Abstract
Human activity have been emitting greenhouse gases into the atmosphere for a long time. To separate these gases, especially CO2 and CH4, polymeric membranes have been used in the chemical industry as this technology has a lower power consumption when compared to other separation processes. In this work, α-alumina ceramic tubes (support) were internally impregnated with poly(fluoride vinylidene) (PVDF), and the permeability and selectivity of the membrane to CO2, CH4, and O2 was studied. All membranes (MT1 and MT2), when tested at low pressures, presented higher selectivity to CH4 gas, and with increasing pressure the selectivity for CO2 increased as well. The MT2 membrane was more efficient in the separation of CO2/CH4 gases, which is an important result because both of them are the most impacting gases to the greenhouse effect and the most difficult to separate using membrane process.
Acknowledgment
The authors would like to thank the UNIVILLE, UCS and CNPq.
Notes
Presented at the International Conference on Desalination for the Environment, Clean Water and Energy, European Desalination Society, 23–26 April 2012, Barcelona, Spain