2014
DOI: 10.1016/j.ijhydene.2014.05.181
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Synthesis, characterization and corrosion performance evaluation of DDR membrane for H 2 separation from HI decomposition reaction

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Cited by 18 publications
(5 citation statements)
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“…, were found to be consistently below five, [29] which is lower than the value reported by Muhammad et al [30] The microwave-assisted DDR zeolite membrane synthesis is also an interesting pathway towards reducing the processing time of the reaction. Few mathematical models of membrane-based gas separation processes are primarily dedicated towards finding the molar diffusivities for mixture of light gases and pure gases.…”
Section: Introductioncontrasting
confidence: 55%
See 1 more Smart Citation
“…, were found to be consistently below five, [29] which is lower than the value reported by Muhammad et al [30] The microwave-assisted DDR zeolite membrane synthesis is also an interesting pathway towards reducing the processing time of the reaction. Few mathematical models of membrane-based gas separation processes are primarily dedicated towards finding the molar diffusivities for mixture of light gases and pure gases.…”
Section: Introductioncontrasting
confidence: 55%
“…71-0962. [29] Therefore, the formation of crystalline DDR zeolite layer on the pre-existing clay-alumina tubular support, which was seeded on the support within 2 days, was confirmed by the XRD study.…”
Section: Membrane Characterizationmentioning
confidence: 74%
“…For example, the pore aperture of zeolite SAPO-34 (CHA structure with 8-MR pores) is $0.38 nm, which allows the selective diffusion of CO 2 (kinetic diameter 0.33 nm) to the inner pore structure, while excluding the larger CH 4 (0.38 nm) molecule. 6 Among 8-MR zeolites, SAPO-34 (CHA type), [6][7][8][9][10][11][12][13][14] CHA [15][16][17] and DDR membranes [18][19][20][21][22] have been extensively studied for CO 2 separation. Great CO 2 -CH 4 separation performance was realized on SAPO-34 zeolite membrane; however, the hydrophilic nature of SAPO-34 zeolite makes it difficult for the application of SAPO-34 membrane for natural gas separation.…”
mentioning
confidence: 99%
“…The DDR membrane was defective after calcination. The membrane was repaired by chemical vapor deposition (CVD) with silica for six days at 823 K. The high H 2 /CO 2 selectivity, which was not observed by other researchers for DDR zeolite membranes [118,119], might be caused by a continuous amorphous silica film acting as an effective membrane for H 2 /CO 2 separation. [101,[115][116][117][118][119][120][121][122][123].…”
Section: H 2 /Comentioning
confidence: 87%
“…Figure3. H 2 /CO 2 separation performance for different types of small-pore zeolite membranes[101,[115][116][117][118][119][120][121][122][123]. * denotes results from pure gas permeation tests.…”
mentioning
confidence: 99%