[1] Eri Ito and Van Veen J. A. Rob, On novel processes for removing sulphur from refinery streams[J]. Catalysis Today, 2006, 116: 446-460.
[2] Wenbo Wang, Wang Shujun, Liu Hongyan and Wang Zhenxin, Desulfurization of gasoline by a new method of electrochemical catalytic oxidation[J]. Fuel, 2007, 86: 2747-2753.
[3] 陈焕章, 催化裂化汽油脱硫技术进展[J]. 化工科技, 2004, 12: 46-51.
[4] 张艳维, 亓玉台, 沈健, 汽油深度脱硫技术进展[J]. 浙江化工, 2004, 5: 13-16.
[5] B. Smitha, Suhanya D., Sridhar∗ S. and Ramakrishna M., Separation of organic–organic mixtures by pervaporation—a review[J]. Journal of Membrane Science, 2004, 241: 1-21.
[6] P. Shao and Huang R., Polymeric membrane pervaporation[J]. Journal of Membrane Science, 2007, 287: 162–179.
[7] S. Semenova, Polymer membranes for hydrocarbon separation and removal[J]. Journal of Membrane Science, 2004, 231: 189–207.
[8] Ping Na, Zhao Baolin, Gu Linyuan, Liu Jia and Na Jiyu, Deep desulfurization of model gasoline over photoirradiated titanium-pillared montmorillonite[J]. Journal of Physics and Chemistry of Solids, 2009, 70: 1465-1470.
[9] Ligang Lin, Zhang Yuzhong and Kong Ying, Recent advances in sulfur removal from gasoline by pervaporation[J]. Fuel, 2009, 88: 1799-1809.
[10] G. Krishnaiah and T.Cartwright,  S-Brane Technology Brings Flexibility To Refiners’ Clean Fuel Solutions[C]. NPRA Annual Meeting 2004.
[11] Lloyd Steven White, Wormsbecher Richard Franklin and Lesemann Markus, Membrane separation for sulfur reduction[P]. US 7048846
[12] Bhupender S. Minhas, R.Chuba Michael and J.Saxton Robert, Membrane process for separating sulfur compounds form FCC light naphtha[P]. US 6649061
[13] Bhupender S. Minhas and J.Saxton Robert, Removal of thiophenic sulfur from gasoline by membrane separation[P]. WO 2002064529
[14] Robert J.Saxton and Minhas Bhupender S., Ionic membranes for organic sulfur separation from liquid hydrocarbon solutions[P]. US 6702945
[15] P Mark, Richard F and Bonelli J, Removal of sulfur from a hydrocarbon through a selective membrane[P]. US 6736961
[16] Ying Kong Ligang Lin, Et Al., Selection and crosslinking modification of membrane material for FCC gasoline desulphurization[J]. Journal of Membrane Science, 2006, 285: 144–151.
[17] Ligang Lin, Ying Kong, Kekun Xie, Fuwei Lu, Rongkun Liu, Lei Guo, Shuai Shao, Jinrong Yang, Deqing Shi and Yuzhong Zhang, Polyethylene glycol/polyurethane blend membranes for gasoline desulphurization by pervaporation technique[J]. Separation and Purification Technology, 2008, 61: 293-300.
[18] Huimin Qu, Ying Kong, Hongling Lv, Yuzhong Zhang, Jinrong Yang and Deqing Shi, Effect of crosslinking on sorption, diffusion and pervaporation of gasoline components in hydroxyethyl cellulose membranes[J]. Chemical Engineering Journal, 2010, 157: 60-66.
[19] Yujun Wang Rongbin Qi, Et Al.,, Pervaporation separation of alkane/thiophene mixtures with PDMS membrane[J]. Journal of Membrane Science, 2006, 280: 545–552.
[20] Changwei Zhao Rongbin Qi, Et Al., Removal of thiophenes from n-octane/thiophene mixtures by pervaporation[J]. Journal of Membrane Science, 2006, 269: 94-100.
[21] Rongbin Qi, Yujun Wang, Jian Chen, Jiding Li and Shenlin Zhu, Pervaporative desulfurization of model gasoline with Ag2O-filled PDMS membranes[J]. Separation and Purification Technology 2007, 57: 170-175.
[22] Zhiping Zhao Lihua Wang, Jiding Li, Et Al.,, Synthesis and characterization of uorinated polyimides for pervaporation of n-heptane/thiophene mixtures[J]. European Polymer Journal, 2006, 42: 1266–1272.
[23] Ben Li, Dan Xu, Zhongyi Jiang, Xiongfei Zhang, Wanpeng Liu and Xiao Dong, Pervaporation performance of PDMS-Ni2+Y zeolite hybrid membranes in the desulfurization of gasoline[J]. Journal of Membrane Science, 2008, 322: 293-301.
[24] Li J D Chen J, Qi R B, Et Al. , Pervaporation performance of crosslinked polydimethylsiloxane membranes for deep desulfurization of FCC gasoline I. Effect of different sulfur species[J]. Journal of Membrane Science 2008, 322: 113-121.
[25] 陈天泉, 陈金勋，李继定, 正庚烷/有机硫体系渗透汽化脱硫[J]. 膜科学与技术, 2007, 27: 87-90.
[26] 卢福伟, 孔瑛, 吕宏凌, 等, 分子动力学模拟噻吩/正庚烷在PEG膜中溶解-扩散行为[C]. 第四届中国膜科学与技术报告会论文集 (北京) 2010, pp. 590-592.
[27] 吕宏凌, 王保国，杨基础, 溶剂小分子在高分子中的传质研究评述[J]. 高分子材料科学与工程, 2008, 24: 6-9.
[28] 吕宏凌, 邓斌，王保国, 用于高分子膜分离材料设计的物性数据库研究[C]. 第五届全国膜与膜过程学术报告会论文集 2005, pp. 95-96.
[29] Sachin Nair and Tatarchuk Bruce J., Supported silver adsorbents for selective removal of sulfur species from hydrocarbon fuels[J]. Fuel, 89: 3218-3225.
[30] Rong Xu, Liu Gongping, Dong Xueliang, Wanqin and Jin, Pervaporation separation of n-octane/thiophene mixtures using polydimethylsiloxane/ceramic composite membranes[J]. Desalination, 258: 106-111.
[31] Fuwei Lu, Kong Ying, Lv Hongling, Yang Jingrong and Feng Zhaoxuan, The correlation between solvent treatment and the microstructure of PAN-b-PEG copolymer membranes[J]. Polymer Journal, 2011, doi:10.1038/pj.2011.6.
[32] Fuwei Lu, Kong Ying, Lv Hongling, Ding Jun and Yang Jinrong, The pervaporation performance of polyimide-block-polyethylene glycol membranes for gasoline desulphurization: effect of PEG groups[J]. Advanced Materials Research, 2011, 150-151: 317-320.
[33] 陈龙祥 由涛, 张庆文, 等, 渗透汽化膜组件在乙醇分离中的应用[J]. 食品工业与科技, 2009, 10: 336-339.
[34] Lin L G Kong Y, Yang J R, Et Al. , FCC gasoline desulfurization by pervaporation: Effects of gasoline components[J]. Journal of Membrane Science, 2007, 293: 36-43.
[35] Kong Y Lin L G, Yang J R, Et Al. , Scale-up of pervaporation for gasoline desulphurization Part 1. Simulation and design[J]. Journal of Membrane Science, 2007, 298: 1-13.
[36] Lin L G Kong Y, Zhang Y Z, Et Al., Studies on polyethylene glycol/polyethersulfone composite membranes for FCC gasoline desulphurization by pervaporation[J]. Eur. Polym. J, 2008, 44: 3335-3343.
[37] 孔瑛 渠慧敏, 张玉忠, 等, FCC汽油脱硫用交联HEC渗透汽化膜的性能评价[J]. 石油学报(石油加工), 2008, 24: 232-236.
[38] 林立刚 孔 瑛, 杨金荣, 等, 一种FCC汽油脱硫用膜材料的制备方法[P]. CN 1974729
[39] Ying Kong Fuwei Lu, Rongkun Liu, Et Al.,  Pervaporation performance and stability analysis of PEG /PVDF composite membrane for desulfurization of FCC gasoline[C]. APCSEET 2009.
[40] G. Krishnaiah and Balko J.,  Reduce Ultra-Low Sulfur Gasoline Compliance Costs with Davison Clean Fuels Technologies[C]. NPRA Annual Meeting 2003.
[41] Gang Wang Ligang Lin, Et Al., Pervaporation performance of crosslinked polyethylene glycol membranes for deep desulphurization of FCC gasoline[J]. Journal of Membrane Science, 2006, 280: 651–658.
[42] Wenchang Ji, Sikdar Subhas K. and Hwang Sun-Tak, Modeling of multicomponent pervaporation for removal of volatile organic compounds from water[J]. Journal of Membrane Science, 1994, 93: 1-19.
[43] 卢福伟，孔瑛，林立刚，等,  膜法汽油深度脱硫技术放大及过程模拟[C]. 第六届全国膜与膜过程会议 (天津) 2008.
[44] J. Balko, Glaser R., Wormsbecher R. and Wynn N.,  Reduce Your Tier 2 Gasoline Sulfur Compliance Costs with Grace Davison S-Brane Technology[C]. NPRA Annual Meeting 2002.
[45] J.Balko and M.Lesemann,  S-Brane-Gasoline Sulfur Reduction Alternative with Low Capital Investment[C]. Davison Catalysts 2002.
[46] Grace receives technology award[J]. Membrane Technology, 2005, 2005: 5-5.
[47] W.R Cb&I,  Grace to market desulphurization process,Membrane technology[C]. An international newsletter 2004.
[48] Robert Cs.,  TransFining™ – a novel process for low sulfur fuels[C]. Prepared for presentation at the 2004 spring meeting of the american institute of chemical engineers 2004, pp. 25–29.
[49] Robert Cs,  Novel membrane pervaporation process removes sulfur from gasoline.[C]. <http://www.transionics.com/TranSep_G_Brochure_082506.pdf> 2006.
[50] K. Gautham and C. Todd X. Zhao, Membrane separation for clean fuels[J]. Petrol Q 2004, 21–27.
[51] G Krishnaiah, Zhao X and Novak K,  What will gasoline sulfur compliance really cost you? S-Brane™ Membrane Technology Economic Analysis[C]. NPRA Annual Meeting 2005.