化工进展
化工進展
화공진전
CHEMICAL INDUSTRY AND ENGINEERING PROGRESS
2014年
3期
595-598
,共4页
异氰酸酯%光气回收%优化设计%模拟优化
異氰痠酯%光氣迴收%優化設計%模擬優化
이청산지%광기회수%우화설계%모의우화
isocyanate%phosgene recovery%optimal design%simulation and optimization
传统冷凝回收3-氯-4-甲基苯基异氰酸酯(CMPI)生产装置尾气的方法具有以下不足:不能保证光气完全回收,而一旦光气进入尾气破坏系统,不仅会增加产品的成本,而且还会降低系统安全性、增加碱液消耗和废水排放;文献中研究的甲苯二异氰酸酯装置的尾气回收系统,由于反应条件的不同,不能适用于常压CMPI装置。本文以年产2000 t CMPI常压反应装置为例,对其光气回收系统进行了模拟分析和优化设计,确定了满足工艺要求的最佳理论塔板数为12,最佳吸收剂甲苯用量为780 kg/h。对常压装置与高压装置光气回收系统进行了比较,认为常压装置的光气回收系统需要更多的吸收剂用量,但是不需要在塔中增加中间冷却器,并给出了理论上的解释。考虑异氰酸酯生产工艺的共性,本文研究结论可以推广应用于其他类似异氰酸酯装置。
傳統冷凝迴收3-氯-4-甲基苯基異氰痠酯(CMPI)生產裝置尾氣的方法具有以下不足:不能保證光氣完全迴收,而一旦光氣進入尾氣破壞繫統,不僅會增加產品的成本,而且還會降低繫統安全性、增加堿液消耗和廢水排放;文獻中研究的甲苯二異氰痠酯裝置的尾氣迴收繫統,由于反應條件的不同,不能適用于常壓CMPI裝置。本文以年產2000 t CMPI常壓反應裝置為例,對其光氣迴收繫統進行瞭模擬分析和優化設計,確定瞭滿足工藝要求的最佳理論塔闆數為12,最佳吸收劑甲苯用量為780 kg/h。對常壓裝置與高壓裝置光氣迴收繫統進行瞭比較,認為常壓裝置的光氣迴收繫統需要更多的吸收劑用量,但是不需要在塔中增加中間冷卻器,併給齣瞭理論上的解釋。攷慮異氰痠酯生產工藝的共性,本文研究結論可以推廣應用于其他類似異氰痠酯裝置。
전통냉응회수3-록-4-갑기분기이청산지(CMPI)생산장치미기적방법구유이하불족:불능보증광기완전회수,이일단광기진입미기파배계통,불부회증가산품적성본,이차환회강저계통안전성、증가감액소모화폐수배방;문헌중연구적갑분이이청산지장치적미기회수계통,유우반응조건적불동,불능괄용우상압CMPI장치。본문이년산2000 t CMPI상압반응장치위례,대기광기회수계통진행료모의분석화우화설계,학정료만족공예요구적최가이론탑판수위12,최가흡수제갑분용량위780 kg/h。대상압장치여고압장치광기회수계통진행료비교,인위상압장치적광기회수계통수요경다적흡수제용량,단시불수요재탑중증가중간냉각기,병급출료이론상적해석。고필이청산지생산공예적공성,본문연구결론가이추엄응용우기타유사이청산지장치。
The traditional method of phosgene recovery for 3-chloro-4-methyl phenyl isocyanate (CMPI) equipments has following disadvantages:The phosgene cannot be recovered completely. Once the phosgene goes to the off-gas,there would be some bad consequence such as:the security of system is decrease;the security of system,the cost of production,the consumption of sodium hydroxide and the discharge of waste water are increase. The research in references which studied the phosgene recovery for producing toluene diisocyanate cannot be used in CMPI system for the difference of reactive conditions. An equipment of 2000 t/a for producing CMPI was taken for example,the phosgene recovery system was simulated and optimally designed:Under the condition of meeting the technological requirements,the number of theoretical plates was identified as 12 and the optimal feeding rate was defined as 780 kg/h. We as compared the phosgene recovery systems of normal pressure reactive system and that of high pressure. The results showed that under normal pressure system,the phosgene recovery system needed more absorbent than that of under high pressure,but no intercooler in the absorber was needed and the theoretical explanation for the phenomenon was provided. Considered the generility for various kinds of isocyanate production processes,the conclusion of this study can be applied in other similar isocyanate equipments.