天然气化工
天然氣化工
천연기화공
NATURAL GAS CHEMICAL INDUSTRY
2010年
1期
1-5,12
,共6页
户倩倩%谭猗生%韩怡卓%满建明
戶倩倩%譚猗生%韓怡卓%滿建明
호천천%담의생%한이탁%만건명
二甲醚制低碳烯烃%低碳烯烃制汽油%热力学计算%正辛烷%对二甲苯%平衡组成
二甲醚製低碳烯烴%低碳烯烴製汽油%熱力學計算%正辛烷%對二甲苯%平衡組成
이갑미제저탄희경%저탄희경제기유%열역학계산%정신완%대이갑분%평형조성
DME to lower olefins%lower olefins to gasoline%thermodynamic calculation%n-octane%p-xylene%equilibrium composition
采用原子矩阵法确定了二甲醚经低碳烯烃制正辛烷和对二甲苯的独立反应数,并通过建立平衡关系,采用文献介绍方法,计算了各个反应的反应热、平衡常数及反应平衡时的平衡组分浓度.经分析表明,反应属放热反应;模型中绝大多数反应能自发进行,并且平衡转化率较高;低温高压有利于正辛烷的生成,而低温低压有利于对二甲苯的生成;丙烯生成正辛烷和对二甲苯的转化率远高于乙烯和丁烯,因此控制中间产物丙烯的含量有利于控制目的产物的产出.
採用原子矩陣法確定瞭二甲醚經低碳烯烴製正辛烷和對二甲苯的獨立反應數,併通過建立平衡關繫,採用文獻介紹方法,計算瞭各箇反應的反應熱、平衡常數及反應平衡時的平衡組分濃度.經分析錶明,反應屬放熱反應;模型中絕大多數反應能自髮進行,併且平衡轉化率較高;低溫高壓有利于正辛烷的生成,而低溫低壓有利于對二甲苯的生成;丙烯生成正辛烷和對二甲苯的轉化率遠高于乙烯和丁烯,因此控製中間產物丙烯的含量有利于控製目的產物的產齣.
채용원자구진법학정료이갑미경저탄희경제정신완화대이갑분적독립반응수,병통과건립평형관계,채용문헌개소방법,계산료각개반응적반응열、평형상수급반응평형시적평형조분농도.경분석표명,반응속방열반응;모형중절대다수반응능자발진행,병차평형전화솔교고;저온고압유리우정신완적생성,이저온저압유리우대이갑분적생성;병희생성정신완화대이갑분적전화솔원고우을희화정희,인차공제중간산물병희적함량유리우공제목적산물적산출.
The number of independent reactions of dimethyl ether (DME) to n-octane and p-xylene via light olefins was obtained by atomic matrix method. Reactions heat, equilibrium constants, equilibrium relationships among the products of all those reactions were calculated through building equilibrium relationships with the methods from literatures. The results show that most of the reactions are exothermic reactions. Most of the reactions in models could proceed spontaneously with high equilibrium conversion. Low temperature and high pressure are beneficial to improve the yield of n-octane, but low temperature and low pressure are beneficial to improve the yield of p-xylene; conversion rates of propylene to n-octane and p-xylene were higher than that to ethane and butylene. The product yield could be improved through controlling the content of propylene.