石油炼制与化工
石油煉製與化工
석유련제여화공
PETROLEUM PROCESSING AND PETROCHEMICALS
2014年
12期
38-42
,共5页
王宗波%张孔远%杨康%刘晨光
王宗波%張孔遠%楊康%劉晨光
왕종파%장공원%양강%류신광
碱金属%Pd﹣Au∕Al2 O3 L酸%Pd﹣Au二元合金%异戊二烯
堿金屬%Pd﹣Au∕Al2 O3 L痠%Pd﹣Au二元閤金%異戊二烯
감금속%Pd﹣Au∕Al2 O3 L산%Pd﹣Au이원합금%이무이희
alkali metal%Pd﹣Au∕Al2 O3%Lewis acid%Pd﹣Au binary alloy%isoprene
采用等体积浸渍法制备了不同K2 O、Li2 O 含量的 Pd﹣Au∕Al2 O3催化剂,采用低温氮吸附法、吡啶吸附红外光谱、程序升温还原(H2﹣TPR)等方法进行了表征研究。吡啶吸附红外光谱表征结果表明,催化剂表面只有L酸,无B酸,K2 O改性比Li2 O改性催化剂的表面酸性弱。H2﹣TPR表征结果表明,催化剂表面形成了Pd﹣Au二元合金,加入碱金属改性后,催化剂的还原峰向高温方向移动。以异戊二烯的模型化合物为原料评价了自制的改性Pd﹣Au∕Al2 O3催化剂的选择加氢性能,结果表明:催化剂经过Li2 O 改性后,异戊二烯的转化率和单烯烃选择性提高,而用K2 O改性时,异戊二烯的转化率降低,单烯烃选择性提高;采用K2 O质量分数为1.2%的催化剂,在反应温度为70℃时异戊二烯的转化率为90.0%,单烯烃的选择性为86.0%。
採用等體積浸漬法製備瞭不同K2 O、Li2 O 含量的 Pd﹣Au∕Al2 O3催化劑,採用低溫氮吸附法、吡啶吸附紅外光譜、程序升溫還原(H2﹣TPR)等方法進行瞭錶徵研究。吡啶吸附紅外光譜錶徵結果錶明,催化劑錶麵隻有L痠,無B痠,K2 O改性比Li2 O改性催化劑的錶麵痠性弱。H2﹣TPR錶徵結果錶明,催化劑錶麵形成瞭Pd﹣Au二元閤金,加入堿金屬改性後,催化劑的還原峰嚮高溫方嚮移動。以異戊二烯的模型化閤物為原料評價瞭自製的改性Pd﹣Au∕Al2 O3催化劑的選擇加氫性能,結果錶明:催化劑經過Li2 O 改性後,異戊二烯的轉化率和單烯烴選擇性提高,而用K2 O改性時,異戊二烯的轉化率降低,單烯烴選擇性提高;採用K2 O質量分數為1.2%的催化劑,在反應溫度為70℃時異戊二烯的轉化率為90.0%,單烯烴的選擇性為86.0%。
채용등체적침지법제비료불동K2 O、Li2 O 함량적 Pd﹣Au∕Al2 O3최화제,채용저온담흡부법、필정흡부홍외광보、정서승온환원(H2﹣TPR)등방법진행료표정연구。필정흡부홍외광보표정결과표명,최화제표면지유L산,무B산,K2 O개성비Li2 O개성최화제적표면산성약。H2﹣TPR표정결과표명,최화제표면형성료Pd﹣Au이원합금,가입감금속개성후,최화제적환원봉향고온방향이동。이이무이희적모형화합물위원료평개료자제적개성Pd﹣Au∕Al2 O3최화제적선택가경성능,결과표명:최화제경과Li2 O 개성후,이무이희적전화솔화단희경선택성제고,이용K2 O개성시,이무이희적전화솔강저,단희경선택성제고;채용K2 O질량분수위1.2%적최화제,재반응온도위70℃시이무이희적전화솔위90.0%,단희경적선택성위86.0%。
A series of Pd﹣Au∕Al2 O3 catalysts modified by different amount of alkali metal K or Li were prepared by incipient wetness impregnation and characterized by low temperature nitrogen adsorp﹣tion,FT﹣IR and H2﹣TPR techniques. The isoprene was used to evaluate the selective hydrogenation performance of the modified catalysts. The FT﹣IR results show that only Lewis acid sites exist on the catalysts,no Bronsted acid is found. The acid strength of K﹣modified catalyst is weaker than Li﹣modi﹣fied catalyst. The H2﹣TPR results indicate that Pd﹣Au binary alloy is formed,the reduction peaks of catalysts shift to higher temperature after modified by alkali metals. The reaction results of isoprene se﹣lective hydrogenation on the modified Pd﹣Au∕Al2 O3 catalysts show that the isoprene conversion and iso﹣pentenes selectivity increase when addition of K2 O. The LiO modification reduces the conversion of iso﹣prene but isopentenes selectivity increases. At 70 ℃,isoprene conversion reaches 90. 0%,isopentenes selectivity is 86. 0% on the catalyst Pd﹣Au∕Al2 O3 with 1. 2% K2 O.