2017
DOI: 10.1016/j.memsci.2017.06.082
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Vacuum film etching effect of carbon alumina mixed matrix membranes

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Cited by 13 publications
(5 citation statements)
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“…3), indicating porous membranes contrary to the dense xerogels. These results are in line with reports that impregnation using an assisted-vacuum method causes oligomers to get entrained with solvent and diffuse into porous substrates to form porous structures [18,19,24]. Therefore, molecular weight (MW) cut-off tests were carried out as the best approach to determine pore sizes.…”
Section: Resultssupporting
confidence: 87%
“…3), indicating porous membranes contrary to the dense xerogels. These results are in line with reports that impregnation using an assisted-vacuum method causes oligomers to get entrained with solvent and diffuse into porous substrates to form porous structures [18,19,24]. Therefore, molecular weight (MW) cut-off tests were carried out as the best approach to determine pore sizes.…”
Section: Resultssupporting
confidence: 87%
“…Porous substrates are also extensively used for the preparation of inorganic membranes for microfiltration, [1][2][3] desalination, [4][5][6][7] gas separation, [8][9][10][11] and percrystallization processes. [12,13] These inorganic membranes are known as asymmetric membranes as they are conventionally prepared by coating ceramic [14][15][16] or carbon [17][18][19] thin films as top layers on porous substrates. The importance of the porous substrate is to provide the mechanical strength otherwise not available in thin films.…”
mentioning
confidence: 99%
“…The feed NaCl 17.5 wt% concentration used in this work would generate an osmotic pressure over 135 bar, well beyond the RO plant operation capabilities. In addition, the high water fluxes in this work are also much higher than those obtained in pervaporative desalination using inorganic membranes operating at higher temperatures and lower NaCl feed concentration such as 22.9 L m -2 h -1 for cobalt oxide silica membranes (7.5 wt% at 60 ºC)[32], 25.4 L m -2 h -1 for carbon alumina membranes (3.5 wt% at 75 ºC)[33] and 9.2 L m -2 h -1 for hybrid carbon silica membranes (15 wt% at 60 ºC)[34]. This great performance of the carbonised sucrose membranes for pure water recovery proved to be a bonus for using this technology to crystallise solutes whilst recovering the solvent.As the best performance in terms of water and NaCl fluxes was delivered by the membrane carbonised at 750 ºC, this membrane was further tested to investigate the effect of the vacuum pressure in the permeate side.Fig.…”
mentioning
confidence: 77%