Synthesis Of Asymmetric Polyetherimide Membrane For co2 n2 Separation
The climate change becomes the global challenges due to the increasing earth’s surface temperature. This phenomenon was aggravated by the expansion of industrial activities due to the increasing emissions of the greenhouse gas mainly CO2. This makes the separation of CO2 from flue gas attracted r...
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| 主要作者: | |
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| 格式: | Thesis |
| 語言: | English |
| 出版: |
2017
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| 主題: | |
| 在線閱讀: | http://eprints.usm.my/45758/1/Synthesis%20Of%20Asymmetric%20Polyetherimide%20Membrane%20For%20co2%20n2%20Separation.pdf |
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| 總結: | The climate change becomes the global challenges due to the increasing
earth’s surface temperature. This phenomenon was aggravated by the expansion of
industrial activities due to the increasing emissions of the greenhouse gas mainly
CO2. This makes the separation of CO2 from flue gas attracted research interest due
to increasing demand for energy and the need for more energy efficient and
environmental friendly gas separation technique. Most of the flue gases are coproduced
with CO2 which needs to be removed in order to have a clean environment.
Dry-wet phase inversion process is one of the techniques that were adopted
in this work to further improve the membrane performance. The adopted technique
used to performed the dry-wet phase inversion is to have a dense asymmetric and a
less pores at the surface of the membrane to allow a more selective CO2. The use of
higher free standing time prior being immersed in coagulation is expected to solve
this problem. The optimum PEI polymer concentration was found to be at 30 wt. %. At this
concentration, the membrane has a dense skin layer, a sponge-like structure with
uniform finger-like macrovoid at the sub-layer. The produced membrane has CO2
permeance of 500.2 GPU with selectivity of 1.43. The casting thickness effect was
investigated and the optimum casting thickness is found at 300 μm. At higher casting
thickness, the finger-like macrovoid is minimal with a thick skin layer of 16.84 μm.
The utilization of soft coagulant such as isopropanol leads to delay demixing with
thick skin layer and almost complete sponge-like structure. This membrane gives
CO2 permeance of 5.49 GPU and a CO2/N2 selectivity of 11.44. Also, coagulant bath
temperature was used to study condition of coagulant that could favour higher CO2
selectivity. At lower coagulation bath temperature of 0 ⁰C, the membrane structure
has a complete spongy-like structure with a thickness of approximately 88.06 μm.
The lower coagulation bath temperature favours the membrane separation in this
condition with CO2 permeancce of 3.41 GPU and selectivity of 18.94. Meanwhile,
there is development of finger-like macrovoid at higher coagulation bath temperature
of 30 ⁰C upward with increasing thickness of the membrane. However, PEI
membranes with a free standing time (FST) prior immersion into coagulation bath
improved the CO2 separation performance. These membranes at 30 min (FST)
showed CO2 permeance of 3.35 GPU combined with a CO2/N2 selectivity of 29.79.
These membranes were found to acquire good control in producing the PEI
membrane for CO2 separation. Generally, the overall results showed the PEI membrane is able to producegood selectivity compared to other polymer for CO2 separation. It can be concluded
that the PEI membrane is comparable for CO2 separation with good selectivity. |
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