本文阐述了醚化反应器的特点及其动力学反应器的计算方法，并分析了影响醚化反应器的主要因素。
The properties of methyltertiarybutyl ether reactor and the calculation methods of the kinetic reactor are introduced. The major factors which effect the reactor are analyzed.
本文介绍了当前多相光催化反应体系中反应动力学模型以及反应器数模研究领域内的主要方法及成果。
This article introduces the main existing methods and achievements in the field of the math models of reaction kinetics and reactor of the heterogeneous photocatalysis reaction system.
引入莫诺特方程建立了反应器基质降解的数学模型，并测出其动力学参数。
Using monod equation built mathematical model describing organic compound degradation in reactor and measured its dynamics parameters.
采用自行研制的微分型种分反应器，在较为单一的条件下了研究铝酸钠溶液中的晶体长大动力学。
The kinetics of crystal growth was studied with a self-designed differential reactor that can be performed on a relatively single condition.
与L - h模型相比较微观动力学在反应器的设计模拟工作中有更广的适用范围。
The application range of micro kinetics is wider than L-H model in simulation design of reactors.
采用固定床恒温积分反应器，对YS—6型银催化剂进行乙烯氧化本征动力学研究。
Research for intrinsic kinetics of ethylene oxidation on the YS-6 Silver Catalyst is done by using a fixed bed constant temperature integral reactor.
在建立合适的对二甲苯氧化反应动力学基础上，对工业氧化反应器进行了模拟计算。
Simulation calculation was carried out on industrial oxidation reactor on the basis of building a suitable para-xylene oxidation reaction kinetics.
在固定床加压反应器和加压热天平上，对五种中国气化用煤及其煤焦进行了加氢气化的动力学研究。
Kinetic characteristics of hydrogasification for five Chinese coals and their chars are investigated at pressure using a fixed-bed reactor and a thermobalance.
描述了在批式反应器和连续流搅拌反应器(CSTR)中酶动力学拆分对映异构体的不同之处。
The difference between a continuous stirred tank reactor (CSTR) and a batch reactor was analyzed for the enzymatic kinetic resolution of enantiomers.
常压下使用等温积分反应器研究了B110中温变换反应的本征动力学模型。
The intrinsic kinetic model of shift reaction over B110 high-temperature shift catalyst has been investigated in an isothermal integral-reactor.
可以对小规模的催化反应器进行透彻的研究并分析动力学速率数据来求得本征反应速率。
Small-scale catalyst reactors can be tested thoroughly and the kinetic rate data analyzed to provide the intrinsic reaction rate.
以C100型阳离子交换树脂作为催化剂，在间歇搅拌釜式反应器中测定了甲醇和醋酸合成醋酸甲酯的本征反应动力学。
The main work is as followings:The kinetics of the synthesis of methyl acetate was measured in a batch stirred reactor with C100 cation exchange resin as catalyst.
中浓纸浆在升流式反应器中的流体动力学性能影响到反应器的反应质量和反应器前后设备的设计及选型。
The flow dynamics property of medium consistency pulp in up-flow re actor affects the reaction quality and design and selection of the devices prior to and after the reactor.
采用积分反应器，研究了吡啶氯化反应中催化剂失活动力学。
The catalyst deactivation kinetics of pyridine chlorination was investigated in an integral fixed reactor.
温度动力学基于反应器的热量平衡。
The temperature model was based on a heat balance of reactor.
论文对中试反应器有机物去除动力学进行了分析。
The kinetics of organics treatment of the pilot-scale reactor was analyzed finally.
采用等温积分反应器，测试了KD306型耐硫甲烷化催化剂的本征动力学，建立了幂函数动力学模型。
The intrinsic kinetics of KD306 type sulfur tolerant methanation catalyst was studied in an isothermal integrated reactor and the reaction model of power functions type was established.
本文针对催化裂化工业装置的提升管反应器以三集总催化裂化反应动力学模型为基础，利用工业装置的现场数据对模型中的参数进行了拟合。
Based on three lumping kinetic model of catalytic cracking, the parameters in the model are estimated with actual operation data of a commercial catalytic cracking riser.
本文根据AAFEB反应器特性，建立了AAFEB反应器的过程动力学模型。
Based on characteristic of AAFEB reactor, the process kinetic models of AAFEB reactor have been developed in this paper.
通过运用新型的内环流反应器对氯化苄光氯化反应机理和宏观状态的分析，建立了氯化苄氯化的连串反应动力学模型。
The kinetic model of consecutive reaction for chlorination of benzyl chloride was built by analyzing the reaction mechanism and macroscopic stage.
在直流流动积分反应器中常压下研究了C207催化剂甲醇分解反应本征动力学。
The intrinsic kinetics of the methanol decomposition at atmospheric pressure over C207 catalyst are studied in a tubular-flow integral reactor.
本文涉及的循环反应器，其循环比r的取值与反应类型、动力学方程、操作条件、实验数据等因素有关。
In this article the circle ratio of circle reactor relates to reaction type, kinetics equation, operation conditions and experimental data.
从探讨丙烯聚合工艺中环管反应器流体动力学模型着手，介绍环管反应器循环泵功率的计算方法。
A fluid dynamical model of the materials in a loop reactor for polypropylene production is suggested and the power of the circulating pump of the reactor is calculated by means of Newitt correlation.
研究了在复合环流反应器中，用络合铁催化剂液相催化氧化脱除H2S的吸收反应动力学、催化剂再生反应动力学及吸收-再生反应联合动力学。
The reactors were applied to liquid-phase-reactive absorption of H2S with ferric coordination compound as catalyst. Kinetics of reactive absorption and catalyst regeneration were investigated.
在体积10L的静态反应器中研究了水合物分解动力学，考察了储存温度和水合物量等因素对水合物分解的影响。
The effects of temperature and hydrate quantity on the dissociation kinetics of methane hydrate were studied in a 10 L quiescent reactor.
在等温积分反应器中研究了操作条件对甲醇合成反应的影响以及C307催化剂上甲醇合成反应的本征动力学。
The intrinsic kinetics and effects of operational conditions on methanol synthesis over the C307 catalyst were investigated.
反应器的设计使用了各个领域的信息，知识和经验，比如热力学，化学动力学，流体力学，传热，传质，和经济学。
D1 Reactor design uses information, knowledge, and experience from a variety of areas thermodynamics, chemical kinetics, fluid mechanics, heat transfer, mass transfer, and economic.
本文采用等温管式微分反应器，研究了常压下在NBC - 1型铁系无铬催化剂上CO变换反应的本征动力学。
In this paper, the intrinsic kinetics of CO shift reaction on NBC-1 type non-chromium iron-based catalysts at ambient pressure is studied by means of isothermal tube-type differential reactor.
本文采用等温管式微分反应器，研究了常压下在NBC - 1型铁系无铬催化剂上CO变换反应的本征动力学。
In this paper, the intrinsic kinetics of CO shift reaction on NBC-1 type non-chromium iron-based catalysts at ambient pressure is studied by means of isothermal tube-type differential reactor.
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