Carbon dioxide removal in indirect gasification - SGC
Carbon dioxide removal in indirect gasification - SGC
Carbon dioxide removal in indirect gasification - SGC
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<strong>SGC</strong> Rapport 2013:277<br />
brane systems used for gas separation is available <strong>in</strong> <strong>SGC</strong> report 270 [47]. A<br />
membrane is a dense filter that can separate the components <strong>in</strong> a gas or a liquid<br />
down to the molecular level. The membranes used for biogas upgrad<strong>in</strong>g are ma<strong>in</strong>ly<br />
manufactured from polymeric materials. The membranes used for biogas upgrad<strong>in</strong>g<br />
reta<strong>in</strong> methane while the carbon <strong>dioxide</strong> is able to permeate through the<br />
membrane. Dur<strong>in</strong>g the separation of carbon <strong>dioxide</strong> from the raw gas other compounds<br />
such as water vapor, hydrogen and to some degree oxygen are removed<br />
from the biomethane. The permeation rate through a glassy polymer, commonly<br />
used <strong>in</strong> the biogas applications, is ma<strong>in</strong>ly depend<strong>in</strong>g on the size of the molecules,<br />
which gives the relative permeation rates shown <strong>in</strong> Figure 15.<br />
Figure 15. Relative permeation rate of different molecules through a membrane<br />
used for upgrad<strong>in</strong>g of biomethane.<br />
The gas stream go<strong>in</strong>g <strong>in</strong>to a membrane is called the feed stream. The feed is separated<br />
<strong>in</strong>to permeate and retentate <strong>in</strong>side the membrane. Retentate is the gas<br />
stream that do not pass through the membrane while permeate is the gas stream<br />
that pass through the membrane. An example of a membrane process for upgrad<strong>in</strong>g<br />
of bio-SNG is depicted <strong>in</strong> Figure 16. The membrane unit can consist of several<br />
membrane stages. The producer gas is cleaned from pollutants, e.g. water and<br />
hydrogen sulphide, before it is compressed and fed to the membrane unit. In cases<br />
where ammonia and volatile organic carbons are expected <strong>in</strong> significant concentrations<br />
<strong>in</strong> the producer gas, these components are also removed before the<br />
biogas upgrad<strong>in</strong>g. Additional to this clean<strong>in</strong>g, it is also common to have a particle<br />
filter to protect the compressor and the membranes.<br />
After gas clean<strong>in</strong>g, the biogas is compressed to 5-20 barg. S<strong>in</strong>ce oil lubricated<br />
compressors are commonly used, it is important to have efficient oil separation<br />
after compression. This oil separation is important not only for the oil residues from<br />
the compressor but also for remov<strong>in</strong>g oil naturally occurr<strong>in</strong>g <strong>in</strong> the biogas. The oil<br />
will otherwise foul the membrane and decrease its lifetime. In the membrane unit<br />
itself the carbon <strong>dioxide</strong> is separated from the ma<strong>in</strong> gas stream, but s<strong>in</strong>ce a m<strong>in</strong>or<br />
share of the methane and other compounds will permeate, the off-gas stream from<br />
one stage is recirculated to the compressor to reach an acceptable yield.<br />
Svenskt Gastekniskt Center AB, Malmö – www.sgc.se 37