In this paper in view of the thermal stability of fixed-bed reactor maximum tube diameter and temperature difference of heat transfer for low & pressure tube-shell methanol synthesis reactor were calculated .

从固定床反应器的操作热稳定性出发，对管壳式低压甲醇 合成 反应 器的最大允许管径和最大传热温差进行了计算。

Four stage methanol synthesis reactor quenching with feed gas has been established . The direct searching method for calculating optimum operation condition with minimum volume of the catalyst beds has been proposed and the numerical solution has been obtained .

四段原料气冷激 式甲醇 合成 塔催化床的数学模型，并提出了计算最小催化床体积的最优设计工况的直接搜索法，求得了数值解。

The Study to the Prereduction Technology of Whole Catalyst in the Ammonia Synthesis Reactor

氨 合成 塔内件中催化剂整体预还原技术的研究

After profound studying the kinetics ( including macro and intrinsic ) the principle for synthesis reactor design was determined .

对反应的动力学（包括宏观动力学及微观动力学）进行深入的研究，初步确定 反应 器设计原则。

Cation-exchange membrane is a important constitutent part of electrochemical synthesis reactor .

阳离子交换膜是电 合成 反应 器的重要组成部分。

This paper is a technical study to the prereduction technology of whole catalyst in the ammonia synthesis reactor .

本文总结了六台Φ500氨 合成 塔内件中A（110-2）型催化剂的整体预还原技术的工业性 试验及实验室 试验研究的情况。

Taking the typical three-tube co-current ammonia synthesis reactor in a middle-size ammonia synthesis plant of our country as an example the mathematical models of the reactor were employed to simulate the reactor operation calculation .

以我国中型合成氨厂典型的三套管并流式氨 合成 反应 器为例，采用反应器数学模型模拟反应器操作计算。

Analysis and Modeling of the Methanol Synthesis Reactor

联醇 合成 塔 反应 器分析与模拟

Design of shell for 300kt / a ammonia synthesis reactor

300kt/a氨 合成 塔外壳的设计

Digestion high-pressure tank also known as hydrothermal synthesis reactor pressure melting shells can digest .

高压消解罐，也称为水热 合成 釜、压力溶弹、消化罐。

Research of model and estimate of parameters for axial - Radial Ammonia Synthesis Reactor

双层中间换热径向式氨 合成 反应 器参数估计和数学模拟

Optimal temperature-time policy of ethylene oxide synthesis reactor

环氧乙烷 合成 反应 器温度-时间优化策略

The temperature and Ammonia concentration distribution in the packed bed were calculated by pseudo-homogeneous phase two-dimensional model for Ammonia synthesis reactor . The calculating results indicated that the distribution of the void fraction and flow velocity along radial direction have great influence on the temperature and Ammonia concentration distribution .

采用拟均相二维模型计算了固定床 反应 器的温度和浓度分布，结果表明，床层空隙率和速度分布对床层的径向温度分布和浓度分布影响较大。

In this paper study was carried out to design synthesis reactor and chose the optimal parameters of operation aiming at enlarging production capacity and increasing yield .

本文对 合成 反应 器的设计和最佳的操作条件进行了研究，以期提高生产规模与产品收率。

The one-dimensional model of Lurgi tude-shell type methanol synthesis reactor has been established .

建立了鲁奇式甲醇 合成 塔完整的双速率一维模型。

Dynamic simulation of lurgi methanol synthesis reactor

Lurgi型甲醇 合成 反应 器的动态模拟

Choosing the reactions of hydrogenation of CO and CO_2 as two key reactions of methanol synthesis the mathematical model of multiple-stage quenching-with-feed-gas type methanol synthesis reactor has been established .

以CO、CO2平行加H2为甲醇合成的关键反应，以CO、CO2作为关健反应组分，建立了多段原料气冷激型甲醇 合成 塔 催化 床的一维拟均相数学模型。

Chromatographic analysis of methanol content in the inlet gas of a methanol synthesis reactor

甲醇 塔入口气体中甲醇含量的色谱分析

Two-Dimensional Mathematical Model of Tube-Shell Type Dimethyl Ether Synthesis Reactor from Syngas

管壳型二甲醚 合成 反应 器的二维数学模型

Cause analysis and solutions of mechanical seal leakage of synthesis reactor

合成 釜机械密封泄漏原因分析及改造措施

Detection of Urea Synthesis Reactor 's Leaking with Ammonia Infrared Analysis

氨红外分析检测尿素 合成 塔泄漏

Maximum Tube Diameter and Temperature Difference of Heat Transfer for Tube-shell Methanol Synthesis Reactor

管壳式 甲醇含 成 反应 器的最大允许管径和最大传热温差

Application of JW Φ 2000mm low pressure-uniform temperature type methanol synthesis reactor in a 80 / y unit

JWΦ2000均温型 合成 塔在8万吨甲醇装置中的应用

Load Calibration and Process Analysis of PA Synthesis Reactor

苯酐 反应 器负荷的标定及工艺分析

The work of this paper can provide theoretical basis for further study of heat transfer mechanism and reaction performance in the fixed-bed methanol synthesis reactor .

本研究结果可以为更好的理解甲醇 合成 过程的传热规律和反应现象提供理论依据。

Transformation of high effective boards in the urea synthesis reactor from Casale in Switzerland and its benefit were introduced in the paper .

介绍了采用瑞士 Casale公司高效塔板对尿素 合成塔进行的改造，以及改造后产生的效果。

The developing status of world large-scale methanol production technology is analyzed and Linda 's JW low-pressure methanol synthesis reactor with uniform temperature is described .

分析了国内外甲醇大型化技术发展现状，介绍了林达成功开发的JW低压均温型甲醇 合成 塔。

The pseudo-homogeneous two-dimensional model considered the radial distribution of velocity for the cooling-tube type methanol synthesis reactor is established and the radial concentrations and temperature profiles of the bed are given .

本文考虑床层径向流速分布，建立了冷管型甲醇 合成 塔的拟均相二维模型，得出床层径向温度与浓度分布。

Dynamic Simulation of Phosgene Synthesis Reactor

光气 合成 反应 器动态仿真

Temperature Control in the Synthesis Reactor of O-Cresol

邻甲酚 合成 反应的温度控制