Research Papers by 06531 Ankara

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CH4 N2 0.4 Fig. 2. Single gas permeances for tubular MFI membranes (composition: 80SiO2:16TPAOH:1536H2O; T = 95°C; t = 72 h).
Desalination 199 (2006)

MFI membranes with high permeances, separation selectivities between 4 and 8.5 and ideal selectivities between 10 and 70 were synthesized in a flow system with circulation. Such high permeances and similar selectivities are seen in membranes synthesized at low temperatures. Carried out at low temper
Desalination 199 (2006)