Effect of N2 and CO Inhibition in H2 Permeation through Pd82Ag18/Al2O3 Membrane at Various Temperatures
Pd-based membrane is one of the highly selective membranes for hydrogen separation. However, the permeability of Pd-based membrane will decrease if the feed gas mixture for the membrane contains N2 and CO. This research aimed to determine the inhibitory effect of N2 and CO gas, dynamic conditions...
Saved in:
Main Author: | |
---|---|
Format: | Final Project |
Language: | Indonesia |
Online Access: | https://digilib.itb.ac.id/gdl/view/38425 |
Tags: |
Add Tag
No Tags, Be the first to tag this record!
|
Institution: | Institut Teknologi Bandung |
Language: | Indonesia |
Summary: | Pd-based membrane is one of the highly selective membranes for hydrogen separation. However,
the permeability of Pd-based membrane will decrease if the feed gas mixture for the membrane
contains N2 and CO. This research aimed to determine the inhibitory effect of N2 and CO gas,
dynamic conditions on H2 permeability, and determine the effect of temperature on H2 recovery
through Pd82Ag18/Al2O3 membrane.
The membrane used has a thickness of 20.2 ?m Pd82Ag18 and 2 mm Al2O3 as the support. The
feed used was a mixture of hydrogen gas, one of the inhibitor gases, and argon for residence time
balancing purpose. The sweep gas was flowed on the tube side to create a driving force in form
of a pressure difference. The variation used for the membrane permeability tests was the
composition of the feed and for the temperature effect tests was the operating temperatures
which were at 320°C, 340°C, and 360°C. The membrane permeability tests were carried out at
350°C and the switching time for the dynamic condition was 60 seconds.
From the research, the permeability for Pd82Ag18/Al2O3 with pure hydrogen feed was obtained at
5.57×10-4 mole H2 m-1 h-1 kPa-0.5, whereas with CO as inhibitor, the permeability was at 5.17×10-
4 mole H2 m-1 h-1 kPa-0.5, and with N2 as inhibitor, the permeability was at 5.09×10-4 mole H2 m-1
h-1 kPa-0.5. The dynamic condition with N2 as inhibitor increased the permeability by 49%. H2
recovery from the temperature tests, for the pure H2 and with N2 inhibitor, increased as the
operating temperature rose, whilst for the mixture with CO as inhibitor, the H2 recovery
decreased at 360°C. The effect of temperature on time lag was also observed and it decreased as
the operating temperature rose for all feed mixtures. Based on the results of this research, the
presence of inhibitors would decrease while dynamic conditions increase the membrane
permeability. The operating temperature also affected the H2 recovery and time lag based on the
feed mixture used.
|
---|