Abstract
An asymmetric carbon membrane was prepared by coating alcohol solution of novolac phenol-formaldehyde resin containing a little hexamine on a porous resin support from the same material. After drying in air for two days at room temperature, the coated support was heated at 150 °C for 1 h in air (heating rate: 0.5 °C/min) and then carbonized at 800 °C (heating rate: 0.5 °C/min) in Ar atmosphere. The support and the membrane layer were carbonized simultaneously. The coating-pyrolysis cycle only needed one time. SEM photographs showed the carbon membrane had an asymmetric structure formed by a dense skin layer with a thickness of around 35 μm and a porous substrate. Pure gases of different molecular size (H2, CO2, O2, N2 and CH4) were used to test the carbon membrane permeance property. The membrane has a good selectivity for H2/N2 and H2/CH4 with H2 permeance of 4.05 × 10-6 cm3 cm-2 s-1 cmHg-1. The permeance is independent of pressure. The results indicate that the gases transport through the membrane according to molecular sieve mechanism. © 2007 Elsevier B.V. All rights reserved.
| Original language | English |
|---|---|
| Pages (from-to) | 80-85 |
| Journal | Journal of Membrane Science |
| Volume | 303 |
| Issue number | 1-2 |
| DOIs | |
| Publication status | Published - 15 Oct 2007 |
| Externally published | Yes |
Bibliographical note
Publication details (e.g. title, author(s), publication statuses and dates) are captured on an “AS IS” and “AS AVAILABLE” basis at the time of record harvesting from the data source. Suggestions for further amendments or supplementary information can be sent to [email protected].Research Keywords
- Carbon membrane
- Gas separation
- Molecular sieve
- Phenol-formaldehyde resin