SAPO-18 and SAPO-34 catalysts for propylene production from the oligomerization-cracking of ethylene or 1-butene

[1]  J. Bilbao,et al.  Selective dealumination of HZSM-5 zeolite boosts propylene by modifying 1-butene cracking pathway , 2017 .

[2]  S. M. Sadrameli.  Thermal/catalytic cracking of liquid hydrocarbons for the production of olefins: A state-of-the-art review II: Catalytic cracking review , 2016 .

[3]  S. Ernst,et al.  Influence of the pore architecture on the selective conversion of ethene to propene and butenes over medium pore zeolites , 2016 .

[4]  J. Čejka,et al.  Catalytic cracking of Arabian Light VGO over novel zeolites as FCC catalyst additives for maximizing propylene yield , 2016 .

[5]  J. Bilbao,et al.  Effect of the Acidity of HZSM-5 Zeolite and the Binder in the DME Transformation to Olefins , 2016 .

[6]  J. McGregor,et al.  Things go better with coke: the beneficial role of carbonaceous deposits in heterogeneous catalysis , 2016 .

[7]  C. Márquez-Álvarez,et al.  Mesopore-Modified SAPO-18 with Potential Use as Catalyst for the MTO Reaction , 2016, Topics in Catalysis.

[8]  Zhongmin Liu,et al.  Methanol to Olefins (MTO): From Fundamentals to Commercialization , 2015 .

[9]  S. M. Sadrameli.  Thermal/catalytic cracking of hydrocarbons for the production of olefins: A state-of-the-art review I: Thermal cracking review , 2015 .

[10]  J. Bilbao,et al.  Modified HZSM-5 zeolites for intensifying propylene production in the transformation of 1-butene , 2014 .

[11]  J. Bilbao,et al.  Differences among the deactivation pathway of HZSM-5 zeolite and SAPO-34 in the transformation of ethylene or 1-butene to propylene , 2014 .

[12]  S. Mitchell,et al.  Effects of Binders on the Performance of Shaped Hierarchical MFI Zeolites in Methanol-to-Hydrocarbons , 2014 .

[13]  J. Bilbao,et al.  Modifications in the HZSM-5 zeolite for the selective transformation of ethylene into propylene , 2014 .

[14]  G. Lopez,et al.  Identification of the coke deposited on an HZSM-5 zeolite catalyst during the sequenced pyrolysis–cracking of HDPE , 2014 .

[15]  Zhongmin Liu,et al.  Spatial confinement effects of cage-type SAPO molecular sieves on product distribution and coke formation in methanol-to-olefin reaction , 2014 .

[16]  Yue M. Liu,et al.  Acid strength controlled reaction pathways for the catalytic cracking of 1-butene to propene over ZSM-5 , 2014 .

[17]  B. Weckhuysen,et al.  Spatial Distribution of Zeolite ZSM‐5 within Catalyst Bodies Affects Selectivity and Stability of Methanol‐to‐Hydrocarbons Conversion , 2013 .

[18]  M. Lemos,et al.  1-Butene oligomerization over ZSM-5 zeolite: Part 1 – Effect of reaction conditions , 2013 .

[19]  Shengfu Ji,et al.  Preparation of modified Ce-SAPO-34 catalysts and their catalytic performances of methanol to olefins , 2013 .

[20]  Sharon Mitchell,et al.  From powder to technical body: the undervalued science of catalyst scale up. , 2013, Chemical Society reviews.

[21]  S. Norsic,et al.  Study of ethylene/2-butene cross-metathesis over W-H/Al2O3 for propylene production: Effect of the temperature and reactant ratios on the productivity and deactivation , 2013 .

[22]  Chao Duan,et al.  Comparative studies of ethanol to propylene over HZSM-5/SAPO-34 catalysts prepared by hydrothermal synthesis and physical mixture , 2013 .

[23]  Biaohua Chen,et al.  Theoretical study on the cracking reaction catalyzed by a solid acid with zeolitic structure: The catalytic cracking of 1-hexene on the surface of H-ZSM-5 , 2013 .

[24]  De Chen,et al.  A methanol to olefins review: Diffusion, coke formation and deactivation on SAPO type catalysts , 2012 .

[25]  S. Kaskel,et al.  Carbon templated SAPO-34 with improved adsorption kinetics and catalytic performance in the MTO-reaction , 2012 .

[26]  R. Halladj,et al.  Methanol conversion to light olefins over sonochemically prepared SAPO-34 nanocatalyst , 2012 .

[27]  J. Bilbao,et al.  Effect of operating conditions on the coke nature and HZSM-5 catalysts deactivation in the transformation of crude bio-oil into hydrocarbons , 2012 .

[28]  Zhongmin Liu,et al.  An effective route to improve the catalytic performance of SAPO-34 in the methanol-to-olefin reaction , 2012 .

[29]  T. Baba,et al.  Effect of morphology and particle size of ZSM-5 on catalytic performance for ethylene conversion and heptane cracking , 2012 .

[30]  M. Artetxe,et al.  Effect of the acidity of the HZSM-5 zeolite catalyst on the cracking of high density polyethylene in a conical spouted bed reactor , 2012 .

[31]  S. Norsic,et al.  Production of Propylene from 1-Butene on Highly Active “Bi-Functional Single Active Site” Catalyst: Tungsten Carbene-Hydride Supported on Alumina , 2011 .

[32]  Ramin Karimzadeh,et al.  Catalytic cracking of hydrocarbons over modified ZSM-5 zeolites to produce light olefins: A review , 2011 .

[33]  D. Akporiaye,et al.  Direct observation of catalyst behaviour under real working conditions with X-ray diffraction: Comparing SAPO-18 and SAPO-34 methanol to olefin catalysts , 2011 .

[34]  J. Bilbao,et al.  Hydrothermal stability of HZSM-5 catalysts modified with Ni for the transformation of bioethanol into hydrocarbons , 2010 .

[35]  Javier Bilbao,et al.  Selective production of olefins from bioethanol on HZSM-5 zeolite catalysts treated with NaOH , 2010 .

[36]  S. Kawauchi,et al.  Key role of the pore volume of zeolite for selective production of propylene from olefins. , 2010, Physical chemistry chemical physics : PCCP.

[37]  Chaohe Yang,et al.  Study on the Oligomerization of Ethylene in Fluidized Catalytic Cracking (FCC) Dry Gas over Metal-Loaded HZSM-5 Catalysts† , 2010 .

[38]  T. Baba,et al.  Influence of Si distribution in framework of SAPO-34 and its particle size on propylene selectivity and production rate for conversion of ethylene to propylene. , 2009, Physical chemistry chemical physics : PCCP.

[39]  Qinghong Zhang,et al.  Catalytic Conversion of Ethylene to Propylene and Butenes over H-ZSM-5 , 2009 .

[40]  Fernando Ramôa Ribeiro,et al.  Prevention of zeolite deactivation by coking , 2009 .

[41]  J. M. Arandes,et al.  Effect of the support acidity on the aromatic ring-opening of pyrolysis gasoline over Pt/HZSM-5 catalysts , 2009 .

[42]  G. Seo,et al.  IR study on methanol-to-olefin reaction over zeolites with different pore structures and acidities , 2009 .

[43]  A. Marcilla,et al.  Evolution of the deactivation mode and nature of coke of HZSM-5 and USY zeolites in the catalytic cracking of low-density polyethylene during successive cracking runs , 2009 .

[44]  F. Wei,et al.  Kinetics of the reactions of the light alkenes over SAPO-34 , 2008 .

[45]  C. P. Nicolaides,et al.  Homogeneous metathesis for the production of propene from butene , 2008 .

[46]  J. M. Arandes,et al.  Effect of catalyst properties on the cracking of polypropylene pyrolysis waxes under FCC conditions , 2008 .

[47]  Waldemar Liebner,et al.  Lurgi's Methanol To Propylene (MTP®) Report on a successful commercialisation , 2007 .

[48]  Weimin Yang,et al.  Catalytic cracking reactions of C4-olefin over zeolites H-ZSM-5, H-mordenite and H-SAPO-34 , 2007 .

[49]  T. Baba,et al.  Highly selective conversion of ethene to propene over SAPO-34 as a solid acid catalyst , 2006 .

[50]  K. Góra-Marek,et al.  IR studies of the formation of ammonia dimers in zeolites TON , 2006 .

[51]  J. Teng,et al.  Synthesis of ZSM-48 zeolites and their catalytic performance in C4-olefin cracking reactions , 2006 .

[52]  I. Miracca,et al.  Dehydrogenation of paraffins: synergies between catalyst design and reactor engineering , 2006 .

[53]  Terje Fuglerud,et al.  Recent advancements in ethylene and propylene production using the UOP/Hydro MTO process , 2005 .

[54]  Longya Xu,et al.  Catalytic cracking of C4 alkenes to propene and ethene : Influences of zeolites pore structures and Si/Al2 ratios , 2005 .

[55]  B. Wichterlová,et al.  Cracking of pentenes to C2–C4 light olefins over zeolites and zeotypes: Role of topology and acid site strength and concentration , 2005 .

[56]  J. Bilbao,et al.  Role of acidity and microporous structure in alternative catalysts for the transformation of methanol into olefins , 2005 .

[57]  M. Hunger,et al.  Thermal stability and dehydroxylation of Brønsted acid sites in silicoaluminophosphates H-SAPO-11, H-SAPO-18, H-SAPO-31, and H-SAPO-34 investigated by multi-nuclear solid-state NMR spectroscopy , 2002 .

[58]  Weiguo Song,et al.  Aromatic Hydrocarbon Formation in HSAPO-18 Catalysts: Cage Topology and Acid Site Density , 2002 .

[59]  Michael Hunger,et al.  In situ MAS NMR spectroscopic investigation of the conversion of methanol to olefins on silicoaluminophosphates SAPO-34 and SAPO-18 under continuous flow conditions , 2001 .

[60]  L. Kevan,et al.  Catalytic Study of Methanol-to-Olefins Conversion in Four Small-Pore Silicoaluminophosphate Molecular Sieves: Influence of the Structural Type, Nickel Incorporation, Nickel Location, and Nickel Concentration , 2000 .

[61]  D. Akporiaye,et al.  Synthesis, characterization and catalytic testing of SAPO-18, MgAPO-18, and ZnAPO-18 in the MTO reaction , 1996 .

[62]  R. P. Townsend,et al.  Silicoaluminophosphate number eighteen (SAPO-18): a new microporous solid acid catalyst , 1994 .

[63]  Frederick J. Krambeck,et al.  Chemistry of olefin oligomerization over ZSM-5 catalyst , 1988 .

[64]  Brent M. T. Lok,et al.  Silicoaluminophosphate molecular sieves: another new class of microporous crystalline inorganic solids , 1984 .