合成塔

  • 网络converter;synthesis tower;synthetic tower;synthesizing tower
合成塔合成塔
  1. 层板包扎氨合成塔的安全评定

    Safety Assessment to a Multilayer Ammonia Synthesizing Tower

  2. Φ1400mmNJ型三轴一径氨合成塔运行总结

    Sum-Up of Operation of Φ 1400 mm Type NJ Three Axial-One Radial Ammonia Converter

  3. 基于MATLAB四段冷激式氨合成塔模拟与操作优化

    Simulation and optimization of stage quenching ammonia synthesis converter based on MATLAB

  4. 化工合成塔设备CAD软件开发

    Development of CAD Software for Chemical Tower Equipment

  5. 运用BP网络分析尿素合成塔CO2转化率

    CO_2 Conversion Rate Analysis of Urea Synthesis Tower By Means of BP Network

  6. NC型轴-径向氨(甲醇)合成塔的开发与应用

    Exploitation and Application of NC Type Axial - radial Ammonia ( Methanol ) Synthetic Tower

  7. 基于ANSYS对氨合成塔端盖主螺栓的优化设计

    Optimal Design of the Main Bolt of Top Cover of the Ammonia Converter Based on ANSYS

  8. 浅谈对尿素合成塔CO2转化率的认识&高压液气(汽)管式快速反应器的应用研究

    Discussion on Ratio of Carbon Dioxide Conversion in Urea Reactor : Research on Application of HP Liquid-Gas Tube Reactor

  9. MATLAB在过程计算和Kellogg氨合成塔模拟中的应用

    Application of the MATLAB in course of chemical simulation and calculation

  10. Shell煤气化工艺中甲烷化副反应的控制研究甲醇合成塔的制造工艺

    Influence of Process Conditions on By-reaction of Methanation in Shell Powdered Coal Gasification Process Study on the Fabricating Procedure for Methanol Synthetic Column

  11. 介绍了NC型一轴二径型氨合成塔触媒的钝化方案、过程及经验。

    A presentation is given of the catalyst passivation scheme , course and experience in the Model NC ammonia converter with one axial and two radial beds .

  12. 氨合成塔用Cr-Mo钢的热处理

    Heat Treatment of Cr-Mo Steel Used for Ammonia Synthesis Tower

  13. KBR卧式氨合成塔及催化剂还原

    KBr horizontal ammonia converter and catalyst reduction

  14. S-200型氨合成塔催化剂运行总结

    Summary of the operation of S-200 type synthetic ammonia converter catalyst

  15. JWΦ2000均温型合成塔在8万吨甲醇装置中的应用

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

  16. φ2.8m尿素合成塔上封头衬里缺陷及更换

    Defects of the top head lining of urea converter and its replacement

  17. 结果表明,在氨碳比、水碳比均为4.5,操作温度为190℃时,尿素合成塔CO2转化率可达到55%。

    The result indicates that the ammonia / carbon ratio and water / carbon ratio were both 4.5 , when operating temperature is 190 ℃, the CO_2 conversion rate of urea reactor can reach to 55 % .

  18. φ1000mm甲醇合成塔缠绕钢带的预拉应力分析

    Initial Tensile Stress Analysis of Winding Steel Band of ■ 1000 Methanol Synthetic Column

  19. WWS型尿素合成塔组合内件的研究开发与使用

    Research and Development of Type WWS Composite Internals in Urea Reactor and their Use

  20. 分析了原料气中CO含量对甲醇合成塔生产状况的影响,解释了工厂实际生产中CO含量过高时甲醇合成塔温度控制不稳定的现象;

    The influence of the concentration of CO in feed on the operation situation of the reactor was analyzed quantitatively . The result explained the phenomenon in the factory that the temperature of reactor will be instable as the concentration of CO is high .

  21. 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 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 .

  22. 本文详细介绍了化工合成塔设备CAD软件的特点、功能及开发过程中的关键技术,对基于Windows2000操作系统下AutoCAD2000软件平台上进行专业化CAD软件开发的技术做了深入研究。

    In this thesis , the properties , function and key technology of developing process in chemical tower equipment CAD software are introduced in detail . This professional CAD software is based on AutoCAD 2000 software platform in the Windows 2000 system . And the paper discusses the technology .

  23. NC-41000氨合成塔系统开车总结

    Summary on Trial Run of NC-41000 Ammonia Synthesis Tower System

  24. 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。

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

  25. 结果表明,对于TopsφeS-200型合成塔流体沿流动方向的物料与热量的返混影响不大,气相主体与颗粒外表面存在着一定的温度差和浓度差。

    The results indicate that back mixing of mass and heat alone flow direction for Tops φ e S-200 conveter is negligible , but the differences of concentration and temperature exist between gas bulk and external surface of catalyst .

  26. 以UTI公司的等温合成塔和卡萨利公司开发的高效塔板为例,介绍提高合成塔二氧化碳转化率的技术开发情况。

    With the isothermal reactor internals of UTI and the high-efficiency trays developed by Casale as examples , an introduction is given to the technical development of improving carbon dioxide conversion in the reactor .

  27. SAPV及API579凹坑评定标准用于尿素合成塔的保守度评价

    Conservative Factor Evaluation of Local Thinning Defect Assessment Standard ( SAPV and API579 ) Using in Urea Reactor

  28. HC-1高效金属切削液是以合成塔底油副产物为基料,经多元配伍而成。

    The HC-1 high-efficiency metallic cutting liquid is made up of the byproduct of synthetical tower oil , and comes into form by several ways .

  29. 采用电石转化氢焰色谱法,用TDX-01固定相为分离柱,分析氨合成塔触媒升温还原中水汽浓度。

    Using TDX-01 fixed phase as separator column , the water vapor concentration of catalyst in synthetic converter was determined by hydrogenation gas chromatography .

  30. 传统凯洛格多床氨合成塔的冷激气是采用经121-C换热的出口气,温度为142℃。

    The quench gas of Kellogg multi-bed ammonia converter is the gas from tube-side of heat exchanger 121-C , whose temperature is 142C .