2017
DOI: 10.1016/j.fuproc.2017.01.050
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Catalytic cracking of vacuum gasoil over -SVR, ITH, and MFI zeolites as FCC catalyst additives

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Cited by 32 publications
(14 citation statements)
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“…It has been reported that the structural and acidic properties of Al-ITH make it a good alternative to ZSM-5 as shape selective FCC additive for producing propylene. [27,49] Thus, the catalytic behavior of the Al-ITH sample and two ZSM-5 samples have been compared for catalytic cracking of a vacuum gasoil (VGO; see the Supporting Information, Table S8 for VGO properties) in a microactivity test unit. [28] The results are shown in the Supporting Information, Figures S15-S17.…”
Section: Before the Crystallization Only An Amorphous Phase Is Obsermentioning
confidence: 99%
“…It has been reported that the structural and acidic properties of Al-ITH make it a good alternative to ZSM-5 as shape selective FCC additive for producing propylene. [27,49] Thus, the catalytic behavior of the Al-ITH sample and two ZSM-5 samples have been compared for catalytic cracking of a vacuum gasoil (VGO; see the Supporting Information, Table S8 for VGO properties) in a microactivity test unit. [28] The results are shown in the Supporting Information, Figures S15-S17.…”
Section: Before the Crystallization Only An Amorphous Phase Is Obsermentioning
confidence: 99%
“…It has been reported that the structural and acidic properties of Al-ITH make it ag ood alternative to ZSM-5 as shape selective FCC additive for producing propylene. [27,49] Thus,t he catalytic behavior of the Al-ITH sample and two ZSM-5 samples have been compared for catalytic cracking of av acuum gasoil (VGO;s ee the Supporting Information, Table S8 for VGOp roperties) in am icroactivity test unit. [28] Ther esults are shown in the Supporting Information, Figures S15-S17.…”
Section: Before the Crystallization Only An Amorphous Phase Is Obsermentioning
confidence: 99%
“…[3] They attributed this difference to a higher shape selectivity towards propene caused by the narrower pore dimensions, a finding that was confirmed in subsequent work. [5] ITQ-13 was also found to give a product spectrum different from other zeolite catalysts (ZSM-5, MCM-22) in methanol-to-hydrocarbon (MTH) conversions, potentially enhancing the flexibility of the MTH process in the context of varying demands for different products. [6] ITQ-13 is the type material of the ITH framework, [7] which can be decomposed into four types of discrete cages: double-four ring (d4r) cages (face symbol [4 6 ], labelled t-cub in the nomenclature of natural tilings [8] ), lau cages (face symbol [4 2 •6 4 ], t-lau), stf cages (face symbol [4•5 6 ], t-nuh) and [4•5 2 •6 2 ] cages (t-mel).…”
Section: Introductionmentioning
confidence: 99%