石油炼制与化工
石油煉製與化工
석유련제여화공
PETROLEUM PROCESSING AND PETROCHEMICALS
2014年
7期
29-35
,共7页
周岩%张杰潇%许明德%田辉平
週巖%張傑瀟%許明德%田輝平
주암%장걸소%허명덕%전휘평
NaY 分子筛%催化裂化催化剂%后处理工艺%焙烧%稀土交换%铵离子交换
NaY 分子篩%催化裂化催化劑%後處理工藝%焙燒%稀土交換%銨離子交換
NaY 분자사%최화열화최화제%후처리공예%배소%희토교환%안리자교환
NaY zeolite%FCC catalyst%post-treatment%calcination%rare earth exchange%ammoni-um ion exchang e
针对目前 FCC 催化剂制备方法工艺流程复杂的现状,进行催化剂后处理工艺条件的探索。直接以 NaY 分子筛与拟薄水铝石、铝溶胶、高岭土打浆混合,喷雾干燥得到催化剂粉体,对该催化剂粉体进行基本性质的表征。利用已经制备好未经改性的催化剂进行一次焙烧和一次稀土交换,再分别采用三次焙烧和三次常温(<90℃)铵盐交换、两次焙烧和两次高温(>90℃)铵盐交换,探索了优化的工艺条件,两种铵盐交换方法得到的催化剂中 Na2 O 质量分数均达到0.3%以下。
針對目前 FCC 催化劑製備方法工藝流程複雜的現狀,進行催化劑後處理工藝條件的探索。直接以 NaY 分子篩與擬薄水鋁石、鋁溶膠、高嶺土打漿混閤,噴霧榦燥得到催化劑粉體,對該催化劑粉體進行基本性質的錶徵。利用已經製備好未經改性的催化劑進行一次焙燒和一次稀土交換,再分彆採用三次焙燒和三次常溫(<90℃)銨鹽交換、兩次焙燒和兩次高溫(>90℃)銨鹽交換,探索瞭優化的工藝條件,兩種銨鹽交換方法得到的催化劑中 Na2 O 質量分數均達到0.3%以下。
침대목전 FCC 최화제제비방법공예류정복잡적현상,진행최화제후처리공예조건적탐색。직접이 NaY 분자사여의박수려석、려용효、고령토타장혼합,분무간조득도최화제분체,대해최화제분체진행기본성질적표정。이용이경제비호미경개성적최화제진행일차배소화일차희토교환,재분별채용삼차배소화삼차상온(<90℃)안염교환、량차배소화량차고온(>90℃)안염교환,탐색료우화적공예조건,량충안염교환방법득도적최화제중 Na2 O 질량분수균체도0.3%이하。
Due to the complexity of present FCC catalyst preparation process,catalyst post-treat-ment technology was explored. NaY zeolite,pseudo-boehmite,aluminum sol and kaolin were mixed and spray-dried into catalyst microsphere NaY35. The basic properties of the unmodified NaY35 were char-acterized by XRF,XRD,BET. The NaY35 catalyst was treated by once calcination and then once rare earth ion exchange. The treated NaY35 was used as a starting precursor. The precursor was then trea-ted by three times calcinations and three times ammonium ion exchanges at normal temperature (<90 ℃),and two times calcinations and two times ammonium ion exchanges at high temperature (>90 ℃),respectively to explore the optimized post-treatment conditions for FCC catalyst.The test re-sults indicate that the Na2 O contents in both prepared catalysts are less than 0.3%.