石油炼制与化工
石油煉製與化工
석유련제여화공
PETROLEUM PROCESSING AND PETROCHEMICALS
2014年
7期
7-12
,共6页
王斌%高雄厚%李春义%山红红
王斌%高雄厚%李春義%山紅紅
왕빈%고웅후%리춘의%산홍홍
催化裂化%协同作用%质子裂化%预裂化
催化裂化%協同作用%質子裂化%預裂化
최화열화%협동작용%질자열화%예열화
catalytic cracking%synergistic effect%protolytic cracking%preliminary crackin g
在固定床反应器上,以磷酸改性的含氧化铝高岭土材料为基质,以 ReUSY 为分子筛组分,通过基质与分子筛分层填装以及部分机械混合的方式,考察不同装填顺序及混合程度对产品分布的影响,研究了催化裂化催化剂基质与分子筛之间的相互作用以及重油分子裂化反应历程。试验结果表明:基质对于重油大分子存在预裂化作用,重油分子首先与基质接触时,其转化率以及总液体收率均高于先经过分子筛体系;分子筛与基质各自所具备的特点均无法有效促使重油分子转化,当二者相互混合、共同作用于重油裂化时,目的产物收率明显增多且氢的分配也更为合理,说明基质与分子筛表面活性位存在良好的协同关系;基质及分子筛表面发生的重油裂化反应以经典裂化机理为主,但存在质子裂化路径。
在固定床反應器上,以燐痠改性的含氧化鋁高嶺土材料為基質,以 ReUSY 為分子篩組分,通過基質與分子篩分層填裝以及部分機械混閤的方式,攷察不同裝填順序及混閤程度對產品分佈的影響,研究瞭催化裂化催化劑基質與分子篩之間的相互作用以及重油分子裂化反應歷程。試驗結果錶明:基質對于重油大分子存在預裂化作用,重油分子首先與基質接觸時,其轉化率以及總液體收率均高于先經過分子篩體繫;分子篩與基質各自所具備的特點均無法有效促使重油分子轉化,噹二者相互混閤、共同作用于重油裂化時,目的產物收率明顯增多且氫的分配也更為閤理,說明基質與分子篩錶麵活性位存在良好的協同關繫;基質及分子篩錶麵髮生的重油裂化反應以經典裂化機理為主,但存在質子裂化路徑。
재고정상반응기상,이린산개성적함양화려고령토재료위기질,이 ReUSY 위분자사조분,통과기질여분자사분층전장이급부분궤계혼합적방식,고찰불동장전순서급혼합정도대산품분포적영향,연구료최화열화최화제기질여분자사지간적상호작용이급중유분자열화반응역정。시험결과표명:기질대우중유대분자존재예열화작용,중유분자수선여기질접촉시,기전화솔이급총액체수솔균고우선경과분자사체계;분자사여기질각자소구비적특점균무법유효촉사중유분자전화,당이자상호혼합、공동작용우중유열화시,목적산물수솔명현증다차경적분배야경위합리,설명기질여분자사표면활성위존재량호적협동관계;기질급분자사표면발생적중유열화반응이경전열화궤리위주,단존재질자열화로경。
The synergy of zeolite and matrix and the VGO cracking routes were studied by a fixed-bed reactor in which ReUSY zeolite and phosphoric acid modified alumina kaolin as matrix were loaded in different layered or mixed packing ways. It is observed that contacting the matrix first for heavy oil results in a higher conversion compared with that of contacting zeolite first. However,neither the molec-ular sieve nor the matrix along can make the heavy oil convert effectively. This indicates the preliminary cracking functions of the matrix,resulting in synergistic effect of zeolite and matrix. With the mixing degree of zeolite and matrix increase,the conversion and the liquid product yield rises significantly, while the yields of dry gas and coke decrease slightly. The synergy effect of mixing zeolite and matrix was also discussed in view of the hydrogen distribution in dry gas and LPG products. The data obtained in this work well fit the classic cracking mechanism,but existing protolytic cracking path which contrib-utes to a rise in dry gas yield.