期刊文献+
共找到476篇文章
< 1 2 24 >
每页显示 20 50 100
A^(2)O工艺活性污泥黏性膨胀原因及控制措施
1
作者 赵晓娟 张智瑞 +1 位作者 刘东洋 雷彬 《工业水处理》 CAS CSCD 北大核心 2024年第4期198-204,共7页
污泥黏性膨胀问题一直是A^(2)O工艺运行控制的难点。郑州市某污水处理厂在运行过程中出现污泥黏性膨胀问题,造成污泥沉降性能变差,SVI逐渐提升至240 mL/g左右,二沉池泥位持续升高。从进水水质、水温、曝气量、浮渣等多方面综合分析引起... 污泥黏性膨胀问题一直是A^(2)O工艺运行控制的难点。郑州市某污水处理厂在运行过程中出现污泥黏性膨胀问题,造成污泥沉降性能变差,SVI逐渐提升至240 mL/g左右,二沉池泥位持续升高。从进水水质、水温、曝气量、浮渣等多方面综合分析引起污泥膨胀的原因,及时从剩余污泥排放量、污泥龄、溶解氧、回流比、水力停留时间等工艺参数调整运行工艺,使污泥膨胀问题得到一定程度的缓解。为彻底消除生物池浮泥,又通过在二沉池配水井精准投加40 mg/L的阳离子高分子絮凝剂,经过一段时间的药剂助沉,明显提高了污泥沉降性能,SVI也逐渐下降至120 mL/g左右的正常水平,解决了污泥黏性膨胀问题,消除了生物池浮泥,为解决污泥黏性膨胀提供了思路。 展开更多
关键词 A^(2)o工艺 污泥黏性膨胀 生物浮泥 絮凝剂
下载PDF
基于A^(2)/O工艺污水厂改造与提标工程设计
2
作者 姚瑞珍 周国胜 +2 位作者 杨新春 陶敏 汪瀚 《水处理技术》 CAS CSCD 北大核心 2024年第2期148-152,共5页
南方某污水厂提标扩建工程,一期A^(2)/O好氧区采用MBBR工艺改造并增大缺氧区容积;二期提标采用高效沉淀池+纤维转盘滤池+紫外消毒工艺,强化脱氮除磷及SS去除,并对全厂进行除臭设计。提标扩建后总规模12×10^(4)m^(3)/d,直接运行成本... 南方某污水厂提标扩建工程,一期A^(2)/O好氧区采用MBBR工艺改造并增大缺氧区容积;二期提标采用高效沉淀池+纤维转盘滤池+紫外消毒工艺,强化脱氮除磷及SS去除,并对全厂进行除臭设计。提标扩建后总规模12×10^(4)m^(3)/d,直接运行成本约0.63元/m^(3),出水均值为COD 17.10 mg/L、BOD55.40 mg/L、SS 5.80 mg/L、NH_(4)^(+)-N 0.90 mg/L、TN 5.90 mg/L、TP 0.30 mg/L。均优于《城镇污水处理厂污染物排放标准》(GB 18918-2002)一级A标准,其经验可供其他污水厂借鉴。 展开更多
关键词 A^(2)/o工艺 MBBR工艺 高效沉淀池 纤维转盘滤池 提标改造
下载PDF
A^(2)O-SBR工艺在城镇污水处理厂中的应用
3
作者 曹一鸣 肖露 +3 位作者 农海豪 胡晓光 唐权昌 甘榜燚 《水处理技术》 CAS CSCD 北大核心 2024年第2期144-147,152,共5页
A^(2)O-SBR工艺为A2O工艺与SBR工艺串联组合,为了探究A^(2)O-SBR工艺在城镇污水处理厂的应用效果,分析广西壮族自治区东兴市城东污水处理厂2021年运行情况,结果表明:厂区出水稳定达标排放,A^(2)O-SBR工艺脱氮除磷效果好;COD、NH_(4)^(+... A^(2)O-SBR工艺为A2O工艺与SBR工艺串联组合,为了探究A^(2)O-SBR工艺在城镇污水处理厂的应用效果,分析广西壮族自治区东兴市城东污水处理厂2021年运行情况,结果表明:厂区出水稳定达标排放,A^(2)O-SBR工艺脱氮除磷效果好;COD、NH_(4)^(+)-N、TP平均去除率为87.05%、97.23%、80.86%,最高去除率为97.55%、98.36%、91.21%;出水浓度相对稳定,A^(2)O-SBR工艺对上述三种污染物的去除率也相对稳定,对NH_(4)^(+)-N效果最好,全年去除率稳定达到95%以上;该污水处理厂平均处理成本0.53元/m^(3)。 展开更多
关键词 A^(2)o-SBR工艺 城镇污水 脱氮除磷 污水处理厂
下载PDF
H_(2)O分子在五边形BCN上的吸附与解离特性研究
4
作者 史金磊 付龙 +2 位作者 时俊仙 冯祎 王美娟 《原子与分子物理学报》 CAS 北大核心 2024年第2期31-34,共4页
基于密度泛函理论的第一性原理计算方法,研究了H_(2)O分子在五边形BCN上的吸附与解离过程.研究结果表明,五边形BCN结构的B原子是H_(2)O分子的最稳定的活性吸附位点.H_(2)O分子在该活性位点极易解离,其初步解离过程为放热反应且分解势垒... 基于密度泛函理论的第一性原理计算方法,研究了H_(2)O分子在五边形BCN上的吸附与解离过程.研究结果表明,五边形BCN结构的B原子是H_(2)O分子的最稳定的活性吸附位点.H_(2)O分子在该活性位点极易解离,其初步解离过程为放热反应且分解势垒仅为0.191 eV,并形成稳定的OH/H产物.深入研究发现,H_(2)O分子初步解离后的五边形BCN表面,可直接分解后续吸附的H_(2)O分子.该研究结果为五边形BCN对H_(2)O分子的吸附解离机制提供理论借鉴. 展开更多
关键词 五边形BCN H_(2)o吸附解离 第一性原理计算
下载PDF
A^(2)O和MBR组合工艺在寒冷地区污水处理中的应用分析
5
作者 吴鹏涛 张文翔 《能源与节能》 2024年第3期65-67,共3页
为进一步探究寒冷地区污水处理效果的提升路径,以一污水处理厂冬季出水水质不达标为研究对象,确定采用A^(2)O (Anaerobic-Anoxic-Oxic,厌氧-缺氧-好氧)工艺与MBR (Membrane Bio-Reactor,膜生物反应器)工艺相结合的方式进行污水处理,在... 为进一步探究寒冷地区污水处理效果的提升路径,以一污水处理厂冬季出水水质不达标为研究对象,确定采用A^(2)O (Anaerobic-Anoxic-Oxic,厌氧-缺氧-好氧)工艺与MBR (Membrane Bio-Reactor,膜生物反应器)工艺相结合的方式进行污水处理,在设计整体方案的基础上,对具体的工艺流程及参数等内容进行全面优化设计,以完成工艺设计。从实际运行效果来看,设计的A^(2)O和MBR组合工艺在寒冷地区污水处理中取得相对较优的效果,证明其具有一定的实际应用价值。 展开更多
关键词 组合工艺 污水处理 工艺设计 A^(2)o MBR
下载PDF
寒冷地区污水处理厂A^(2)O工艺改良调试与运行效果
6
作者 王雨飞 《能源与节能》 2024年第3期112-115,共4页
为进一步提升寒冷地区A^(2)O污水处理工艺的运行效果,以位于寒冷地区的A污水处理厂为研究案例,研究1种具有多点进水、混合液多点回流特性,且适用于寒冷地区污水处理厂的改良型A^(2)O工艺,并从多个角度着手,确定该工艺的设计要点和运行... 为进一步提升寒冷地区A^(2)O污水处理工艺的运行效果,以位于寒冷地区的A污水处理厂为研究案例,研究1种具有多点进水、混合液多点回流特性,且适用于寒冷地区污水处理厂的改良型A^(2)O工艺,并从多个角度着手,确定该工艺的设计要点和运行技术参数等内容。从实际应用效果来看,该改良型A^(2)O工艺在寒冷条件下仍可取得较优的处理效果,可为后续相关工作提供参考。 展开更多
关键词 污水处理厂 A^(2)o工艺 工艺改良
下载PDF
ZnO/Vo-(111)Cu_(2)O/NiF光催化材料协同PMS氧化高效去除盐酸环丙沙星
7
作者 于姗姗 《山东化工》 CAS 2024年第10期34-36,共3页
针对盐酸环丙沙星(CIP-HCl)的难降解性,本实验成功合成了以泡沫镍为基底的光催化异质结ZnO/Vo-(111)Cu_(2)O/NiF,该复合材料具有良好的光响应强度,电化学阻抗较小;通过光照产生的能量激活PMS,使其生成具有强氧化性的活性物质SO_(4)^(... 针对盐酸环丙沙星(CIP-HCl)的难降解性,本实验成功合成了以泡沫镍为基底的光催化异质结ZnO/Vo-(111)Cu_(2)O/NiF,该复合材料具有良好的光响应强度,电化学阻抗较小;通过光照产生的能量激活PMS,使其生成具有强氧化性的活性物质SO_(4)^(·-);利用光催化协同PMS氧化共同参与盐酸环丙沙星的高效降解,在20 min内降解效率高达97.5%。 展开更多
关键词 Zno/Vo-(111)Cu_(2)o/NiF 过氧一硫酸盐 盐酸环丙沙星 氧化工艺
下载PDF
高原生境下乙酸钠为单一碳源对A^(2)O工艺的影响
8
作者 宗永臣 傅椿惠 +3 位作者 李璐辰 史旭升 王明权 刘乐然 《高原农业》 2024年第3期250-257,296,共9页
以高原生境的A^(2)O工艺为研究对象,结合污水处理中污染物浓度不确定性特点,探究了乙酸钠为单一碳源时A^(2)O工艺的反应规律。研究表明,高原生境下A^(2)O工艺在使用乙酸钠作为单一碳源驯化后,具备一定的污染物降解能力,但其去除效率随... 以高原生境的A^(2)O工艺为研究对象,结合污水处理中污染物浓度不确定性特点,探究了乙酸钠为单一碳源时A^(2)O工艺的反应规律。研究表明,高原生境下A^(2)O工艺在使用乙酸钠作为单一碳源驯化后,具备一定的污染物降解能力,但其去除效率随污染物浓度的变化呈现出较大的波动性,说明系统具有不稳定性的特点;同时该系统的污染物去除效率远低于平原地区,菌群在门水平及属水平上的主要细菌及相对丰度均与平原地区有显著差异,说明高原特殊生境对A^(2)O工艺的菌群结构有较大影响,进而影响了污染物的处理效率。研究成果能够为高原生境下污水处理研究提供一定的理论参考。 展开更多
关键词 高原生境 A^(2)o工艺 乙酸钠 群落结构
下载PDF
城市污水处理厂A^(2)/O工艺调试运行实例分析 被引量:3
9
作者 刘荣荣 居之安 《广东化工》 CAS 2023年第2期103-106,共4页
江苏某污水厂实际进水NH3-N值高于设计值。运营以来,由于部分曝气设施老化,好氧池实际泥龄短,生存的硝化菌数量不能实现氨氮稳定达标的要求而导致实际出水水质不能稳定达标。通过提高好氧段实际水力停留时间、活性污泥的培养驯化、改进... 江苏某污水厂实际进水NH3-N值高于设计值。运营以来,由于部分曝气设施老化,好氧池实际泥龄短,生存的硝化菌数量不能实现氨氮稳定达标的要求而导致实际出水水质不能稳定达标。通过提高好氧段实际水力停留时间、活性污泥的培养驯化、改进生化池缺氧段等技术措施,提高好氧池硝化能力,使NH3-N及主要水质指标达到城镇污水处理厂污染物排放标准(GB18918-2002)一级A标准。因为污水处理厂工艺流程复杂就必须不断地进行调试分析,本文是以改污水处理厂为研究对象进行调试研究,并根据调试中遇到的问题提出解决措施和注意事项。 展开更多
关键词 城市污水处理厂 A^(2)/o工艺 调试 水质指标 一级A标准
下载PDF
Formaldehyde degradation by UV/TiO_2/O_3 process using continuous flow mode 被引量:12
10
作者 QI Hong SUN De-zhi CHI Guo-qing 《Journal of Environmental Sciences》 SCIE EI CAS CSCD 2007年第9期1136-1140,共5页
The degradation of formaldehyde gas was studied using UV/TiO2/O3 process under the condition of continuous flow mode. The effects of humidity, initial formaldehyde concentration, residence time and ozone adding amount... The degradation of formaldehyde gas was studied using UV/TiO2/O3 process under the condition of continuous flow mode. The effects of humidity, initial formaldehyde concentration, residence time and ozone adding amount on degradation of formaldehyde gas were investigated. The experimental results indicated that the combination of ozonation with photocatalytic oxidation on the degradation of formaldehyde showed a synergetic action, e.g,, it could considerably increase decomposing of formaldehyde. The degradation efficiency of formaldehyde was between 73.6% and 79.4% while the initial concentration in the range of 1.84--24 mg/m^3 by O3/TiO2flJV process. The optimal humidity was about 50% in UV/TiO2/O3 processs and degradation of formaldehyde increases from 39.0% to 94.1% when the ozone content increased from 0 to 141 mg/m^3. Furthermore, the kinetics of formaldehyde degradation reaction could be described by Langmuir-Hinshelwood model. The rate constant k of 46.72 mg/(m^3.min) and Langmuir adsorption coefficient K of 0.0268 m^3/mg were obtained. 展开更多
关键词 UV/Tio2/o3 process FoRMALDEHYDE continuous flow mode
下载PDF
改良A^(2)O工艺在两级生物滤池改造中的应用
11
作者 赵玺 李绪忠 叶娅萍 《中国资源综合利用》 2023年第11期199-201,共3页
厌氧生物滤池(AF)和曝气生物滤池(BAF)均属于生物膜法污水处理工艺,可以实现脱氮除磷。改造前,某城镇污水处理厂采用两级生物滤池(AF+BAF)组合工艺处理生活污水,冬季水温低至10℃左右,进水氨氮浓度超过60 mg/L,原工艺出水总氮浓度在20 m... 厌氧生物滤池(AF)和曝气生物滤池(BAF)均属于生物膜法污水处理工艺,可以实现脱氮除磷。改造前,某城镇污水处理厂采用两级生物滤池(AF+BAF)组合工艺处理生活污水,冬季水温低至10℃左右,进水氨氮浓度超过60 mg/L,原工艺出水总氮浓度在20 mg/L以上,不满足《城镇污水处理厂污染物排放标准》(GB 18918—2002)的一级A标准要求。本次改造采用改良厌氧缺氧好氧池(A^(2)O)+竖流式沉淀池+高效沉淀池+反硝化滤池的组合工艺强化脱氮除磷,出水水质能够稳定达标。 展开更多
关键词 改良A^(2)o工艺 生物滤池 高效沉淀池 反硝化滤池
下载PDF
IN SITU PROCESSING OF Al_(2)O_(3) WHISKERS REINFORCED Ti-Al INTERMETALLIC COMPOSITES 被引量:6
12
作者 F.Wang Z.K.Fan J.F.Zhu 《Acta Metallurgica Sinica(English Letters)》 SCIE EI CAS CSCD 2006年第6期432-440,共9页
In situ Al2O3 whiskers reinforced Ti-Al intermetallic composites were fabricated at ~1200℃ by reaction sintering of cold-consolidated fillets consisting mainly of Ti, Al, and different additives. The phases and micro... In situ Al2O3 whiskers reinforced Ti-Al intermetallic composites were fabricated at ~1200℃ by reaction sintering of cold-consolidated fillets consisting mainly of Ti, Al, and different additives. The phases and microstructures of the sintered composites were characterized using X-ray diffraction (XRD) and scanning electron microscopy (SEM) coupled with energy dispersive spectroscopy (EDS). The process of synthesis was investigated using differential thermal analysis (DTA). The effects of processing parameters and additives on the microstructures of the composites and the development of whisker were examined. It is found that the morphology of the whisker is strongly influenced by the additives, the exothermal reaction process, and the processing parameters. 展开更多
关键词 in situ Al2o3 whisker Ti-Al intermetallic composite ADDITIVE reaction process
下载PDF
Photolysis pathway of nitroaromatic compounds in aqueous solutions in the UV/H_2O_2 process 被引量:2
13
作者 GOH Ngoh Khang 《Journal of Environmental Sciences》 SCIE EI CAS CSCD 2006年第6期1061-1064,共4页
Nitroaromatic compounds such as nitrobenzene and nitrophenols are largely synthesised and particularly often occur in water bodies as toxic pollutants. The degradation of these compounds in the environment via direct ... Nitroaromatic compounds such as nitrobenzene and nitrophenols are largely synthesised and particularly often occur in water bodies as toxic pollutants. The degradation of these compounds in the environment via direct photolysis and by biological treatment is difficult and usually slow. In our two previous published papers, we have discussed the advanced oxidation of nitrobenzene and nitrophenols in aqueous solutions irradiated by direct photolysis using polychromatic light and by means of UV/H2O2 process. The experimental results suggested the UV/H2O2 process is an effective and efficient technology for complete mineralization of these organic compounds. Based on the results therein, comprehensive reaction mechanism for nitrobenzene photolysis was proposed with detailed discussions. 展开更多
关键词 PHoToLYSIS PATHWAY NITRoBENZENE NITRoPHENoLS UV/H2o2 process
下载PDF
Nitrogen removal for low-carbon wastewater in reversed A^2/O process by regulation technology 被引量:1
14
作者 张智 陈杰云 +3 位作者 谢丽华 范功端 尹晓静 李勇 《Journal of Central South University》 SCIE EI CAS 2009年第S1期304-308,共5页
Full scale experimental study on nitrogen removal for low-carbon wastewater was conducted in reversed A2/O process in Jiguanshi waste water treatment plant in Chongqing,in order to aid the operation and maintenance of... Full scale experimental study on nitrogen removal for low-carbon wastewater was conducted in reversed A2/O process in Jiguanshi waste water treatment plant in Chongqing,in order to aid the operation and maintenance of similar WWTP. When the proposed measures,such as using 0.1% (volume fraction of wastewater) landfill leachate,shortening HRT by 2/3 in the primary sedimentation tank and controlling DO at 0.5 mg/L in the 3rd section of aerobic zone,are applied,15% of the carbon source can be complemented,the favorable property of activated sludge is achieved,and the nitrogen removal effect is significantly improved. The effluent NH3-N is 2 mg/L and the removal rate is 90%. The effluent TN is 17 mg/L and the removal rate is 54%. The up-to-standard discharge of the effluent is achieved. And after the optimization,the unit electricity consumption also reaches 0.21 kW/h and saves 20%. 展开更多
关键词 reversed A2/o process low-carbon resource LANDFILL LEACHATE primary SEDIMENTATIoN TANK nitrogen removal
下载PDF
Effects of Nitrogen Application on N_2O Flux from Fluvo-Aquic Soil Subject to Freezing-Thawing Process 被引量:3
15
作者 WANG Feng GAO Shang-bin +4 位作者 ZHANG Ke-qiang LI Hai-bo BAI Li-jing HUANG Zhi-ping MI Chang-hong 《Agricultural Sciences in China》 CAS CSCD 2010年第4期577-582,共6页
A lab-incubation experiment was conducted to investigate the effects of different forms of nitrogen application (ammonium, NH4+-N; nitrate, NO3--N; and amide-N, NH2-N) and different concentrations (40, 200 and 800... A lab-incubation experiment was conducted to investigate the effects of different forms of nitrogen application (ammonium, NH4+-N; nitrate, NO3--N; and amide-N, NH2-N) and different concentrations (40, 200 and 800 mg L-1) on N2O emission from the fluvo-aquic soil subjected to a freezing-thawing cycling. N2O emission sharply decreased at the start of soil freezing, and then showed a smooth line with soil freezing. In subject to soil thawing, N2O emission increased and reached a peak at the initial thawing stage. The average N2O emissions with addition of NH4+-N, NO3 -N and NH2-N are 119.01, 611.61 and 148. 22 ug m-2 h-1, respectively, at the concentration of 40 mg L-1; 205.28, 1 084.40 and 106.13 ug m2 h-1 at the concentration of 200 mg L-1; and 693.95, 1 820.02 and 49.74 ug m-2 h4 at the concentration of 800 mg L-1. The control is only 100.35 ug m-2 h-1. N2O emissions with addition of NH4+-N and NO3--N increased with increasing concentration, by ranging from 17.49 to 425.67% for NH4+-N, and from 563.38 to 1458.6% for NO3--N compared with control. There was a timelag for N2O emission to reach a steady state with an increase of concentration. In contrast, by adding NH2-N to soil, N2O emission decreased with increasing concentration. In sum, NH4+-N or NO3--N fertilizer incorporated in soil enhanced the cumulative N2O emission from the fluvo-aquic soil relative to amide-N. This study suggested that ammonium and nitrate concentration in overwintering water should be less than 200 and 40 mg L-1 in order to reduce N2O emissions from soil, regardless of amide-N. 展开更多
关键词 freezing-thawing process NH4+ -N No3--N amide-N N2o flux
下载PDF
Photodegradation of nitroaromatic compounds in aqueous solutions in the UV/H_2O_2 process 被引量:1
16
作者 GOH Ngoh Khang 《Journal of Environmental Sciences》 SCIE EI CAS CSCD 2005年第6期886-893,共8页
Photodegradation of nitrobenzene and nitrophenols in aqueous solutions by means of UV/H2 O2 process was studied in the Rayox batch reactors. Three nitrophenol isomers were identified as main photoproducts in the irrad... Photodegradation of nitrobenzene and nitrophenols in aqueous solutions by means of UV/H2 O2 process was studied in the Rayox batch reactors. Three nitrophenol isomers were identified as main photoproducts in the irradiated NB aqueous solutions. The distribution of nitrophenol isomers follows the order p-〉 m-〉 o-nitrophenol. Other intermediates detected include nitrohydroquinone, nitrocatechol, catechol, benzoquinone, phenol, nitrate/nitrite ions, formic acid, glyoxylic acid, maleic acid, oxalic acid and some aliphatic ketones and aldehydes. The degradation of nitrobenzene and nitrophenols at initial stages follows the first-order kinetics and the decay rate constants for nitrobenzene(NB) are around l0^-3-10^-2 s^-1 and for nitrophenols are around 10^-2 s^-1. The decomposition of H2 O2 in the presence of NB and each nitrophenol isomers follows zero-order kinetics. The quantum yields at initial stages for NB decay were estimated around 0.30 to 0.36, and for NPs decay is around 0.31-0.54. 展开更多
关键词 PHoToDEGRADATIoN NITRoBENZENE NITRoPHENoLS UV/H2 o2 process
下载PDF
Preparation of Spherical Bi_2O_3 Powder by Plasma and Precipitation Processes 被引量:1
17
作者 陈培荣 季幼章 冯士芬 《Plasma Science and Technology》 SCIE EI CAS CSCD 2005年第6期3139-3142,共4页
Spherical Bi2O3 powder prepared by plasma chemical vapor reaction and aqueous chemical precipitation is studied. The superfine spherical Bi2O3 powder with an average diameter of 1 μm is made by plasma process. During... Spherical Bi2O3 powder prepared by plasma chemical vapor reaction and aqueous chemical precipitation is studied. The superfine spherical Bi2O3 powder with an average diameter of 1 μm is made by plasma process. During the precipitation process, the micrograph of the Bi2O3 powder can be controlled through the reaction temperature, the rate of addition of the precipitation reagent, the reaction time and the amount of the dispersant. Accordingly, spherical Bi2O3 powder with diameters ranging from 2μm to 3μm is prepared. The spherical Bi2O3 particles have such advantages as uniform size distribution and excellent dispersing property. ZnO varistors made from the resultant powder exhibit properties of a low discharge voltage ratio, great eligibility coefficient measured by a rectangle wave of 2 ins 800 A and good stability in the above characteristics. 展开更多
关键词 spherical Bi2o3 plasma process precipitation process VARISToR
下载PDF
Explosion limits estimation and process optimization of direct propylene epoxidation with H2 and O2 被引量:1
18
作者 Mengke Lu Yanqiang Tang +5 位作者 Wenyao Chen Guanghua Ye Gang Qian Xuezhi Duan Weikang Yuan Xinggui Zhou 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2019年第12期2968-2978,共11页
Direct propylene epoxidation with H2 and O2,an attractive process to produce propylene oxide(PO),has a potential explosion danger due to the coexistence of flammable gases(i.e.,C3 H6 and H2)and oxidizer(i.e.,O2).The u... Direct propylene epoxidation with H2 and O2,an attractive process to produce propylene oxide(PO),has a potential explosion danger due to the coexistence of flammable gases(i.e.,C3 H6 and H2)and oxidizer(i.e.,O2).The unknown explosion limits of the multi-component feed gas mixture make it difficult to optimize the reaction process under safe operation conditions.In this work,a distribution method is proposed and verified to be effective by comparing estimated and experimental explosion limits of more than 200 kinds of flammable gas mixture.Then,it is employed to estimate the explosion limits of the feed gas mixture,some results of which are also validated by the classic Le Chatelier’s Rule and flammable resistance method.Based on the estimated explosion limits,process optimization is carried out using commercially high and inherently safe reactant concentrations to enhance reaction performance.The promising results are directly obtained through the interface called gOPT in gPROMS only by using a simple,easy-constructed and mature packed-bed reactor,such as the PO yield of 13.3%,PO selectivity of 85.1%and outlet PO fraction of 1.8%.These results can be rationalized by indepth analyses and discussion about the effects of the decision variables on the operation safety and reaction performance.The insights revealed here could shed new light on the process development of the PO production based on the estimation of the explosion limits of the multi-component feed gas mixture containing flammable gase s,inert gas and O2,followed by process optimization. 展开更多
关键词 DIRECT PRoPYLENE EPoXIDATIoN with H2/o2 PRoPYLENE oxide Safe operation Explosion limits ESTIMATIoN process optimization
下载PDF
Polyol Process to Large-scale Synthesis of Cu_2O with Disk-like Structure 被引量:1
19
作者 YuanTaoCHEN WeiZHANG BangZhiZHOU XiaoQingXU YanQingFAN YouJingGUO ZhongXinZHANG 《Chinese Chemical Letters》 SCIE CAS CSCD 2005年第2期245-248,共4页
关键词 Polyol process Cu_2o disk-like structure.
下载PDF
Luminescent Properties of Y_2O_3∶Eu Nanocrystalls Synthesized by EDTA Complexing Sol-Gel Process 被引量:1
20
作者 翟永清 姚子华 +2 位作者 刘保生 翟建 王凯肖 《Journal of Rare Earths》 SCIE EI CAS CSCD 2002年第5期465-470,共6页
Y 2O 3: Eu nanocrystals were synthesized by EDTA complexing sol gel process at a relatively low temperature, in which ethylen diamine tetraacetic acid (EDTA) and polyethylene glycol (PEG) were used as the chelat... Y 2O 3: Eu nanocrystals were synthesized by EDTA complexing sol gel process at a relatively low temperature, in which ethylen diamine tetraacetic acid (EDTA) and polyethylene glycol (PEG) were used as the chelating agent and polymerization agent respectively. Formation process of Y 2O 3:Eu and structure characterization were carried out by TG DTA, XRD, SEM/EDX. The results show that pure cubic phase Y 2O 3: Eu nanocrystalsere is produced after the precursor calcinated at 600 ℃ for 2 h, and the crystallinity increases with increasing calcination temperature. The nanoparticles of the Y 2O 3: Eu are basically spherical in shape. The mean particle size increases from about 30 to 70 nm when the calcination temperature increases from 600 to 1000 ℃. The luminescent properties of phosphor were analyzed by measuring the excitation and emission spectra. The main emission peak of the sample is around 612 nm, resulting in a red emission. The emission intensity increases with the calcination temperature. Compared with microsized Y 2O 3: Eu phosphors prepared by a conventional method, nanosized Y 2O 3: Eu synthesized by the present work, gives and a clear red shift in the emission spectrum. Moreover, the quenching concentration of Eu is raised. 展开更多
关键词 rare earths Y 2o 3∶Eu NANoCRYSTALLINE sol sel process luminescence
下载PDF
上一页 1 2 24 下一页 到第
使用帮助 返回顶部