Table A11.

Solubility coefficient of heterogeneous membranes containing ZIF−8 to different gases measured for different feed pressure and temperature values.

Membrane Type	Feed Pressure [bar]	Solubility Si [10−3 mol/(m3·Pa)]
		N2			CH4			CO2
		Process Temperature [ °C]			Process Temperature [ °C]			Process Temperature [ °C]
		25	4[°C]	55	25	4[°C]	55	25	4[°C]	55
PEBAX 2533 +2 wt% ZIF−8	2	0.123	0.130	0.119	0.186	0.171	0.189	0.411	0.351	0.311
		±0.008	±0.008	±0.007	±0.006	±0.005	±0.006	±0.025	±0.021	±0.019
	4	0.130	0.146	0.121	0.201	0.216	0.199	0.471	0.428	0.342
		±0.008	±0.009	±0.008	±0.006	±0.007	±0.006	±0.028	±0.026	±0.021
	8	0.122	0.142	0.127	0.200	0.238	0.211	0.572	0.505	0.428
		±0.008	±0.009	±0.008	±0.006	±0.007	±0.007	±0.034	±0.03	±0.026
PEBAX 2533 +5 wt% ZIF−8	2	0.124	0.131	0.116	0.187	0.181	0.190	0.418	0.400	0.309
		±0.008	±0.008	±0.007	±0.006	±0.006	±0.006	±0.025	±0.024	±0.019
	4	0.125	0.147	0.122	0.205	0.214	0.214	0.477	0.465	0.366
		±0.008	±0.009	±0.008	±0.006	±0.007	±0.007	±0.029	±0.028	±0.022
	8	0.133	0.142	0.131	0.212	0.232	0.218	0.605	0.537	0.452
		±0.008	±0.009	±0.008	±0.007	±0.007	±0.007	±0.036	±0.032	±0.027