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CSTR系统中氢气燃烧特性的分岔分析
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作者 曾文 解茂昭 +2 位作者 贾明 艾延廷 王成军 《燃烧科学与技术》 EI CAS CSCD 北大核心 2009年第1期40-44,共5页
运用分岔理论,采用了氢气的详细化学反应机理,对连续流动均匀搅拌反应器(CSTR)中氢气的燃烧特性进行详细的分析.分别以系统温度、滞留时间为分岔参数,详细讨论了CSTR系统的各种工况(系统压力、入口混合气过量空气系数、系统温度及滞留时... 运用分岔理论,采用了氢气的详细化学反应机理,对连续流动均匀搅拌反应器(CSTR)中氢气的燃烧特性进行详细的分析.分别以系统温度、滞留时间为分岔参数,详细讨论了CSTR系统的各种工况(系统压力、入口混合气过量空气系数、系统温度及滞留时间)对混合气着火特性的影响.结果表明,当以系统温度为分岔参数时,系统压力及滞留时间对混合气的燃烧特性影响较大,而过量空气系数影响较小;当以滞留时间为分岔参数时,系统温度对混合气燃烧特性有较大的影响. 展开更多
关键词 连续流动均匀搅拌反应器(cstr) 分岔理论 氢气 着火特性
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Temperature fault-tolerant control system of CSTR with coil and jacket heat exchanger based on dual control and fault diagnosis 被引量:1
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作者 WANG Zai-ying WANG Guo-xin 《Journal of Central South University》 SCIE EI CAS CSCD 2017年第3期655-664,共10页
For the characteristics of the continuous stirred-tank reactor(CSTR) with coil and jacket cooling system,a CSTR temperature dual control solution based on the analysis of the CSTR exothermic reaction control character... For the characteristics of the continuous stirred-tank reactor(CSTR) with coil and jacket cooling system,a CSTR temperature dual control solution based on the analysis of the CSTR exothermic reaction control characteristic was proposed for an organic material polymerization production.The control solution has passive fault-tolerant ability for the jacket cooling water cutting off fault and active fault-tolerant potential for the coil cooling water cutting off fault,and it has good control ability,high saving energy and reducing consumption performance.Fault detection and diagnosis and fault-tolerant control strategy are designed for the coil cooling fault to achieve the active fault-tolerant control function.The CSTR temperature dual control,process fault detection and diagnosis and active fault-tolerant control were full integrated into the CSTR temperature fault-tolerant control system,which achieve fault tolerance control of CSTR temperature for any severe malfunction of jacket cooling or coil cooling cutting off,and the security for CSTR exothermic reaction is improved.Finally,the effectiveness of this system was validated by semi-physical simulation experiment. 展开更多
关键词 continuous stirred-tank reactor (cstr exothermic reaction dual control process fault diagnosis fault-tolerant control
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垂直流人工湿地系统中水流规律的研究 被引量:47
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作者 付贵萍 吴振斌 +3 位作者 任明迅 贺锋 Alex Pressl Reinhard Perfler 《环境科学学报》 CAS CSCD 北大核心 2001年第6期720-725,共6页
对一种新型的垂直流人工湿地系统的水流特性进行了研究 .考察了系统的运行状况及介质中滞留区的分布范围 ,并且运用化学工程中反应器理论 ,采用示踪剂试验的方法得到了垂直流人工湿地系统的停留时间分布与污水的实际停留时间 .根据水流... 对一种新型的垂直流人工湿地系统的水流特性进行了研究 .考察了系统的运行状况及介质中滞留区的分布范围 ,并且运用化学工程中反应器理论 ,采用示踪剂试验的方法得到了垂直流人工湿地系统的停留时间分布与污水的实际停留时间 .根据水流停留时间分布函数对系统实际液流流态进行了数学模拟 ,提出二级串联的理想完全混合反应器 (CSTR) 展开更多
关键词 垂直流人工湿地 水流分布 示踪剂 完全混合反应器 cstr 水流规律 废水处理 污水净化
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pH对发酵系统的产甲烷活性抑制及产氢强化 被引量:9
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作者 李建政 苏晓煜 +2 位作者 昌盛 张立国 于泽 《哈尔滨工业大学学报》 EI CAS CSCD 北大核心 2012年第4期63-66,共4页
为抑制厌氧发酵系统的产甲烷活性,强化其发酵产氢性能,采用逐级降低pH的调控方法,探讨连续流搅拌槽式反应器(CSTR)从具有显著甲烷发酵特征的厌氧发酵系统向发酵产氢系统转变的运行特征.在进水COD 7 000 mg/L、水力停留时间(HRT)8 h条件... 为抑制厌氧发酵系统的产甲烷活性,强化其发酵产氢性能,采用逐级降低pH的调控方法,探讨连续流搅拌槽式反应器(CSTR)从具有显著甲烷发酵特征的厌氧发酵系统向发酵产氢系统转变的运行特征.在进水COD 7 000 mg/L、水力停留时间(HRT)8 h条件下,发酵体系在pH由6.5~7.2降低到6.0~6.5时,虽然发酵气中的甲烷体积分数逐渐减少乃至消失,但氢气体积分数一直在3%以下;当pH下降到4.0~5.0时,系统中的产酸发酵作用得到了进一步强化,挥发性发酵产物总量平均为2 052 mg/L,呈现为典型的乙醇型发酵,发酵气产量平均为26 L/d,其氢气体积分数稳定在45%左右,活性污泥的比产氢率达1.67 L/(g.d). 展开更多
关键词 有机废水 甲烷发酵 发酵产氢 pH调控 连续流搅拌槽式反应器
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超痕量H_2O_2对MnSO_4-KBrO_3-乙酰丙酮化学振荡体系的扰动 被引量:8
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作者 张珂 蔡汝秀 +2 位作者 马万红 林智信 甘南琴 《高等学校化学学报》 SCIE EI CAS CSCD 北大核心 2000年第3期377-379,共3页
The similarities between life processes that exhibit oscillatory behavior and chemical oscillating systems impel people to think that the biological and abiological phenomena conform to the same law. Oscillating chemi... The similarities between life processes that exhibit oscillatory behavior and chemical oscillating systems impel people to think that the biological and abiological phenomena conform to the same law. Oscillating chemical systems have been the focus of much research in the area of theoretical and experimental chemical dynamics as well as analytical sciences in recent years, but the studies on the perturbation species are kept around the concentration level of 10 -7 mol/L. In our experiment, an amazed phenomenon was found. Ultra trace level (10 -20 mol/L) of H 2O 2 can cause so magnitude influence on the macro system (MnSO 4 KBrO 3 diacetone oscillating chemical system) that the effect can be observed by a macroscopical method. When the concentration of H 2O 2 is above 10 -13 mol/L , the oscillation can even be stopped. A further study on the mechanism will doubtlessly help to understand the mystery of life, such as the sudden cardiopathy and the metabolism failure. 展开更多
关键词 化学振荡反应 非线性动力学 过氧化氢 cstr
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ABR发酵系统运行特性及产氢效能研究 被引量:6
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作者 郑国臣 李建政 +5 位作者 昌盛 张照韩 官涤 金羽 郭静波 卢海凤 《中国环境科学》 EI CAS CSCD 北大核心 2013年第1期75-81,共7页
为解决连续流搅拌槽式反应器(CSTR)发酵制氢系统存在的不足,如单位基质氢气转化率低、因搅拌带来的耗能,抗负荷冲击能力不强等问题,开展了厌氧折流板反应器(ABR)发酵产氢的研究.结果表明,在35℃和进水COD 5000mg/L等条件下,ABR系统可在... 为解决连续流搅拌槽式反应器(CSTR)发酵制氢系统存在的不足,如单位基质氢气转化率低、因搅拌带来的耗能,抗负荷冲击能力不强等问题,开展了厌氧折流板反应器(ABR)发酵产氢的研究.结果表明,在35℃和进水COD 5000mg/L等条件下,ABR系统可在26d达到乙醇型发酵,其比产氢速率为0.13L/(gMLVSS.d),而在同样条件下,CSTR达到乙醇型发酵后,比产氢速率仅为0.06L/(gMLVSS.d).ABR通过生物相的分离,使产氢系统梯级利用有机物并达到深度产氢的目的.与CSTR相比,ABR具有较高的产氢活性、较低能源消耗等优点,是一种较为理想的有机废水发酵制氢反应设备. 展开更多
关键词 有机废水 厌氧发酵 生物制氢 连续流搅拌槽式反应器(cstr) 厌氧折流板反应器(ABR)
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Determination of Heroin Based on Analyte Pulse Perturbation to an Oscillating Chemical Reaction 被引量:4
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作者 RENJie GAOJin-zhang +5 位作者 Suo-nan ZHAOGuo-hu YANGWu LüDong-yu SUNKan-jun LIChong-yang 《Chemical Research in Chinese Universities》 SCIE CAS CSCD 2004年第5期534-538,共5页
A new analytical method is proposed for the determination of heroin based on a sequential perturbation caused by trace amounts of heroin in the Cu(Ⅱ)-catalyzed oscillating reaction between hydrogen peroxide and sodiu... A new analytical method is proposed for the determination of heroin based on a sequential perturbation caused by trace amounts of heroin in the Cu(Ⅱ)-catalyzed oscillating reaction between hydrogen peroxide and sodium thiocyanate in an alkaline medium with the aid of a continuous-flow stirred tank reactor(CSTR). The method relies on the linear relationship between the change in oscillation period of the system and the concentration of heroin, with a detecting limit of 4.0×10^(-7) mol/L. The calibration curve fits a linear equation very well when the concentration of heroin is in the range of 2.0×10^(-6)_1.2×10^(-5) mol/L(r=0.9971). This method features good precision(RSD=0.98%). The influences of temperature, injection point, flow rate and reaction variables on the oscillation period were investigated in detail and a possible mechanism of the performance of heroin in the Cu(Ⅱ)-catalyzed oscillating reaction system is also discussed. The proposed method opens a new avenue for the determination of heroin. 展开更多
关键词 Cu(Ⅱ)-catalyzed oscillating reaction HEROIN Analyte pulse perturbation technique(APP) Mechanism continuous-flow stirred tank reactor(cstr).
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厌氧发酵反应器的启动运行及活性污泥的优势菌群分析 被引量:1
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作者 王靖媛 秦智 尹梦 《上海师范大学学报(自然科学版)》 2018年第6期704-712,共9页
为探讨连续流搅拌槽式厌氧发酵反应器(CSTR)的启动运行效能和活性污泥的优势菌群组成,考察了CSTR处理高浓度糖蜜废水启动运行期的进出水化学需氧量(COD)和p H值变化规律,并采用Illumina Mi Seq平台高通量测序技术对比分析了启动运行不... 为探讨连续流搅拌槽式厌氧发酵反应器(CSTR)的启动运行效能和活性污泥的优势菌群组成,考察了CSTR处理高浓度糖蜜废水启动运行期的进出水化学需氧量(COD)和p H值变化规律,并采用Illumina Mi Seq平台高通量测序技术对比分析了启动运行不同阶段的优势菌群组成.研究结果表明:厌氧发酵反应器经过启动阶段的运行,较好地完成了厌氧活性污泥的驯化.在启动运行后期,反应器出水pH值稳定在4. 7~4. 9之间,液相发酵产物总量为1298 mg·L^(-1),其中乙酸和丁酸质量占发酵产物总质量的73. 1%,形成丁酸型发酵的主要发酵产物;活性污泥沉降30 min后,沉降污泥的体积分数为37%,驯化后活性污泥具有良好的沉降性能.活性污泥优势菌群分析表明:反应器启动运行后期,活性污泥形成以产乙醇杆菌属(Ethanoligenes)、巨型球菌属(Megasphaera)和Ⅳ型梭菌(Clostridium IV)为主的优势菌群. 展开更多
关键词 连续流搅拌槽式反应器(cstr) 启动运行 优势菌群
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2种启动方式下CSTR厌氧甲烷发酵系统的运行特性比较 被引量:1
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作者 昌盛 刘枫 李建政 《环境工程学报》 CAS CSCD 北大核心 2017年第2期689-694,共6页
厌氧产甲烷菌生长缓慢,对生境环境尤为敏感,其富集难且慢,所以厌氧反应器的快速启动一直是热点研究问题。为摸清连续流搅拌槽式反应器(CSTR)处理糖蜜废水的适宜启动条件和调控方法,比较了两种启动方式下CSTR厌氧甲烷发酵系统的运行特性... 厌氧产甲烷菌生长缓慢,对生境环境尤为敏感,其富集难且慢,所以厌氧反应器的快速启动一直是热点研究问题。为摸清连续流搅拌槽式反应器(CSTR)处理糖蜜废水的适宜启动条件和调控方法,比较了两种启动方式下CSTR厌氧甲烷发酵系统的运行特性。结果显示,以啤酒废水污水处理车间的剩余污泥为种泥,在HRT为18 h、温度35℃条件下,进水COD为4 000 mg·L^(-1)时直接启动CSTR厌氧反应器,系统因挥发酸积累,产甲烷菌群活性受限,难以富集培养,经过近103d的运行,系统未形成高效的厌氧甲烷发酵微生物菌群结构体系;而当采用保持HRT18 h不变,进水COD阶段性提升至4000 mg·L^(-1)的启动方式时,产甲烷菌群活性较高,能在较短时间内得到有效富集和培养,CSTR能成功培养具有完整甲烷发酵功能的微生物菌,COD去除率可在65 d内达到56%,反应器成功启动。 展开更多
关键词 厌氧消化 糖蜜废水 cstr 启动负荷 COD去除率
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CSTR和ABR甲烷发酵系统运行特征比较
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作者 李雨霏 郑国臣 +4 位作者 项丽君 李建政 郭静波 张照韩 王英伟 《中国给水排水》 CAS CSCD 北大核心 2014年第19期24-28,共5页
厌氧发酵技术是解决环境污染及能源需求问题的重要途径。针对常见的连续流搅拌槽式反应器(CSTR)和厌氧折流板反应器(ABR)存在的甲烷发酵技术问题,开展了产甲烷系统的调控技术研究。在特定条件下,比较CSTR和ABR两类反应器的甲烷发酵系统... 厌氧发酵技术是解决环境污染及能源需求问题的重要途径。针对常见的连续流搅拌槽式反应器(CSTR)和厌氧折流板反应器(ABR)存在的甲烷发酵技术问题,开展了产甲烷系统的调控技术研究。在特定条件下,比较CSTR和ABR两类反应器的甲烷发酵系统效能。结果表明,在进水COD为4 000 mg/L、HRT为24 h条件下,CSTR系统运行73 d后可形成完整甲烷发酵,对COD的去除率维持在70%左右,但系统运行不够稳定。在接种污泥、进水COD、HRT等相同的情况下,ABR系统运行17 d后,对COD的去除率即可达到74%;保持有机负荷为4 kg/(m3·d)不变,通过调控ABR进水COD浓度、HRT等后,对COD的去除率可达到90%以上。与CSTR相比,ABR通过生物相的分离(产酸发酵菌群、产氢产乙酸菌群和产甲烷菌群等沿程分布于各格室并呈现不同的优势度),增强了产氢产乙酸作用,使系统去除效能更高、抗冲击负荷能力更强,运行也更稳定。 展开更多
关键词 有机废水 甲烷发酵 连续流搅拌槽式反应器 厌氧折流板反应器
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Growth mechanism of CsPbBr3 perovskite nanocrystals by a co-precipitation method in a CSTR system 被引量:3
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作者 Jibin Zhang Lianwei Fan +4 位作者 Junli Li Xiangfu Liu Rongwen Wang Lei Wang Guoli Tu 《Nano Research》 SCIE EI CAS CSCD 2019年第1期121-127,共7页
A co-precipitation method based on supersaturated recrystallization in a continuous stirred-tank reactor(CSTR)system was applied to un cover the growth mecha nism of CsPbBr3 perovskite nano crystals(NCs).The reacti on... A co-precipitation method based on supersaturated recrystallization in a continuous stirred-tank reactor(CSTR)system was applied to un cover the growth mecha nism of CsPbBr3 perovskite nano crystals(NCs).The reacti on rate can be controlled by changi ng the reaction conditions in this CSTR system,which helps us to observe importa nt intermediate stages to gain in sight into the growth mecha nism of these NCs.The effects of the temperature,concentrations of the ligands(oleylamine and oleic acid),and precursor concerttrations during the growth process of CsPbBr3 NCs were discussed in detail.Further,the growth mechanism of CsPbBr3 NCs was investigated in terms of the dynamics and thermodynamics on the basis of experimental results.The growth mechanism is a useful guide to large-scale synthesis.The synthesized CsPbBr3 NCs were employed for fabrication of both white light-emitting diodes and quantum-dot light-emitting diodes to test their photoelectric properties;the results show that CsPbBr3 NCs show great promise for optoelectronics applications. 展开更多
关键词 PEROVSKITE CsPbBr3 NANOCRYSTALS growth mechanism continuous stirred-tank reactor(cstr)system
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Ammoniacal Nitrogen and Organics Removal Modelling in Vertical Flow Wetlands Treating Strong Wastewaters
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作者 Tanveer Ferdous Saeed Abdullah A1 Muyeed Guangzhi Sun 《湿地科学》 CSCD 北大核心 2013年第4期421-432,共12页
This paper reports a comparative evaluation between 2 kinetic models for predicting nitrification and biodegradable organics(BOD5)removal rates in 5 vertical flow(VF)wetland systems,that received strong wastewaters(i.... This paper reports a comparative evaluation between 2 kinetic models for predicting nitrification and biodegradable organics(BOD5)removal rates in 5 vertical flow(VF)wetland systems,that received strong wastewaters(i.e.tannery,textile and municipal effluents).The models were formulated by combining first order and Monod kinetics,with continuous-stirred tank reactor(CSTR)flow approach.The performance of the 2 models had been evaluated with3 statistical parameters:coefficient of determination(R2),relative root mean square error(RRMSE),and model efficiency(ME).The statistical parameters indicated better performance of the Monod CSTR model(over first order CSTR approach),for correlating ammoniacal nitrogen(NH4+—N)and BOD5removal profiles across VF systems.Higher Monod coefficient values(from Monod CSTR model)coincided with greater input NH4+—N and BOD5loading,and experimentally measured removal rate(g/(m2·d))values.Such trends indicate that NH4+—N and BOD5removals in the VF systems were mainly achieved via biological routes.On the other hand,the rate constants(from the first order CSTR model)did not exhibit such correlations(of Monod coefficients),elucidating their inefficiencies in capturing overall removal mechanisms.The interference of organics removal on nitrification process(in VF wetlands)was identified through Monod coefficients.The deviation between NH4+—N and BOD5Monod coefficients imply incorporation of both coefficients,for calculating the area of a single VF bed.Overall,closer performance of the Monod CSTR model for predicting NH4+—N and BOD5removals indicate its potential application,as a design tool for VF systems. 展开更多
关键词 cstr 废物处理 技术方法 BOD
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城市生物质废物热水解-ASBR厌氧消化研究 被引量:8
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作者 侯华华 王伟 +1 位作者 胡颂 徐衣显 《环境科学》 EI CAS CSCD 北大核心 2010年第2期526-533,共8页
通过热水解预处理提高城市生物质废物的固体有机物溶解率,使用厌氧序批式反应器(ASBR)提高生物质废物厌氧消化效率.结果表明,热水解的优化条件为175℃、60min,餐厨垃圾、果蔬垃圾和污泥的挥发性悬浮固体(VSS)的溶解率分别为31.... 通过热水解预处理提高城市生物质废物的固体有机物溶解率,使用厌氧序批式反应器(ASBR)提高生物质废物厌氧消化效率.结果表明,热水解的优化条件为175℃、60min,餐厨垃圾、果蔬垃圾和污泥的挥发性悬浮固体(VSS)的溶解率分别为31.3%、31.9%和49.7%.热水解后餐厨垃圾、果蔬垃圾和污泥中液态有机物占总有机物的比例分别为54.28%、58.14%和40.91%.在水力停留时间(HRT)20d的条件下,2个ASBR反应器(简称A1和A2)与1个连续流完全混合反应器(CSTR,简称C)同时启动,COD容积负荷3.2~3.6kg/(m^3·d),3个反应器的平均日产气量分别为:5656mL/d(A1)、6335mL/d(A2)、3103mL/d(C);VSS的降解率分别为45.3%(A1)、50.87%(A2)、20.81%(C).TCOD的去除率分别为88.1%(A1)、90%(A2)、72.6%(C).ASBR反应器通过沉降使固体有机物和厌氧微生物获得较长的停留时间,在HRT20d时获得的污泥停留时间(SRT)超过130d,因此,获得比CSTR更高的处理效率. 展开更多
关键词 生物质废物 热水解 厌氧序批式反应器 厌氧消化 连续流完全混合反应器
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Effects of mixture ratio on anaerobic co-digestion with fruit and vegetable waste and food waste of China 被引量:38
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作者 Jia Lin Jiane Zuo +5 位作者 Lili Gan Peng Li Fenglin Liu Kaijun Wang Lei Chen Hainan Gan 《Journal of Environmental Sciences》 SCIE EI CAS CSCD 2011年第8期1403-1408,共6页
The biochemical methane potentials for typical fruit and vegetable waste (FVW) and food waste (FW) from a northern China city were investigated, which were 0.30, 0.56 m3 CH4/kgVS (volatile solids) with biodegrad... The biochemical methane potentials for typical fruit and vegetable waste (FVW) and food waste (FW) from a northern China city were investigated, which were 0.30, 0.56 m3 CH4/kgVS (volatile solids) with biodegradabilities of 59.3% and 83.6%, respectively. Individual anaerobic digestion testes of FVW and FW were conducted at the organic loading rate (OLR) of 3 kg VS/(m3-day) using a lab-scale continuous stirred-tank reactor at 35°C. FVW could be digested stably with the biogas production rate of 2.17 ma/(m3-day) and methane production yield of 0.42 m3 CH4/kg VS. However, anaerobic digestion process for FW was failed due to acids accumulation. The effects of FVW: FW ratio on co-digestion stability and performance were further investigated at the same OLR. At FVW and FW mixing ratios of 2:1 and 1:1, the performance and operation of the digester were maintained stable, with no accumulation of volatile fatty acids (VFA) and ammonia. Changing the feed to a higher FW content in a ratio of FVW to FW 1:2, resulted in an increase in VFAs concentration to 1100-1200 rag/L, and the methanogenesis was slightly inhibited. At the optimum mixture ratio 1:1 for co-digestion of FVW with FW, the methane production yield was 0.49 m3 CH4/kg VS, and the volatile solids and soluble chemical oxygen demand (sCOD) removal efficiencies were 74.9% and 96.1%, respectively. 展开更多
关键词 anaerobic co-digestion biochemical methane potential continuous stirred-tank reactor (cstr fruit and vegetable waste food waste
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Optimal Choice of Weighting Factors in Adaptive Linear Quadratic Control
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作者 Jiri Vojtesek Petr Dostal 《International Journal of Automation and computing》 EI CSCD 2014年第3期241-248,共8页
Most of the processes in the industry have nonlinear behavior. Control of such processes with conventional control methods could lead to unstable, suboptimal, etc., results. On the other hand, the adaptive control is ... Most of the processes in the industry have nonlinear behavior. Control of such processes with conventional control methods could lead to unstable, suboptimal, etc., results. On the other hand, the adaptive control is a technique widely used for controlling of nonlinear systems. The approach here is based on the recursive identification of the external linear model as a linear representation of the originally nonlinear system. The controller then reacts to the change of the working point or disturbances which could occur by the change of the parameters, structure, etc. The polynomial synthesis together with the linear quadratic(LQ) approach is employed here for the controller synthesis. These techniques satisfy basic control requirements such as the stability, the reference signal tracking and the disturbance attenuation. Resulted controller could be tuned with the choice of weighting factors in LQ approach. This work investigates the effect of these factors on control results. Proposed methods are tested on the mathematical model of the isothermal continuous stirred-tank reactor and simulated results are also verified on the real model of the continuous stirred tank reactor. 展开更多
关键词 SIMULATION adaptive control recursive identification linear quadratic(LQ) approach continuous stirred-tank reactor(cstr).
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