化学反应工程与工艺
化學反應工程與工藝
화학반응공정여공예
CHEMICAL REACTION ENGINEERING AND TECHNOLOGY
2014年
5期
458-462
,共5页
白彦波%毛伟%秦越%张伟%王博%吕剑
白彥波%毛偉%秦越%張偉%王博%呂劍
백언파%모위%진월%장위%왕박%려검
1,1,1,2-四氟乙烷%脱氟化氢%三氟乙烯%氟化铝基催化剂
1,1,1,2-四氟乙烷%脫氟化氫%三氟乙烯%氟化鋁基催化劑
1,1,1,2-사불을완%탈불화경%삼불을희%불화려기최화제
1,1,1,2-tetrafluoroethane%dehydrofluorination%trifluoroethylene%aluminum chloride-based catalysts
为了制备具有工业化应用价值的1,1,1,2-四氟乙烷脱氟化氢制备三氟乙烯用催化剂,在固定床反应器上考察了催化剂制备条件如溶剂、沉淀温度、沉淀剂浓度对氟化铝基催化剂性能的影响。结果表明不同制备条件下得到的催化剂均为β-AlF3。当乙醇为溶剂、室温沉淀、氢氟酸浓度为22.5 mol/L时,制得的AlF3催化剂初始活性最高。在反应温度450℃,接触时间3.2(g·s)/mL的条件下,1,1,1,2-四氟乙烷初始转化率达36%,三氟乙烯选择性为100%,运行8 h后催化剂活性保持在26%,选择性为100%。
為瞭製備具有工業化應用價值的1,1,1,2-四氟乙烷脫氟化氫製備三氟乙烯用催化劑,在固定床反應器上攷察瞭催化劑製備條件如溶劑、沉澱溫度、沉澱劑濃度對氟化鋁基催化劑性能的影響。結果錶明不同製備條件下得到的催化劑均為β-AlF3。噹乙醇為溶劑、室溫沉澱、氫氟痠濃度為22.5 mol/L時,製得的AlF3催化劑初始活性最高。在反應溫度450℃,接觸時間3.2(g·s)/mL的條件下,1,1,1,2-四氟乙烷初始轉化率達36%,三氟乙烯選擇性為100%,運行8 h後催化劑活性保持在26%,選擇性為100%。
위료제비구유공업화응용개치적1,1,1,2-사불을완탈불화경제비삼불을희용최화제,재고정상반응기상고찰료최화제제비조건여용제、침정온도、침정제농도대불화려기최화제성능적영향。결과표명불동제비조건하득도적최화제균위β-AlF3。당을순위용제、실온침정、경불산농도위22.5 mol/L시,제득적AlF3최화제초시활성최고。재반응온도450℃,접촉시간3.2(g·s)/mL적조건하,1,1,1,2-사불을완초시전화솔체36%,삼불을희선택성위100%,운행8 h후최화제활성보지재26%,선택성위100%。
The AlF3 catalyst was prepared by the precipitator method to catalyze dehydrofluorination of 1,1,1,2-tetrafluoroethane to trifluoroethylene in the fixed-bed reactor. The effects of preparation conditions on catalyst performance were discussed, including solvent, precipitation temperature and the concentration of hydrofluoric acid. It was concluded that the all catalysts were theβ-AlF3 without regard to preparation conditions. The AlF3, prepared under ethanol as solvent, room temperature and hydrofluoric acid(22.5 mol/L), showed the highest initial activity. Over the catalyst, the initial conversion of 1,1,1,2-tetrafluoroethane reached to 36% with the selectivity of trifluoroethylene about 100% at 450℃, contact time 3.2 (g·s)/mL. After 8 h reaction, the conversion decreased to 26% and the selectivity was still 100%.