在低浓铀条件下医用同位素试验堆的^(99)Mo分离工艺至关重要。本研究主要对低浓铀燃料的医用同位素... 医用同位素试验堆是以硝酸铀酰溶液为燃料,生产^(99)Mo具有一定优势,已成为医用同位素生产的重要方法。低浓铀燃料是研究堆发展的趋势,在低浓铀条件下医用同位素试验堆的^(99)Mo分离工艺至关重要。本研究主要对低浓铀燃料的医用同位素试验堆^(99)Mo分离进行深入研究,结果显示,联合使用球形氧化铝柱、α-安息香肟柱和活性炭柱工艺,能够实现^(99)Mo提取、分离和纯化。此外,使用该工艺在低浓铀模拟燃料溶液中对Mo的分离效果进行验证,得到Mo回收率为75.7%,杂质也满足要求。该工艺不仅提高了医用同位素试验堆在低浓铀燃料条件下^(99)Mo的产率,更为医用同位素试验堆的低浓化奠定了基础,具有较大的应用价值。 展开更多
关键词 ^(99)Mo 医用同位素试验堆 ^(99)Mo分离工艺 球形氧化铝 α-安息香肟
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Balanced multiple weighted linear discriminant analysis and its application to visual process monitoring 被引量:1
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作者 Weipeng Lu Xuefeng Yan 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2021年第8期128-137,共10页
Visual process monitoring is important in complex chemical processes.To address the high state separation of industrial data,we propose a new criterion for feature extraction called balanced multiple weighted linear d... Visual process monitoring is important in complex chemical processes.To address the high state separation of industrial data,we propose a new criterion for feature extraction called balanced multiple weighted linear discriminant analysis(BMWLDA).Then,we combine BMWLDA with self-organizing map(SOM)for visual monitoring of industrial operation processes.BMWLDA can extract the discriminative feature vectors from the original industrial data and maximally separate industrial operation states in the space spanned by these discriminative feature vectors.When the discriminative feature vectors are used as the input to SOM,the training result of SOM can differentiate industrial operation states clearly.This function improves the performance of visual monitoring.Continuous stirred tank reactor is used to verify that the class separation performance of BMWLDA is more effective than that of traditional linear discriminant analysis,approximate pairwise accuracy criterion,max–min distance analysis,maximum margin criterion,and local Fisher discriminant analysis.In addition,the method that combines BMWLDA with SOM can effectively perform visual process monitoring in real time. 展开更多
关键词 Linear discriminant analysis process monitoring Self-organizing map Feature extraction Continuous stirred tank reactor process
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液体脂肪酶催化制备甘油二酯油连续化工艺研究
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作者 王建芳 李昕 张蕊 《中国油脂》 北大核心 2025年第1期43-47,共5页
旨在强化酶催化大豆油的甘油解反应为甘油二酯油的工业化生产提供技术支持,以大豆油和甘油为原料,液体脂肪酶为催化剂,利用微通道反应器制备甘油二酯油。通过单因素实验考察了液体脂肪酶用量、大豆油与甘油质量比、反应温度、反应时间... 旨在强化酶催化大豆油的甘油解反应为甘油二酯油的工业化生产提供技术支持,以大豆油和甘油为原料,液体脂肪酶为催化剂,利用微通道反应器制备甘油二酯油。通过单因素实验考察了液体脂肪酶用量、大豆油与甘油质量比、反应温度、反应时间对反应粗产物中甘油二酯质量分数的影响,设计中试放大实验考察工艺的稳定性,并采用分子蒸馏对中试粗产物进行纯化。结果表明:甘油二酯油制备的最佳工艺条件为液体脂肪酶(10 000 U/mL)用量3%(以大豆油质量计)、大豆油与甘油质量比10∶1、反应温度50℃、反应时间9.0 s,在此条件下粗产物中甘油二酯的质量分数达44%;经中试实验放大后,粗产物中各组分(游离脂肪酸、单甘酯、甘油二酯和甘油三酯)的质量分数无明显变化,甘油二酯的质量分数为42%,反应可在微通道反应器中连续进行;经分子蒸馏纯化后,产物中甘油二酯的质量分数达到48%。综上,通过微通道反应器可以实现液体脂肪酶催化大豆油甘油解制备甘油二酯油的连续化生产,且该方法稳定性较好。 展开更多
关键词 甘油二酯油 脂肪酶 微通道反应器 工艺优化
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基于Aspen的丙烯腈聚合反应釜性能优化研究
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作者 曹晓磊 陈晔 《化工机械》 2025年第1期107-114,共8页
在丙烯腈自由基聚合工艺流程中,丙烯腈聚合釜对聚丙烯腈的品质具有重要影响,以通用丙烯腈工艺流程为基础,优化聚合反应模型,比较了单釜聚合和多釜串联聚合的性能差异。利用Aspen化工分析软件,结合实际的工程数据,分析了不同工艺流程下... 在丙烯腈自由基聚合工艺流程中,丙烯腈聚合釜对聚丙烯腈的品质具有重要影响,以通用丙烯腈工艺流程为基础,优化聚合反应模型,比较了单釜聚合和多釜串联聚合的性能差异。利用Aspen化工分析软件,结合实际的工程数据,分析了不同工艺流程下的影响因素。结果表明,多釜串联聚合能够有效提高聚丙烯腈的品质和产量。 展开更多
关键词 聚合反应釜 丙烯腈 多釜串联 工艺参数优化 Aspen软件
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新型波纹翅片金属氢化物反应器的放氢性能有限元分析
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作者 王瀚彬 胡帅 +2 位作者 毕丰雷 李隽森 贺来宾 《化工学报》 北大核心 2025年第1期221-230,共10页
旨在开发一种新型波纹换热翅片金属氢化物反应器,以期满足清洁能源技术领域对高效氢气释放性能的迫切需求。通过可靠的有限元数值模拟,得到了换热翅片结构参数、换热流体流动速度对反应器放氢时间的影响。结果表明:基于有限元数值模型... 旨在开发一种新型波纹换热翅片金属氢化物反应器,以期满足清洁能源技术领域对高效氢气释放性能的迫切需求。通过可靠的有限元数值模拟,得到了换热翅片结构参数、换热流体流动速度对反应器放氢时间的影响。结果表明:基于有限元数值模型可以准确得到反应器内部温度以及存储容量变化;翅片高度5 mm、翅片长度2.0 mm、翅片数目13为最优的反应器结构,其氢气释放时间比传统圆盘翅片反应器缩短了24%;换热流体流速对放氢速率有明显改善,当Reynolds数从1780增加到11860时,放氢饱和时间从930 s缩短到700 s。此外波纹翅片易于制造的特性,有利于其在工业领域进行大规模的制造和使用。 展开更多
关键词 金属氢化物 反应器 传递过程 数值模拟 放氢性能 换热翅片
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固态吸附剂用于燃煤烟气碳捕集的研究和应用进展
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作者 崔洁 章鹏飞 《电力科技与环保》 2025年第1期50-58,共9页
碳捕集是减缓全球气候变暖的重要技术手段。固态材料吸附法具有CO_(2)吸附容量高、反应速率高、选择性良好等优点,是近年来的研究热点。本文分析了固体吸附方法的技术原理和研究现状,基于吸附反应器类型总结了不同碳捕集工艺路线的特点... 碳捕集是减缓全球气候变暖的重要技术手段。固态材料吸附法具有CO_(2)吸附容量高、反应速率高、选择性良好等优点,是近年来的研究热点。本文分析了固体吸附方法的技术原理和研究现状,基于吸附反应器类型总结了不同碳捕集工艺路线的特点和中试试验进展,指出了固态吸附碳捕集技术的发展方向。(1)物理吸附剂已广泛应用于变压吸附和真空变压吸附工艺,分为活性炭基吸附剂、沸石基吸附剂以及金属有机框架吸附剂,根据反应温度、压力、浓度的不同,CO_(2)吸附量在20~1500 mg/g;(2)化学吸附剂包括传统的金属氧化物吸附剂和碱金属碳酸盐吸附剂,以及新兴的固态胺吸附剂,其中基于固废材料的固态胺吸附剂常压下CO_(2)吸附量在48.4~206.8 mg/g;(3)目前国内外基于固态吸附剂的碳捕集中试试验主要包括固定床、流化床和移动床等工艺,其中流化床工艺因为具有传热传质效率高、易于规模化放大等优点被大部分研究者采用;(4)固废基固态胺吸附材料具有耐高温、CO_(2)选择性高、循环寿命长等优点,是未来固态碳捕集材料的重点发展方向,且其对于高温燃煤烟气碳捕集更具应用潜力;(5)固态材料碳捕集的工业化应用的工艺研究方向有:低气固传质阻力、高效气固传热的反应器开发,吸附剂解吸再生能耗降低材料和工艺开发。 展开更多
关键词 碳捕集 固态吸附剂 变温吸附 吸附反应器 循环工艺
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A/O工艺与SBR工艺在综合污水处理厂的对比分析
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作者 庞红萍 《中国资源综合利用》 2025年第2期252-256,共5页
2023年3月28日起,江苏省《城镇污水处理厂污染物排放标准》(DB 32/4440—2022)正式实施,对于现有污水处理厂预留了3年改造时间,改造后执行该标准。针对序批式活性污泥(Sequencing Batch Reactor activated sludge,SBR)工艺和厌氧好氧(An... 2023年3月28日起,江苏省《城镇污水处理厂污染物排放标准》(DB 32/4440—2022)正式实施,对于现有污水处理厂预留了3年改造时间,改造后执行该标准。针对序批式活性污泥(Sequencing Batch Reactor activated sludge,SBR)工艺和厌氧好氧(Anaerobic Oxic,A/O)工艺对综合型污水的处理效果进行比较分析。通过运行结果分析可知,A/O工艺对成分复杂的水质处理较为有效,具有耐冲击负荷强、运行简单的特点,为综合性污水处理厂提标改造提供较好的工程实例参考。 展开更多
关键词 厌氧好氧(A/O)工艺 序批式活性污泥(SBR)工艺 综合型污水处理厂
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Hydrodynamic characteristics of a four-compartment periodic anaerobic baffled reactor 被引量:5
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作者 LIU Xiao-lei REN Nan-qi WAN Chun-li 《Journal of Environmental Sciences》 SCIE EI CAS CSCD 2007年第10期1159-1165,共7页
Periodic anaerobic baffled reactor (PABR) is a novel reactor based on the design concept of anaerobic baffled reactor (ABR). Residence time distribution (RTD) studies on both clean and working reactors at the sa... Periodic anaerobic baffled reactor (PABR) is a novel reactor based on the design concept of anaerobic baffled reactor (ABR). Residence time distribution (RTD) studies on both clean and working reactors at the same hydraulic residence time (HRT) of 2 d were carded out to investigate the dead spaces and mixing patterns in PABRs at different organic loading rates (OLRs) in various switching manners and frequencies. The results showed that the fraction of dead space in PABR was similar to that in ABR, which was low in comparison with other reactor designs. Dead space may be divided into two categories, hydraulic and biological. In RTD studies without biomass, the hydraulic dead space in the PABR run in an "every second" switching manner with T = 2 d was the lowest whereas that in the PABR run in a T = ∞ (ABR) switching manner was the highest. The same trend was obtained with the total dead space in RTD studies with biomass no matter what the OLR was. Biological dead space was the major contributor to dead space but affected decreasingly at higher OLR whichever switching manner the PABR run in. The flow patterns within the PABRs were intermediate between plug-flow and perfectly mixed under all the conditions tested, 展开更多
关键词 dead space residence time distribution periodic anaerobic baffled reactor anaerobic processes wastewater treatment
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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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Analysis of prompt supercritical process with heat transfer and temperature feedback 被引量:2
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作者 ZHU Bo ZHU Qian CHEN Zhiyun 《Nuclear Science and Techniques》 SCIE CAS CSCD 2009年第5期317-320,共4页
The prompt supercritical process of a nuclear reactor with temperature feedback and initial power as well as heat transfer with a big step reactivity (ρ0>β) is analyzed in this paper. Considering the effect of he... The prompt supercritical process of a nuclear reactor with temperature feedback and initial power as well as heat transfer with a big step reactivity (ρ0>β) is analyzed in this paper. Considering the effect of heat transfer on temperature of the reactor, a new model is set up. For any initial power, the variations of output power and reactivity with time are obtained by numerical method. The effects of the big inserted step reactivity and initial power on the prompt supercritical process are analyzed and discussed. It was found that the effect of heat transfer on the output power and reactivity can be neglected under any initial power, and the output power obtained by the adiabatic model is basically in accordance with that by the model of this paper, and the analytical solution can be adopted. The results provide a theoretical base for safety analysis and operation management of a power reactor. 展开更多
关键词 超临界 温度反应 核技术 核反应堆
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Computational Modelling of the Hydride Generation Reaction in a Tubular Reactor and Atomization in a Quartz Cell Atomizer 被引量:1
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作者 Wameath S. Abdul-Majeed William B. Zimmerman 《Journal of Analytical Sciences, Methods and Instrumentation》 2012年第3期126-139,共14页
In this study, we present a model whereby the centre of the atomization channel is shown to be the optimal location for the spectrometric data acquisition in a quartz cell atomizer. The study aims to explore the hydri... In this study, we present a model whereby the centre of the atomization channel is shown to be the optimal location for the spectrometric data acquisition in a quartz cell atomizer. The study aims to explore the hydride generation technique which is normally coupled with efficient thermal source to apply determination of heavy metals in water samples via spectrometric analysis. The arsenic hydride generation process and the atomization of the generated hydride in a quartz cell atomizer were studied analytically as model case studies. The hydride generation (HG) process was analyzed by adopting two hypotheses, the nascent hydrogen and formation of intermediate hydroboron species, where the results based on the second hypothesis are found to be more realistic for design purposes. Moreover, the release of the generated hydride from the liquid phase and their transport to the gas phase is simulated in a helical tubular section, in which the actual tubular section length required for separation is deduced. The analytical results have been verified experimentally by measuring the signal intensity for the free arsenic atoms against several reaction tube lengths, in which increasing the tubular section length from 12 cm to 100 cm results in signal amelioration by no more than 6.6%. Furthermore, the atomization of the hydride and the distribution of the generated free atoms are deduced in two configurations of tubular quartz atomizers. The results obtained from both studied cases illustrate that a high concentration of the free analyte atoms is generated in the first part of the atomization channel, saturates to a maximum in a position at the atomizer centre, and dissipates at the inside wall of the tubular atomizer before reaching the atomizer outlet edge, which is found to be in total agreement with the current understanding of atomization mechanism in tubular atomizer and emphasizes the fact that the centre of the quartz cell atomizer is the best location for the spectrometric data acquisition. 展开更多
关键词 HYDRIDE Generation process TUBULAR reactor QUARTZ CELL ATOMIZER Emission Spectroscopy
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Characteristics of high-sulfate wastewater treatment by two-phase anaerobic digestion process with Jet-loop anaerobic fluidized bed 被引量:24
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作者 WEI Chao-hai, WANG Wen-xiang, DENG Zhi-yi, WU Chao-fei School of Environmental Science and Engineering, South China University of Technology, Guangzhou 510640, China. 《Journal of Environmental Sciences》 SCIE EI CAS CSCD 2007年第3期264-270,共7页
A new anaerobic reactor, Jet-loop anaerobic fluidized bed (JLAFB), was designed for treating high-sulfate wastewater. The treatment characteristics, including the effect of influent COD/SO42 ratio and alkalinity and... A new anaerobic reactor, Jet-loop anaerobic fluidized bed (JLAFB), was designed for treating high-sulfate wastewater. The treatment characteristics, including the effect of influent COD/SO42 ratio and alkalinity and sulfide inhibition in reactors, were discussed for a JLAFB and a general anaerobic fiuidized bed (AFB) reactor used as sulfate-reducing phase and methane-producing phase, respectively, in two-phase anaerobic digestion process. The formation of granules in the two reactors was also examined. The results indicated that COD and sulfate removal had different demand of influent COD/SO4^2- ratios. When total COD removal was up to 85%, the ratio was only required up to 1.2, whereas, total sulfate removal up to 95% required it exceeding 3.0. The alkalinity in the two reactors increased linearly with the growth of influent alkalinity. Moreover, the change of influent alkalinity had no significant effect on pH and volatile fatty acids (VFA) in the two reactors. Influent alkalinity kept at 400-500 mg/L could meet the requirement of the treating process. The JLAFB reactor had great advantage in avoiding sulfide and free-H2S accumulation and toxicity inhibition on microorganisms. When sulfate loading rate was up to 8. 1 kg/(m^3.d), the sulfide and free-H2S concentrations in JLAFB reactor were 58.6 and 49.7 mg/L, respectively. Furthermore, the granules, with offwhite color, ellipse shape and diameters of 1.0-3.0 mm, could be developed in JLAFB reactor. In granules, different groups of bacteria were distributed in different layers, and some inorganic metal compounds such as Fe, Ca, Mg etc. were found. 展开更多
关键词 Jet-loop anaerobic fluidized bed reactor sulfate wastewater two-phase anaerobic digestion process granule sludge
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VLDPE Synthesis by Radical Ethylene Polymerization in Tubular Reactors–Negative Factor or Unrealized Opportunities
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作者 Ye. Koval Ye. Skvortsevitch E. Mayer 《Journal of Materials Science and Chemical Engineering》 2013年第1期11-16,共6页
This paper presents the results of polymeric deposit analysis in HP recycling system on two ethylene polymerization trains in tubular reactors when using mixed initiation (organic peroxides and oxygen) in the process ... This paper presents the results of polymeric deposit analysis in HP recycling system on two ethylene polymerization trains in tubular reactors when using mixed initiation (organic peroxides and oxygen) in the process of various grade production. It is demonstrated that polymers belong to the very low density type (with ρ in 0,860 to 0,900 g/cm3 range), due to ultra high branching. Consideration is given to known processes of that kind polymer production. There discussed the alternatives of different approaches to special process features found. It is stated that 80-year high pressure PE synthesis history has been keeping potential for the development. 展开更多
关键词 VLDPE LDPE Production process TUBULAR reactor Mixed INITIATION
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水平对置撞击流反应器强化液-液萃取及传质特性
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作者 张建伟 张昊明 +1 位作者 董鑫 冯颖 《高校化学工程学报》 EI CAS CSCD 北大核心 2024年第5期724-734,共11页
为了研究撞击流技术强化水相从煤油相中萃取乙酸,考察操作条件和溶液性质对萃取效果和传质特性的影响,测定液滴分散程度,利用响应面法优化萃取工况。结果表明:随煤油相进口体积流量和相比(水相与煤油相的体积流量比)的增加,分散相液滴... 为了研究撞击流技术强化水相从煤油相中萃取乙酸,考察操作条件和溶液性质对萃取效果和传质特性的影响,测定液滴分散程度,利用响应面法优化萃取工况。结果表明:随煤油相进口体积流量和相比(水相与煤油相的体积流量比)的增加,分散相液滴粒径分布范围先缩小后扩大,Sauter平均直径d32先减小后增大。萃取率和总体积传质系数随煤油相进口体积流量的增加、水相黏度的增加和表面张力的减小而先增大后减小,随相比的增加呈先增后减再增加的趋势。各因素对萃取率的影响程度为:相比>煤油相进口体积流量>十六烷基三甲基溴化铵(CTAB)质量浓度,且交互作用显著。最佳工况下萃取率为93.11%,较传统萃取工艺提高了5.11%。 展开更多
关键词 撞击流反应器 过程强化 萃取 传质 响应面分析
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SBR处理大蒜废水影响因素和微生物群落特征 被引量:1
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作者 由昆 王晗 +1 位作者 王晓丹 王双全 《水处理技术》 CAS CSCD 北大核心 2024年第5期97-101,共5页
采用AO工艺,利用SBR反应器,以高浓度大蒜废水(COD>7 000 mg/L)为对象,基于控制变量法探究曝气量、进水pH、搅拌速度对污染物去除效果的影响,明确微生物功能菌群和多样性对污染物降解的作用。曝气量和进水pH对污染物去除效果影响显著... 采用AO工艺,利用SBR反应器,以高浓度大蒜废水(COD>7 000 mg/L)为对象,基于控制变量法探究曝气量、进水pH、搅拌速度对污染物去除效果的影响,明确微生物功能菌群和多样性对污染物降解的作用。曝气量和进水pH对污染物去除效果影响显著。系统中以具有脱氮除磷降解有机物功能的拟杆菌门(Bacteroidetes)、变形菌门(Proteobacteria)为主,两者总体细菌相对丰度分别达到了97.82%和98.41%,明显高于接种污泥的56.48%。科水平A2、A3和A1的样本间距离分别为0.894 05和0.875 83,说明其在物种丰度分布上有较大差异,A2、A3中的优势菌科与A1中的优势菌科相差甚大。A2和A3前9类优势菌科基本一致,但其样本间距离为0.233 72,说明物种丰度分布略有差异,两个反应器处理效果会略有不同。A2和A3具有多种功能,其中化能异养和需氧化能异养作用的功能丰度均大于30%。SBR反应器在曝气量为0.3 L/min,进水pH为7.0,搅拌速度为70 r/min的条件下,污染物去除率达到92%以上。 展开更多
关键词 大蒜废水 AO工艺 SBR反应器 微生物 菌群结构
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A study of function mechanism of hemxamethyl tetra-amine in gelation process of uranium
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作者 GUO Wenli LIANG Tongxiang ZHAO Xingyu HAO Shaochang FU Xiaoming 《Rare Metals》 SCIE EI CAS CSCD 2006年第z1期343-346,共4页
The UO2 ceramic microspheres are the most important materials in the spherical fuel elements for high temperature reactor (HTR). A process for preparation of UO2 kernels known as total gelation process of uranium (TGU... The UO2 ceramic microspheres are the most important materials in the spherical fuel elements for high temperature reactor (HTR). A process for preparation of UO2 kernels known as total gelation process of uranium (TGU) was developed as the production process of 10 mW HTR at Tsinghua University. The TGU process is based on the traditional sol-gel process, external gelation process and internal gelation process of uranium (EGU and IGU), which implies that the gelation action is initiated both by ammonia out of the gel particles and hemxamethyl tetra-amine (HMTA) inside the gel particles. The gelation behavior and the properties of uranium microspheres were investigated of the solution with and without HMTA. It is observed that good spherical particles can be obtained without HMTA in the sol, which indicates a more controllable and industrialized route will be set up. Contrasts between this route and the traditional EGU were also listed. 展开更多
关键词 gelation process of uranium high temperature reactor (HTR) UO2 microsphere
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