催化学报
催化學報
최화학보
CHINESE JOURNAL OF CATALYSIS
2015年
6期
806-812
,共7页
刘璞生%张忠东%贾明君%高雄厚%于吉红
劉璞生%張忠東%賈明君%高雄厚%于吉紅
류박생%장충동%가명군%고웅후%우길홍
催化裂化%ZSM-5分子筛%渣油%辛烷值
催化裂化%ZSM-5分子篩%渣油%辛烷值
최화열화%ZSM-5분자사%사유%신완치
Catalytic cracking%ZSM-5 zeolite%Residue oil%Octane number
采用不同方法表征了硅铝比(SiO2/Al2O3)为33、266和487的质子型ZSM-5分子筛,并研究了ZSM-5分子筛作为助催化剂在渣油裂解中的应用。与USY分子筛基催化剂混合后,在固定流化床上,评价了ZSM-5分子筛助催化剂的催化裂化性能。研究发现,提高ZSM-5分子筛硅铝比,可以有效抑制混合催化剂对汽油烯烃的裂解,从而避免了汽油烷烃的大量损失。加入ZSM-5助催化剂后,伴随着液化气(LPG)产率的增加,异丁烷和异戊烷产率增加,这可能是由USY基催化剂和ZSM-5助催化剂的综合效应引起的。汽油烷烃和芳烃含量的变化,引起了汽油辛烷值的增加。高硅铝比ZSM-5分子筛(硅铝比为266和487)不仅可以显著改善汽油的辛烷值,而且有效避免了汽油的大量损失。催化汽油辛烷值的改善主要是由于高硅铝比ZSM-5分子筛具有适宜的芳构化和异构化活性,这些变化主要源于高硅铝比ZSM-5分子筛小的孔道直径和适宜的酸性。
採用不同方法錶徵瞭硅鋁比(SiO2/Al2O3)為33、266和487的質子型ZSM-5分子篩,併研究瞭ZSM-5分子篩作為助催化劑在渣油裂解中的應用。與USY分子篩基催化劑混閤後,在固定流化床上,評價瞭ZSM-5分子篩助催化劑的催化裂化性能。研究髮現,提高ZSM-5分子篩硅鋁比,可以有效抑製混閤催化劑對汽油烯烴的裂解,從而避免瞭汽油烷烴的大量損失。加入ZSM-5助催化劑後,伴隨著液化氣(LPG)產率的增加,異丁烷和異戊烷產率增加,這可能是由USY基催化劑和ZSM-5助催化劑的綜閤效應引起的。汽油烷烴和芳烴含量的變化,引起瞭汽油辛烷值的增加。高硅鋁比ZSM-5分子篩(硅鋁比為266和487)不僅可以顯著改善汽油的辛烷值,而且有效避免瞭汽油的大量損失。催化汽油辛烷值的改善主要是由于高硅鋁比ZSM-5分子篩具有適宜的芳構化和異構化活性,這些變化主要源于高硅鋁比ZSM-5分子篩小的孔道直徑和適宜的痠性。
채용불동방법표정료규려비(SiO2/Al2O3)위33、266화487적질자형ZSM-5분자사,병연구료ZSM-5분자사작위조최화제재사유렬해중적응용。여USY분자사기최화제혼합후,재고정류화상상,평개료ZSM-5분자사조최화제적최화열화성능。연구발현,제고ZSM-5분자사규려비,가이유효억제혼합최화제대기유희경적렬해,종이피면료기유완경적대량손실。가입ZSM-5조최화제후,반수착액화기(LPG)산솔적증가,이정완화이무완산솔증가,저가능시유USY기최화제화ZSM-5조최화제적종합효응인기적。기유완경화방경함량적변화,인기료기유신완치적증가。고규려비ZSM-5분자사(규려비위266화487)불부가이현저개선기유적신완치,이차유효피면료기유적대량손실。최화기유신완치적개선주요시유우고규려비ZSM-5분자사구유괄의적방구화화이구화활성,저사변화주요원우고규려비ZSM-5분자사소적공도직경화괄의적산성。
Three proton-type ZSM-5 zeolites with different SiO2/Al2O3 ratios (SARs) of 33, 266, and 487 were characterized and examined as fluid catalytic cracking catalyst additives for residue oil cracking. The catalytic performance of the ZSM-5 additives was evaluated using an ultra-stable Y-zeolite (USY)-based fluid catalytic cracking catalyst in a fixed fluid bed unit. As observed, the cracking of primary olefins over the hybrid catalysts consisting of USY-based catalyst and ZSM-5 additive was considerably inhibited by increasing the SAR of the ZSM-5 zeolite, thus avoiding substantial loss of gasoline paraffins. The introduction of ZSM-5 additives led to higher liquid petroleum gas yields as well as higher isobutane and isopentane yields. The improved yields were attributed to the com-bined effects of the ZSM-5 additives and USY-based catalyst. The variations of gasoline paraffins and aromatics both accounted for the enhancement in the octane number values. The use of ZSM-5 with higher SARs (266 and 487) led to an enhancement in the octane number with minimal loss of gaso-line. This enhancement was mainly attributed to the moderate aromatization and isomerization reactivity of the ZSM-5 additives that mainly originated from their relatively small pores and suita-ble acidic properties with higher SARs.