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渗透汽化法汽油脱硫用乙基纤维素膜制备工艺的优化 被引量:3

Preparation process optimization of crosslinked EC pervaporation membrane for gasoline desulfurization
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摘要 为了进一步提高乙基纤维素(EC)膜的脱硫性能,利用光引发交联反应将丙烯酸酯单体和EC聚合物合成交联EC膜,用红外光谱仪、扫描电镜对该膜的膜结构进行了表征。采用模拟汽油评价了EC膜的脱硫性能,研究了EC质量分数、交联剂质量分数、成膜温度、脱硫温度对EC膜渗透汽化性能的影响。结果表明,随着EC质量分数和交联剂质量分数的增加,硫富集因子和通量均先增大后减小,存在极大值;随着成膜温度和脱硫温度的升高,硫富集因子逐渐降低,通量一直增加。综合考虑两者对汽油脱硫的贡献,选取EC质量分数为18%,交联剂质量分数为21%~22%,成膜温度为50℃,脱硫温度为80℃为最佳脱硫条件。 In order to further improve the desulfurization performance of ethyl cellulose( EC) membrane,acrylate monomer and EC polymer are used to synthesize crosslinked EC membrane. The membrane structure is characterized by IR spectroscopy and scanning electron microscopy. The model gasoline is used to evaluate the desulfurization performance. The effects of solid content,crosslinking agent content and temperature on the permeation flux and enrichment factor of the membrane are investigated. The results show that higher content of EC and crosslinking agent can make both the permeation flux and enrichment factor first increased and then decreased. There is a maximum value.Increasing the membrane-forming temperature and desulfurization temperature results in the increase of the permeation flux and the gradual decrease of the enrichment factor. On the basis of the results,the optimum conditions of desulfurization are suggested as follows: 18% mass fraction of the solid content,21%- 22% mass fraction of the crosslinking agent content,50℃ of the membrane-forming temperature and 80℃ of the desulfurization temperature.
出处 《现代化工》 CAS CSCD 北大核心 2016年第5期86-89,共4页 Modern Chemical Industry
基金 中央高校基本科研业务费专项资金(R1504059A) 山东省自然科学基金项目(ZR2012BL15) 黄河三角洲京博化工研究院有限公司资助(2014040001)
关键词 渗透汽化 交联EC膜 汽油脱硫 pervaporation crosslinked EC membrane desulfurization of gasoline
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参考文献12

  • 1张晶华,梁晓乐,张宝军.清洁汽油生产技术进展[J].精细石油化工进展,2004,5(11):50-52. 被引量:6
  • 2孙楚桥,庞博,刘凌轩.国内外清洁汽油质量分析及发展趋势[J].广东化工,2012,39(13):60-61. 被引量:5
  • 3Yang Z J, Zhang W Y, Li J D, et al. Polyphosphazene membrane for desulfurization : Selecting poly [bis ( trifluoroethoxy ) phosphazene ] for pervaporative removal of thiophene [J].Separation and Purifica- tion Technology ,2012,93 : 15 - 24.
  • 4Yang Z J, Wang Z Q, Li J D,et al. Enhancing FCC gasoline desulfu- rizalion performanee in a polyphosphazene pervaporative membrane [J]. Separation and Purification Technology,2013,109:48 - 54.
  • 5陈镇,秦培勇,陈翠仙.渗透汽化和蒸汽渗透技术的研究、应用现状及发展[J].膜科学与技术,2003,23(4):103-109. 被引量:33
  • 6王丽华,赵之平,李继定,陈翠仙.一种可溶性聚酰亚胺的合成及其渗透汽化脱有机硫化物性能测试[J].高分子学报,2006,16(3):496-499. 被引量:14
  • 7Qi R,Wang Y, Li J, et al. Pervaporation separation of alkane/thio- phene mixtures with PDMS membrane [ J ]. Journal of Membrane Science,2006,280( 1 ) :545 -552.
  • 8Li B, Liu WP, Wu H, et al. Desulfurization of model gasoline by bioinspired oleophilic nanocomposite membranes [J]. Journal of Membrane Science,2012,415 (416 ) : 278 - 287.
  • 9Lin L,Kong Y,Wang G,et al. Selection and crosslinking modifica- tion of membrane material for FCC gasoline desulfurization [ J ]. Journal of Membrane Science ,2006,285 ( 1 ) :144 - 151.
  • 10Lin L, Wang G, Qu H, et al. Pervaporation performance of crosslinked polyethylene glycol membranes for deep desulfurization of FCC gasoline [J].Journal of Membrane Science,2006,280 ( 1 ) : 651 - 658.

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