Untitled Desalination 199 (2006) 371-372Authorsby 06531 Ankara, Chemical Engineering Department, Middle East Technical University, TurkeyConclusion CH4 N2 0.4 Fig. 2. Single gas permeances for tubular MFI membranes (composition: 80SiO2:16TPAOH:1536H2O; T = 95°C; t = 72 h). Source: http://www.desline.com/articoli/7636.pdf Request a quote Phone: +31 152 610 900 info@lenntech.com Request a quote
