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1)  benzene production equipment
制苯装置
2)  phthalic anhydride plant
苯酐装置
1.
Failure Analysis and Treatment of the Turbine-Fan Set of a Phthalic Anhydride Plant;
苯酐装置透平风机机组故障原因分析及处理
2.
Through the modification of switching system in phthalic anhydride plant, the plant had following resalts including optimal operation, lower turning off, enhanced phthalic anhydride yield and economic profit.
通过对苯酐装置切换冷凝系统的改造,达到优化操作、减少停车、提高苯酐收率和经济效益的目的。
3)  ethylbenzene unit
乙苯装置
1.
Optimizing and remoulding of side take - off in benzene circulating tower in ethylbenzene unit;
乙苯装置循环苯塔侧线采出工艺的优化与改造
2.
Simulation calculations for ethylbenzene units with the thir d generation molecular sieve gas phase alkylation were carried out by using ASPE N PLUS soft ware.
采用Aspen Plus稳态流程模拟软件,对采用第三代分子筛气相烷基化制乙 苯的某乙苯装置全流程进行了模拟计算。
4)  Mek-Tol Unit
酮苯装置
1.
Analysis of Producing High-melting Wax at Mek-Tol Unit;
酮苯装置生产高熔点石蜡分析
5)  alkyl benzene unit
烷基苯装置
6)  styrene unit
苯乙烯装置
1.
In order to decrease energy in styrene unit,thermodynamic methods were used to analyze the energy consumption based on the mathematical simulation.
为了降低苯乙烯装置的能耗,在对全流程进行严格数学模拟的基础上,利用热力学方法分析了各单元的能耗数据,分析结果表明装置能耗升高的主要表现是高压蒸汽用量的上升,其原因是乙苯部分苯循环量过高。
2.
By hazard identification of materials,production facilities in styrene unit,this paper analyzes their risk way to enter the outside environment,as well as the external environment caused by environmental impact,develops some simple preventive measures.
通过对苯乙烯装置所涉及物质的风险识别、生产设施的风险识别,分析出这些风险进入外环境的途径以及对外环境造成的环境影响,并制定简单的环境风险防范措施。
3.
This paper introduces model building of CAD-HAZOP and its analysis process in the styrene unit.
介绍了计算机辅助危险与可操作性分析(CAD-HAZOP)建模过程及应用于苯乙烯装置苯塔系统的分析过程。
补充资料:焦炉煤气回收粗苯的富油脱苯装置


焦炉煤气回收粗苯的富油脱苯装置


  72.焦炉煤气回收粗苯的富油脱苯装置
  
说明:补充资料仅用于学习参考,请勿用于其它任何用途。
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