Biogas upgrading – Review of commercial technologies - SGC
Biogas upgrading – Review of commercial technologies - SGC
Biogas upgrading – Review of commercial technologies - SGC
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<strong>SGC</strong> Rapport 2013:270<br />
Figure 11 Illustration showing the separation involved during <strong>upgrading</strong> <strong>of</strong> biogas<br />
with membranes. Image from Air Liquide.<br />
During the separation <strong>of</strong> carbon dioxide, also water vapor, hydrogen and parts <strong>of</strong><br />
the oxygen are removed from the biomethane. The permeation rate through a typical<br />
membrane (made <strong>of</strong> a glassy polymer) used in biogas applications, is mainly<br />
depending on the size <strong>of</strong> the molecules (Baker 2004) but also on the hydrophilicity.<br />
The relative permeation rates shown in Figure 12 are based on experiences from<br />
the membrane manufacturer.<br />
C3H8 CH4 N2 H2S CO2 H2O<br />
Slow permeation Fast permeation<br />
Figure 12 Relative permeation rate <strong>of</strong> different molecules through a membrane<br />
produced from a glassy polymer.<br />
On the market today, membranes produced by several manufacturer are used for<br />
biogas <strong>upgrading</strong>, e.g. two types <strong>of</strong> polymeric (glassy polymers) hollow fibre membranes<br />
(Air Liquide Medal TM and Evonik Sepuran®) and one carbon membrane<br />
(manufactured by MemfoACT AS), see Figure 13. The membranes are continuously<br />
improved to get higher selectivity, higher permeability and cheaper manufacturing.<br />
Figure 13 Hollow fibre membrane from Evonik Sepuran to the left, from Air Liquide<br />
Medal in the middle and carbon membrane from Memfoact to the right. Images<br />
from Evonik Fibres, Air Liquide and Memfoact.<br />
Svenskt Gastekniskt Center AB, Malmö <strong>–</strong> www.sgc.se 29