化工进展
化工進展
화공진전
CHEMICAL INDUSTRY AND ENGINEERING PROGRESS
2015年
5期
1307-1310,1344
,共5页
杂质%催化剂%烷烃%异丁烷%脱氢%反应
雜質%催化劑%烷烴%異丁烷%脫氫%反應
잡질%최화제%완경%이정완%탈경%반응
impurities%catalyst%alkane%isobutane%dehydrogenation%reaction
采用固定床法考察了原料异丁烷中乙硫醇、甲醇、正丁烷和1-丁烯等杂质对Pt-Sn-K/Al2O3催化剂上异丁烷脱氢制异丁烯反应性能影响,反应产物使用气相色谱进行分析。实验结果表明,在异丁烷脱氢制异丁烯正常反应条件下,即温度580℃、压力0.1MPa、进料组成H2/i-C4H10(体积比)=2、总空速GHSV =2000h?1、GHSV(i-C4H10)=667h?1,乙硫醇、甲醇、正丁烷和1-丁烯对Pt-Sn-K/Al2O3催化剂的异丁烷转化率和异丁烯选择性均有较大的影响,且杂质含量越高,对催化剂的转化率和选择性影响越大。并对杂质造成催化剂失活的原因进行了分析。
採用固定床法攷察瞭原料異丁烷中乙硫醇、甲醇、正丁烷和1-丁烯等雜質對Pt-Sn-K/Al2O3催化劑上異丁烷脫氫製異丁烯反應性能影響,反應產物使用氣相色譜進行分析。實驗結果錶明,在異丁烷脫氫製異丁烯正常反應條件下,即溫度580℃、壓力0.1MPa、進料組成H2/i-C4H10(體積比)=2、總空速GHSV =2000h?1、GHSV(i-C4H10)=667h?1,乙硫醇、甲醇、正丁烷和1-丁烯對Pt-Sn-K/Al2O3催化劑的異丁烷轉化率和異丁烯選擇性均有較大的影響,且雜質含量越高,對催化劑的轉化率和選擇性影響越大。併對雜質造成催化劑失活的原因進行瞭分析。
채용고정상법고찰료원료이정완중을류순、갑순、정정완화1-정희등잡질대Pt-Sn-K/Al2O3최화제상이정완탈경제이정희반응성능영향,반응산물사용기상색보진행분석。실험결과표명,재이정완탈경제이정희정상반응조건하,즉온도580℃、압력0.1MPa、진료조성H2/i-C4H10(체적비)=2、총공속GHSV =2000h?1、GHSV(i-C4H10)=667h?1,을류순、갑순、정정완화1-정희대Pt-Sn-K/Al2O3최화제적이정완전화솔화이정희선택성균유교대적영향,차잡질함량월고,대최화제적전화솔화선택성영향월대。병대잡질조성최화제실활적원인진행료분석。
Effect of impurities,such as ethyl mercaptan,methyl alcohol,butane and 1-butylene,on the performance of Pt-Sn-K/Al2O3 catalyst in the reaction of isobutane dehydrogenation to isobutene was investigated on a fixed bed reactor,and the product was analyzed by gas chromatography. The results showed that ethyl mercaptan,methyl alcohol,butane and1-butylene all had great influence on the isobutane conversion and isobutene selectivity of Pt-Sn-K/Al2O3 catalyst under the reaction condition of isobutane dehydrogenation to isobutene,i.e. at the temperature of 580℃,pressure of 0.1MPa,feedstock of H2/i-C4H10(V)= 2,total space velocity GHSV= 2000h?1,GHSV(i-C4H10)= 667h?1; and the higher the impurities content was,the greater the influence was. Furthermore,how the impurities caused the deactivation of catalyst was analyzed.