[1]龚剑洪,毛安国,刘晓欣,等.催化裂化轻循环油加氢-催化裂化组合生产高辛烷值汽油或轻质芳烃 技术[J].石油炼制与化工, 2016, 47(9):1-5
[2]孙士可,曾榕辉,吴子明.催化裂化柴油加氢转化技术工业应用总结[J].炼油技术与工程, 2019, 49(7):16-19
[3]袁起民, 毛安国, 龚剑洪, 秦煜栋, 陈阳, 洪先荣.选择性加氢-催化裂化组合生产轻质芳烃技术工业实践[J].石油炼制与化工, 2020, 51(12):1-5
[4]郑均林,徐旋,祁晓岚,等.劣质重芳烃资源及其化工产品转化技术[J].化工进展, 2017, 36(10):3665-3673
[5]毛安国,龚剑洪.催化裂化轻循环油生产轻质芳烃的分子水平研究[J].石油炼制与化工, 2014, 45(7):1-6
[6]Arribas M A,Corma A,Díaz-Caba?as M J,et al.Hydrogenation and ring opening of tetralin over bifunctional catalysts based on the new ITQ-21 zeolite[J].Applied Catalysis A:General, 2004, 273(12):277-286
[7]Ferraz S G A,Zotin F M Z,Araujo L R R,et al.Influence of support acidity of NiMoS catalysts in the activity for hydrogenation and hydrocracking of tetralin[J].Applied Catalysis A:General, 2010, 384(12):51-57
[8]Upare D P,Park S,Kim M S,et al.Cobalt promoted Mo/beta zeolite for selective hydrocracking of tetralin and pyrolysis fuel oil into monocyclic aromatic hydrocarbons[J].Journal of Industrial & Engineering Chemistry, 2016, 35:99-107
[9]Corma A,González-Alfaro V,Orchillés A V.Decalin and tetralin as probe molecules for cracking and hydrotreating the light cycle oil[J].Journal of Catalysis, 2001, 200(1):34-44
[10]陈妍,宋海涛,朱玉霞,等.和型分子筛催化四氢萘裂化规律的对比[J].石油学报石油加工, 2015, 31(3):650-656
[11]Townsend AT,Abbot J.Catalytic reactions of tetralin on HZSM-5 zeolite[J].Applied Catalysis A: General, 1993, 95(2):221-236
[12]Mostad HB, Riis TU, Ellestad OH.Catalytic cracking of naphthenes and naphtheno-aromatics in fixed bed micro reactors[J].Applied catalysis, 1990, 63(1):345-364
[13]王新,许友好.四氢萘和十氢萘的催化裂化反应途径及特征产物[J].石油学报石油加工, 2019, 35(02):224-233
[14]唐津莲,许友好,汪燮卿,等.四氢萘在分子筛催化剂上环烷环开环反应的研究[J].石油炼制与化工, 2012, 43(1):20-25
[15]唐津莲, 许友好, 汪燮卿, 程从礼.十氢萘在分子筛催化剂上的开环反应研究[J].燃料化学学报, 2012, 40(12):1422-1428
[16]Cheng X, Xiong G, Guo X.Reactions of indan over zeolite catalysts[J].Industrial & engineering chemistry research, 2010, 49(20):9759-9763
[17]许友好.催化裂化化学与工艺[M]. 科学出版社, 2013
[18]耿秋月, 袁帅, 严加松.丁基苯在不同分子筛催化剂上的催化裂化规律[J].石油化工, 2019, 48(08):787-792 |