搅拌釜

将此方法用于连续反应搅拌釜（CSTR）中和过程pH值控制的仿真试验，仿真结果表明了该方法的有效性。

This method is used for control the pH of neutralization process in continuous stirred tank reactor ( CSTR ) . Simulation shows that this new method is efficient .

连续搅拌釜式反应器的热稳定性问题

On the Stability of the Continuous - flow Stirred Tank Reactor

浆态床搅拌釜中合成反应的结果表明，用氧化铜对脱水催化剂进行改性，能改善催化剂的催化性能，提高CO转化率和产物中二甲醚的选择性，抑制副反应的发生。

The modified dehydration catalyst could increase CO conversion and dimethyl ether selectivity and restrain side reactions .

在双搅拌釜中初步研究了胺溶液吸收CO2反应机理。

Reaction mechanism of CO2 and amines was discussed . This process was studied in a stirred-cell absorber .

采用脉冲法测定了蔗糖水解反应在连续搅拌釜式反应器内的停留时间分布，求得了停留时间分布密度函数E（t）、平均停留时间以及模型参数。

Residence time distribution for sugar hydrolysis reaction in a contineous flow stirred tank reactor was m : asured by pulse input method .

在搅拌釜式间歇反应器中研究了以负载Mg2＋的HD－8型阳离子交换树脂为催化剂的4－OH－TMP非均相氧化反应动力学。

The kinetics of 4-OH-TMP heterogeneous catalytic oxidation reaction catalyzed by ion exchange resin supported Mg2 + was studied .

应用SSTK-ω湍流模型计算Rushton搅拌釜流场

Calculation for Rushton stirred tank with SST k - ω turbulence model

用LDA研究搅拌釜内的流场

Experimental Study on Agitator by LDA

基于连续搅拌釜式反应器（CSTR）的仿真实例验证了该算法的有效性。

The simulation results of fault diagnosis on continuous stired-tank reactor ( CSTR ) prove its validity .

DNT在搅拌釜内液滴大小分布规律的研究

Study of the distribution rule of DNT liquid drop sizes in a agitate reactor

计算流体力学（CFD）是一门用于分析流体流动、传热等现象的学科，CFD能够给出搅拌釜内的总体流动状况和局部详尽信息。

Computational Fluid Dynamics ( CFD ) is used to analyze the fluid flow and heat transfer , which can provide overall flow status and local data in tank .

Cs-137γ射线CT测量标准Rushton搅拌釜气含率分布及数字图像重建弓形降液管内的气含率分布

Measurement of Gas Hold-up Distribution and Digital Color Image Reconstruction for Standard Gas-liquid Rushton Stirred Tank with Cs-137 γ - CT

采用双搅拌釜吸收反应器，对一乙醇胺（MEA）和N-甲基二乙醇胺（MDEA）混合有机胺水溶液吸收模拟烟道气中CO2进行机理研究。

The mechanism study of CO2 absorption from simulated flue gas into aqueous solution of MEA and MDEA has been conducted with a double-stirred-cell absorber .

利用改进的粒子群算法通过优化冷剂流量解决了连续搅拌釜（CSTR）两稳态间的最优过渡问题。

Improved particle swarm has been used optimizing refrigerant flow through a continuous stirred tank settlement between the two optimal steady-state transitions .

间歇操作下由于较高的泰勒数Ta，泰勒反应器中的湍流程度比较高，因此与普通搅拌釜中的结果相差不多。

As Ta is very high and the extent of turbulence in Taylor reactor is very high , the results in Taylor reactor were similar to that in stirring tank .

通过计算流体力学软件FLUENT对带盘管搅拌釜内的非稳态换热过程进行了数值模拟，得到了搅拌釜内流场、温度场和盘管内外两侧平均对流传热系数。

The unsteady heat transfer process in a stirred tank equipped with helical coils was investigated by using software FLUENT . The temperature field and the heat transfer coefficient were obtained .

采用连续搅拌釜式反应器（continuousstirredtankreactor简称CSTR）在常压、30～60℃的温度范围内，对醋酸酐水解反应的宏观动力学进行了探讨。

The main object of this paper is to study the kinetics of the reaction of acetic anhydride hydrolysis in Continuous Stirred Tank Reactor and at the temperature ranging from 30 to 60 ℃ and 1 atm .

提出了一个新的研究CSTR（连续搅拌釜式反应器）热稳定性问题的定态法。

This paper developed a new mathematical model for calculating the thermal stability of the continuous-flow stirred tank reactor ( CSTR ) operating under steady state .

实验表明，增加转速可以显著提高反应速率k，在等比有效功率下，浸没循环撞击流反应器中的化学反应速率常数k明显高于搅拌釜反应器。

The experiments show that the reaction rate k can be significantly improved by increasing the rotational speed in the impinging streams reactor . The reaction rate constant k was significantly higher than that in the stirred reactor at the geometric proportion effective power .

针对一类参数不确定连续搅拌釜式反应釜（CSTR：ContinuesStirred-TankReactors）系统中的参数不确定性，研究了一种基于反步（Backstepping）方法的神经网络自适应控制器。

For a class of CSTR ( Continues Stirred-Tank Reactors ) system with uncertain parameters , the procedure is developed for design of neural adaptive controller based on backstepping approach .

第四步设计了一套800t／a三搅拌釜串联的装置。

In the fourth step , we designed a set of 800-t / a equipment with three agitation-reactors .

运用敏感度方法研究连续搅拌釜式反应器（CSTR）放热反应的参数敏感性行为及规律，探讨CSTR反应器的安全操作区域和敏感操作区域。

The parametric sensitivity behavior and rule of a CSTR are discussed with parametric sensitivity . Safe operation region and runaway reaction region were determined based on the equations of energy balance and mass conservation .

以Hypol工艺聚丙烯反应器为研究对象，建立了连续搅拌釜（CSTR）聚丙烯反应器的动态机理模型，以微分方程组和代数方程组进行描述。

This paper establishes a theoretical dynamic model of Continuous Stirred Tank Reactor ( CSTR ) for propylene polymerization , which consists of several differential equations and algebra equations .

在半连续浆态搅拌釜中，使用NKC-9离子交换树脂细粉作为催化剂，考察了颗粒粒径对异丁烯水合反应速率的影响。

The effect of particle size on reaction rate of isobutene hydration was investigated in the slurry semibatch agitated reactor with fine powder of NKC-9 ion exchange resin .

本文报道了l升浆液搅拌釜内一体化甲醇合成反应过程中涉及的甲醇连续羰基化、甲酸甲酯氢解和低温甲醇合成反应的初步考察结果。

In this paper , continuous carbonylation of methanol , hydrogenolysis of methyl formate ( MeF ) involved in the concurrent synthesis of methanol via MeF were briefly examined in a one liter stirred autoclave .

本文以聚合反应工业中广泛使用的连续搅拌釜CSTR为对象，运用人工智能和模式识别技术，并借助于现代控制理论和模糊数学，对实际CSTR系统的实时智能控制作了研究。

By means of AI Pattern Recognition techniques , and with the help of Modern Control Theory Fuzzy Sets , the real-time intelligent control of a Continuous-Stirred Tank Reactor , which is widely used in the polymerization industry , is studied in this thesis .

论文选用聚醚多元醇（PPG）作为研究介质，借助实验和数值模拟相结合的方法，研究了三层桨搅拌釜内聚合体系气-液两相流的混合特性。

The thesis were investigated the characteristics of gas-liquid mixed for polymerization system in a stirred tank with triple impellers by experimental research and numerical simulation . Polyether polyol ( PPG ) was chosen in this study as a research medium .

在2L的搅拌釜式反应器中，对以正丁基锂（n-BuLi）、THF和环己烷分别为引发剂、调节剂和溶剂的丁二烯/苯乙烯阴离子连续溶液共聚合进行了实验研究。

The anionic solution copolymerization of butadiene / styrene with n-butyllithium ( n-BuLi ) initiator , tetrahydrofuran ( THF ) modifier , and cyclohexane solvent , was studied . The study was carried out experimentally in an agitated tank reactor of 2 liters employing continuous operation mode .

搅拌釜中自浮颗粒悬浮分散的临界搅拌转速

Critical Rotating Speed for Floating Particle Suspension in an Agitated Vessel

加压条件下卧式搅拌釜的气液传质特性

Mass Transfer Characteristics of a Horizontal Agitated Vessel under Pressurized Conditions