2011
DOI: 10.1016/j.energy.2010.11.023
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A novel water perm-selective membrane dual-type reactor concept for Fischer–Tropsch synthesis of GTL (gas to liquid) technology

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Cited by 59 publications
(27 citation statements)
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References 43 publications
(41 reference statements)
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“…Hence, the authors suggested hydroxy sodalite zeolite membranes with a layer thickness of 2 μm as auspicious candidate for the in situ water removal due to their extraordinary separation and permeation performance demonstrated as well earlier by Khajavi et al [198]. Recently, a novel reactor configuration denoted as fixed-bed membrane reactor followed by fluidized-bed membrane reactor (FMFMDR) has been proposed for high temperature Fischer-Tropsch synthesis, in particular gasoline production from syngas [199,200]. This configuration combines a fixed-bed water permselective membrane reactor equipped with H-SOD zeolite membrane coated on α-Al2O3 substrate and a fluidized-bed hydrogen permselective membrane reactor equipped with Pd-Ag membrane.…”
Section: Equilibrium Shift By Water Removalmentioning
confidence: 97%
“…Hence, the authors suggested hydroxy sodalite zeolite membranes with a layer thickness of 2 μm as auspicious candidate for the in situ water removal due to their extraordinary separation and permeation performance demonstrated as well earlier by Khajavi et al [198]. Recently, a novel reactor configuration denoted as fixed-bed membrane reactor followed by fluidized-bed membrane reactor (FMFMDR) has been proposed for high temperature Fischer-Tropsch synthesis, in particular gasoline production from syngas [199,200]. This configuration combines a fixed-bed water permselective membrane reactor equipped with H-SOD zeolite membrane coated on α-Al2O3 substrate and a fluidized-bed hydrogen permselective membrane reactor equipped with Pd-Ag membrane.…”
Section: Equilibrium Shift By Water Removalmentioning
confidence: 97%
“…It can be considered as a capable candidate for water separation in FTS which requires a high H 2 O/H 2 perm-selectivity [23]. The extensive literature survey regarding the H-SOD membrane and effect of in situ water removal on FTS can be found in the previous work [13].…”
Section: Membrane Reactormentioning
confidence: 99%
“…Various coupling schemes were proposed by Yin et al [8] and Kulkarni and Dudukovic [9]. The extensive literature review about FTS can be found in previous publications by Marvast et al [10], RIPI-NIOC [11], Forghani et al [12] and Rahimpour et al [13][14][15][16].…”
Section: Introductionmentioning
confidence: 99%
“…The test tube was then placed in an oil bath and heated up to the temperature desired (190)(191)(192)(193)(194)(195)(196)(197)(198)(199)(200) • C). After the reaction, the crude was cooled, diluted with HPLC acetone, filtered and analyzed.…”
Section: Methodsmentioning
confidence: 99%
“…Hence, the authors suggested hydroxy sodalite zeolite membranes with a layer thickness of 2 µm as auspicious candidate for the in situ water removal due to their extraordinary separation and permeation performance demonstrated as well earlier by Khajavi et al [198]. Recently, a novel reactor configuration denoted as fixed-bed membrane reactor followed by fluidized-bed membrane reactor (FMFMDR) has been proposed for high temperature Fischer-Tropsch synthesis, in particular gasoline production from syngas [199,200]. This configuration combines a fixed-bed water permselective membrane reactor equipped with H-SOD zeolite membrane coated on α-Al 2 O 3 substrate and a fluidized-bed hydrogen permselective membrane reactor equipped with Pd-Ag membrane.…”
Section: Equilibrium Shift By Water Removalmentioning
confidence: 99%