synthesis reactor

Synthesis of Reactor Network Based on Derivative Analysis

基于导数分析的反应器网络综合方法

Application of JW Φ 2000mm low pressure-uniform temperature type methanol synthesis reactor in a 80,000t/ y unit

JWΦ2000均温型合成塔在8万吨甲醇装置中的应用

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。

The dynamic simulation technology of tube reactor of phosgene synthesis has been studied in this paper.

该文对光气合成管式反应器的动态仿真技术进行了研究.

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.

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。

Targeting Strategies Method Based on CSTR Model in Reactor Network Synthesis

基于CSTR的反应器网络综合目标策略法

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。

The kinetics of the dimethyl ether ( DME) synthesis from syngas containing N2 over a bifunctional catalyst of methanol synthesis catalyst and methanol dehydration catalyst have been investigated under 3-7 MPa and 220-260C, the reactor was a tubular flow integral reactor.

研究了由商业甲醇合成催化剂和改性分子筛脱水催化剂混合组成的双功能催化剂上含氮合成气一步法制取二甲醚的本征动力学。实验是在3-7Mpa、220-260℃条件下进行的。

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。

Optimization and Analysis of Inner Part Stability for the Methanol Synthesis Reactor

甲醇塔内件稳定性操作分析及优化

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 Research Progress of the Non-isothermal Reactor Network Synthesis Based on Environment

环境友好的非等温反应器网络综合研究进展

Mathematical simulation and operating conditions analysis of Lurgi methanol synthesis reactor(ⅰ) lurgi tube-shell type methanol synthesis reactor

鲁奇甲醇生产装置数学模拟和工况分析&（Ⅰ）鲁奇副产蒸汽管壳型甲醇合成塔

Partition Strategy of Reactor Network Synthesis Based on Objective Function and It's Application

基于目标的反应器网络综合分区策略及其应用

Mathematical Modeling and Comparison of Lurgi Tube-shell Type Methanol Reactor with by-Product Steam and I.C.I. Four Stage Quench Type Methanol Synthesis Reactor II. Mathematical modeling and optimization of four stage methanol synthesis reactor

鲁奇副产蒸汽管壳型和I.C.I.四段冷激式甲醇合成塔的数学模拟和比较Ⅱ、四段原料气冷激甲醇合成塔的数学模拟及最佳化