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Preparation of Zeolite T Membranes by a Two-Step Temperature Process for CO sub(2) Separation
A thin and well-intergrown zeolite T membrane with high CO sub(2) permeability and selectivity was rapidly prepared on seeded tubular supports by the two-step varying-temperature hydrothermal synthesis process (two-step method). The influence of synthesis parameters such as synthesis temperature and...
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Published in: | Industrial & engineering chemistry research 2013-11, Vol.52 (46), p.16364-16374-16364-16374 |
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Main Authors: | , , , , , , , |
Format: | Article |
Language: | English |
Subjects: | |
Online Access: | Get full text |
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Summary: | A thin and well-intergrown zeolite T membrane with high CO sub(2) permeability and selectivity was rapidly prepared on seeded tubular supports by the two-step varying-temperature hydrothermal synthesis process (two-step method). The influence of synthesis parameters such as synthesis temperature and crystallization time during the two-step durations on crystals growth and separation performance was investigated systematically. The X-ray diffraction (XRD), scanning electron microscopy (SEM), and gas permeation measurements were used to characterize the as-synthesized membranes. Compared with the conventional hydrothermal synthesis at a constant temperature (one-step method), the two-step method is more effective to synthesize a thin and continuous zeolite membrane layer in short time, which fully covered the support surface. Membrane synthesis temperature during the two-step durations could seriously influence the crystal growth and CO sub(2) separation properties. It was found that a lower temperature favored nucleation, while a higher crystallization temperature promoted crystallization during the two-step method, thus improving zeolite T crystal growth and membrane separation properties. The membranes prepared by the two-step method under the optimized conditions exhibited good reproducibility, high CO sub(2) permeance, and relatively high permselectivity for the separation of CO sub(2) from CH sub(4) or N sub(2) gas mixtures. For example, CO sub(2) permeance and CO sub(2)/CH sub(4) selectivity of the membranes reached 6.2 10 super(-8) mol m super(-2) s super(-1) Pa super(-1) and 80 for the equimolar CO sub(2)/CH sub(4) binary gaseous mixtures at 35 degree C, respectively. |
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ISSN: | 0888-5885 1520-5045 |
DOI: | 10.1021/ie4025402 |