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内蒙古自治区呼和浩特市赛罕区大学西街235号 邮编: 010021
作者机构:Changzhou Univ Sch Petrochem Engn Jiangsu Key Lab Adv Catalyt Mat & Technol Changzhou 213164 Peoples R China Changzhou Univ Sch Petr Engn Changzhou 213016 Peoples R China Nanjing Univ Technol State Key Lab Mat Oriented Chem Engn Nanjing 210009 Jiangsu Peoples R China
出 版 物:《JOURNAL OF POROUS MATERIALS》 (多孔性材料杂志)
年 卷 期:2015年第22卷第5期
页 面:1195-1203页
核心收录:
学科分类:08[工学] 0805[工学-材料科学与工程(可授工学、理学学位)] 0703[理学-化学]
基 金:national Science Foundations of China [21276029, 21406018, 21306012] Natural Science Foundation of Jiangsu [BK20131142] Jiangsu Overseas Research & Training Program for University Prominent Young & Middle-aged Teachers and Presidents Jiangsu Key Laboratory of Advanced Catalytic Materials and Technology [BM2012110] Priority Academic Program Development of Jiangsu Higher Education Institutions (PAPD) State Key Laboratory of Materials-Oriented Chemical Engineering
主 题:ZIF-69 membrane N-2/alkane (C5-C7) separation Gasoline vapor recovery Operating condition
摘 要:The compact ZIF-69 membranes have been prepared by seeded growth method for the recovery of gasoline vapor which is a major challenge in the petrochemical industry. The membrane performances for separating N-2/n-alkane mixtures at various operating conditions (e.g. trans-membrane pressure difference, operating temperature, feed concentration, and stage cut) were systematically investigated. The highest separation factor was 2.60 with the corresponding permeance of 5.02 x 10(-8) mol/(m(2) s Pa) for the N-2/n-C6H14 model mixtures. Moreover, the effects of n-alkane components (n-C5H12, n-C6H14, and n-C7H16) on the separation performances were studied, and the separation factors followed alpha(N-2/n-C7H16) alpha(N-2/n-C6H14) alpha(N-2/n-C5H12), due to the different adsorption capacities of n-alkanes on ZIF-69 materials. The present work demonstrates that the ZIF-69 membrane is a highly promising candidate for the application in gasoline vapor recovery.