Abstract
SSZ-13 membranes are highly desired for hydrogen separation from hydrocarbons. The H2/CH4 separation using tubular large-area SSZ-13 membranes with effective membrane area of 180 cm2 were reported for the first time. The up-scaled SSZ-13 membranes consisted of a uniform zeolite layer with a thickness of 3.2 μm along the entire tube. The membrane exhibited H2 permeance, H2 flux, and H2/CH4 selectivity of 1.38 × 10-7 mol m−2 s−1 Pa−1 (410 GPU), 7.0 × 10-3 mol m−2 s−1 and 67.2 for a 50–50 vol% H2/CH4 mixture, respectively, at pressure drop of 0.2 MPa. This separation performance was comparable to the reported ones of small-area zeolite membranes. The effects of conditions such as temperature, pressure, and feed flow rate on the separation performance of the large-area SSZ-13 membranes were investigated. Concentration polarization index was estimated to study and clarify the effect of concentration polarization on separation performance. Furthermore, the separation performance in a simulated refinery dry gas containing typical impurities was also evaluated. The large-area SSZ-13 membrane exhibited stable and good separation performance during the repeated separation tests and long-term storage. The results indicates that the membranes have great potential for H2 separation from CH4.
Original language | English |
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Article number | 133486 |
Journal | Separation and Purification Technology |
Volume | 372 |
DOIs | |
State | Published - 1 Nov 2025 |
Keywords
- Gas separation
- H/CH separation
- Refinery dry gas
- SSZ-13 membrane