Modeling of strippers for CO₂ capture by aqueous amines
This work evaluates stripper performance for CO₂ capture using seven potential solvent formulations and seven stripper configurations. Equilibrium and rate models were developed in Aspen Custom Modeler (ACM). The temperature approach on the hot side of the cross exchanger was varied between 5 - 10°C...
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| Format: | Others |
| Language: | English |
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2008
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| Online Access: | http://hdl.handle.net/2152/3134 |