Pervaporation separation of n-octane/thiophene mixtures using polydimethylsiloxane/ceramic composite membranes

ty10086 提交于 周四, 08/26/2021 - 13:45
文章英文标题
Pervaporation separation of n-octane/thiophene mixtures using polydimethylsiloxane/ceramic composite membranes
正文
Abstract(#br)Crosslinked polydimethylsiloxane (PDMS)/ceramic composite membranes were prepared and employed for desulfurization of model gasoline composed of n-octane and thiophene. The structural morphology and thermal stability of the composite membranes were characterized by scanning electron microscope (SEM) and thermogravimetric analysis (TGA). The pervaporation performances of the membranes under various crosslinking agent amounts, feed sulfur content, feed temperature, permeate pressure and feed flow rate were investigated. Experimental results indicated that 20% of the crosslinking agent amount was more preferable. Increase of sulfur content in feed resulted in a higher total flux but a lower sulfur enrichment factor. By increasing the feed temperature, the total flux increased while sulfur enrichment factor decreased. Low permeate pressure and high feed flow rate were beneficial to improve total flux and sulfur enrichment factor. At 303.15\u003cce:hsp sp=\"0.25\"/\u003eK, the composite membrane exhibited high performance with the total flux of 5.37\u003cce:hsp sp=\"0.25\"/\u003ekg m −\u003cce:hsp sp=\"0.10\"/\u003e2 h −\u003cce:hsp sp=\"0.10\"/\u003e1 and the corresponding sulfur enrichment factor of 4.22 for 400\u003cce:hsp sp=\"0.25\"/\u003eμg g −\u003cce:hsp sp=\"0.10\"/\u003e1 sulfur in feed under 210\u003cce:hsp sp=\"0.25\"/\u003ePa. Our results showed that the PDMS/ceramic composite membrane was a potential candidate to be used for sulfur removal from the gasoline.
文章内容(英文)
Abstract(#br)Crosslinked polydimethylsiloxane (PDMS)/ceramic composite membranes were prepared and employed for desulfurization of model gasoline composed of n-octane and thiophene. The structural morphology and thermal stability of the composite membranes were characterized by scanning electron microscope (SEM) and thermogravimetric analysis (TGA). The pervaporation performances of the membranes under various crosslinking agent amounts, feed sulfur content, feed temperature, permeate pressure and feed flow rate were investigated. Experimental results indicated that 20% of the crosslinking agent amount was more preferable. Increase of sulfur content in feed resulted in a higher total flux but a lower sulfur enrichment factor. By increasing the feed temperature, the total flux increased while sulfur enrichment factor decreased. Low permeate pressure and high feed flow rate were beneficial to improve total flux and sulfur enrichment factor. At 303.15\u003cce:hsp sp=\"0.25\"/\u003eK, the composite membrane exhibited high performance with the total flux of 5.37\u003cce:hsp sp=\"0.25\"/\u003ekg m −\u003cce:hsp sp=\"0.10\"/\u003e2 h −\u003cce:hsp sp=\"0.10\"/\u003e1 and the corresponding sulfur enrichment factor of 4.22 for 400\u003cce:hsp sp=\"0.25\"/\u003eμg g −\u003cce:hsp sp=\"0.10\"/\u003e1 sulfur in feed under 210\u003cce:hsp sp=\"0.25\"/\u003ePa. Our results showed that the PDMS/ceramic composite membrane was a potential candidate to be used for sulfur removal from the gasoline.
来源出处
Journal|[J]DesalinationVolume 258, Issue 1. 2010. PP 106-111
DOI
https://doi.org/10.1016/j.desal.2010.03.035

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