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循环反应器     
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  recycle reactor
     Calculation of Recycle Reactor for Synthesis of Trioxymethylene with Amberlyst-15 Catalyst
     Amberlyst-15催化剂合成三聚甲醛循环反应器的计算
短句来源
     ANALYSIS OF THE BACKMIXING'S INFLUENCE ON THE PRODUCT DISTRIBUTION WITH RECYCLE REACTOR
     用循环反应器分析返混对产物分布的影响
短句来源
     In this article,ethylene hydrogenation over Pt-Sn/A1_2O_3 catalyst is used asthe model reaction. The kinetic models and parameter discrimination of steadystate and non-steady state reactions are studied using external recycle reactor anddifferential pulse reactor,respectively;
     以Pt-Sn/Al_2O_3催化剂上的乙烯加氢反应为模型反应,用外循环反应器和微脉冲反应器研究了稳态和非稳态反应的动力学模型及其分辨。
短句来源
     The kinetics of the vapor phase catalytic oxidation of toluene over V-H-3 catalyst has been studied in a vibrative internal recycle reactor.
     应用振动式内循环反应器进行了在V-H-3型催化剂上甲苯气相催化氧化合成苯甲醛的动力学研究。
短句来源
     Research on the recycle ratio of recycle reactor
     循环反应器中循环比的研究
短句来源
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  loop reactor
     The characteristics of the sludge in high performance inner loop reactor
     高效内循环反应器的污泥特性
短句来源
     Gas holdup and liquid circulation in an internal airlift loop reactor were investigated.
     研究了气升式内循环反应器内的气含率与液体循环 .
短句来源
     Application of Jet Loop Reactor in Sewage Treatment
     喷射式循环反应器在污水处理中的应用
短句来源
     Gas Holdup and Liquid Circulation in an Internal Airlift Loop Reactor
     气升式内循环反应器内的气含率与液体循环(英文)
短句来源
     Characteristics of Carring Biofilm and Suspended Activated Sludge in Airlift Loop Reactor For Wastewater Treatment
     气提式循环反应器生物膜与游离活性污泥处理污水的特点
短句来源
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  circulation reactor
     Modeling of Gas Entrainment in A Gas-Liquid Circulation Reactor
     气液内循环反应器的气体夹带模型
短句来源
     The influence of internal diffusion of benzene on the kinetics of complete oxidation of benzene over Pt/Al2O3 catalyst has been investigated by the external circulation reactor. The reaction took place in the kinetic region when the catalyst with 0. 45-0. 60 mm was used.
     在Pt/Al_2O_3催化剂上用外循环反应器研究了内扩散对苯完全氧化动力学的影响,当用30~40目(即0.45~0.60mm)催化剂时反应在动力学区域进行.
短句来源
     Nnanometer CaCO_3 product with the size of 30~40 nm was prepared by using vortex and internal circulation reactor.
     采用涡旋内循环反应器制备出了粒径为30~40nm的纳米碳酸钙产品。
短句来源
     Design and Making Method of a Experimental Facility of Additional Gas Internal Circulation Reactor
     试验用附加气厌氧内循环反应器的设计与制作
短句来源
     The different types of reactor for hydrogenation such as reactor with complex agitator, ring type reactor, circulation reactor, horizontal continual hydrogenation reactor and three phase fixed bed reactor are also reviewed.
     还介绍了带复合式搅拌器的加氢反应釜、环式加氢反应器、循环反应器、卧式连续加氢反应器和三相固定床反应器。
短句来源
  recirculation reactor
     Optimization calculation for the recirculation reactor
     循环反应器的最优化计算
短句来源
     The macro-kinetics of the F-T synthesis in the CO+H_2 two-stage process for making gasoline is studied on a potassium-promoted precipitted Fe catalyst with industrial size in an internal recirculation reactor.
     该工作为CO+H_2两段法合成汽油工艺中的一般F-T合成宏观反应动力学研究。 采用原颗粒Fe-Cu—K沉淀铁催化剂与内循环反应器
短句来源
     The kinetics of the reaction was studied using the internal recirculation reactor permitting to eliminate temperature and concentration gradient Studies were performed in the temperature range of 380~465℃ at concentration or sulfur diokiodce mole fraction Xso2=2%~7%.
     用无梯度内循环反应器进行SO2氧化动力学研究.实验温度为380~465℃;
短句来源
     The circulating ratio of the recirculation reactor,which is widely applied to homogeneous reaction,reflects the macroscopical mixing degree of the substances,and utilizing optimum circulating ratio can effectively adjust the concentration of the substance at the reactor entrance and reduce the reactor volume and the equipment investment.
     循环反应器广泛应用于均相反应,其循环比反映了物料的宏观混合程度,是反应器设计的重要参数。 采用适宜的循环比可以有效地调整物料的反应器进口浓度、降低反应器体积和设备投资。
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  recycle reactor
Calculation of State Parameters for a Consecutive-Parallel Second-Order Reaction Performed in a Well-Stirred Recycle Reactor
      
Continuous production of lactic acid in a cell recycle reactor
      
Continuous production of lactic acid from glucose and lactose in a cell-recycle reactor
      
Continuous l-carnitine production from crotonobetaine was studied in a cell-recycle reactor with Escherichia coli O44 K74 as biocatalyst.
      
Continuous production of l(+)-tartaric acid from cis-epoxysuccinate using a membrane recycle reactor
      
更多          
  loop reactor
Hydrodynamics and mass transfer in a modified three-phase airlift loop reactor
      
This configuration has likewise been developed into many different forms, including: (a) Concentric tube airlift (2); (b) external loop airlift (3); (c) jet loop reactor (4); and (d) propeller loop reactor (4).
      
To optimize the fed-batch processes of glycerol fermentation in different reactor states, typical bioreactors including 500-mL shaking flask, 600-mL and 15-L airlift loop reactor, and 5-L stirred vessel were investigated.
      
Flow mixing model of liquid phase in an internal airlift loop reactor
      
Residence time distribution (RTD) analysis of liquid phase was conducted in an internal airlift loop reactor (AL) and a bubble column (BC) with the tracer response technique.
      
更多          
  circulation reactor
An improved flow circulation reactor with reaction mixture quenching was used to study the direct oxidation of methane to formaldehyde at 600-770°C, a CH4/O2 volume ratio of 1: 1 in the starting mixture, and gas mixture flow rates of 0.4-2.0 l/h.
      
Influence of external circulation on sludge characteristics during start-up of internal circulation reactor
      
Rate constant of the three-body recombination of fluorine atoms in a closed flow circulation reactor has been measured using ESR data at T=77 K and pressures ranging within 133-532 Pa.
      
Kinetic regularities in catalytic disproportionation of methanethiol to dimethyl sulfide and hydrogen sulfide have been studied in a flow circulation reactor.
      
Kinetic studies of tetrahydrofuran reaction with H2S were carried out in a flow-circulation reactor.
      
更多          
  recirculation reactor
subtilis (Konecny and Voser, 1977) in three types of reactors: A stirred tank and recirculation reactor, both operated in the batch mode under pH-stat conditions, and a continuous packed bed, operated with excess buffer in the feed.
      
The oxidation of propylene with air on silver catalysts of macropore structure has been studied both in a flow and an open recirculation reactor.
      
Catalytic conversions of diethylsilane (E2), triethylsilane (E3) and diethyldimethylsilane (E2M2) were examined at 373-573 K in a closed recirculation reactor by using various solid acid and base catalysts.
      
Temperature dependence in the 323-373 K temperature range in a pulse system was investigated, while a static recirculation reactor was used for hydrogen pressure dependence measurements.
      
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