Textural Properties and Catalytic Applications of ZSM-5 Monolith Foam for Methanol Conversion

ZSM-5 monolith foam (ZMF) samples with various framework Si/Al ratios have been successfully synthesized by polyurethane foam (PUF) template method and evaluated for their catalytic performance towards methanol to propylene (MTP) reaction. The samples were tested for their textural properties using...

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Veröffentlicht in:Catalysis letters 2009-05, Vol.129 (3-4), p.408-415
Hauptverfasser: Lee, Yun-Jo, Kim, Ye-Won, Jun, Ki-Won, Viswanadham, Nagabhatla, Bae, Jong Wook, Park, Hyung-Sang
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container_issue 3-4
container_start_page 408
container_title Catalysis letters
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creator Lee, Yun-Jo
Kim, Ye-Won
Jun, Ki-Won
Viswanadham, Nagabhatla
Bae, Jong Wook
Park, Hyung-Sang
description ZSM-5 monolith foam (ZMF) samples with various framework Si/Al ratios have been successfully synthesized by polyurethane foam (PUF) template method and evaluated for their catalytic performance towards methanol to propylene (MTP) reaction. The samples were tested for their textural properties using SEM, XRD, BET surface area, pore volume and NH₃-TPD techniques revealing the formation of ZMF exhibiting about 100-300 μm range macro pores created by packed assembly of 5 μm size orthorhombic shaped ZSM-5 crystals. The ZMF samples exhibited effective activity in methanol to olefin conversion, with superior product selectivities at optimum Si/Al ratio of 250. Further, the ZMF catalyst with high macro porosity exhibited superior catalytic activity compared to its pelletized form, especially at higher feed flow rates, that signifies the importance of macro porous structure of ZMF in facilitating the enhanced mass transport for the labile diffusion of light olefins. Reaction temperature also played a vital role in determining product selectivity. At 500 °C, the catalysts exhibited the highest light olefin (C₂ [superscript equals sign]-C₄ [superscript equals sign]) selectivity and above this temperature, formation of C₅ ⁺ is prevailed at the cost of C₂ [superscript equals sign]-C₄ [superscript equals sign] revealing the accelerated occurrence of oligomerization reactions at these conditions. At optimized catalytic properties and reaction conditions, the catalyst exhibited as high as 75% selectivity to C₂-C₄ olefins, with propylene as major component (~44%).
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Foams ; Exact sciences and technology ; Flow velocity ; General and physical chemistry ; Industrial Chemistry/Chemical Engineering ; Ion-exchange ; Methanol ; Oligomerization ; Organometallic Chemistry ; Physical Chemistry ; Polyurethane foam ; Porosity ; Porous materials ; Properties (attributes) ; Propylene ; Selectivity ; Silicon ; Surface physical chemistry ; Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry ; Zeolites: preparations and properties</subject><ispartof>Catalysis letters, 2009-05, Vol.129 (3-4), p.408-415</ispartof><rights>Springer Science+Business Media, LLC 2009</rights><rights>2009 INIST-CNRS</rights><rights>Catalysis Letters is a copyright of Springer, (2009). 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The samples were tested for their textural properties using SEM, XRD, BET surface area, pore volume and NH₃-TPD techniques revealing the formation of ZMF exhibiting about 100-300 μm range macro pores created by packed assembly of 5 μm size orthorhombic shaped ZSM-5 crystals. The ZMF samples exhibited effective activity in methanol to olefin conversion, with superior product selectivities at optimum Si/Al ratio of 250. Further, the ZMF catalyst with high macro porosity exhibited superior catalytic activity compared to its pelletized form, especially at higher feed flow rates, that signifies the importance of macro porous structure of ZMF in facilitating the enhanced mass transport for the labile diffusion of light olefins. Reaction temperature also played a vital role in determining product selectivity. 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Foams</subject><subject>Exact sciences and technology</subject><subject>Flow velocity</subject><subject>General and physical chemistry</subject><subject>Industrial Chemistry/Chemical Engineering</subject><subject>Ion-exchange</subject><subject>Methanol</subject><subject>Oligomerization</subject><subject>Organometallic Chemistry</subject><subject>Physical Chemistry</subject><subject>Polyurethane foam</subject><subject>Porosity</subject><subject>Porous materials</subject><subject>Properties (attributes)</subject><subject>Propylene</subject><subject>Selectivity</subject><subject>Silicon</subject><subject>Surface physical chemistry</subject><subject>Theory of reactions, general kinetics. Catalysis. 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Microemulsions. Foams</topic><topic>Exact sciences and technology</topic><topic>Flow velocity</topic><topic>General and physical chemistry</topic><topic>Industrial Chemistry/Chemical Engineering</topic><topic>Ion-exchange</topic><topic>Methanol</topic><topic>Oligomerization</topic><topic>Organometallic Chemistry</topic><topic>Physical Chemistry</topic><topic>Polyurethane foam</topic><topic>Porosity</topic><topic>Porous materials</topic><topic>Properties (attributes)</topic><topic>Propylene</topic><topic>Selectivity</topic><topic>Silicon</topic><topic>Surface physical chemistry</topic><topic>Theory of reactions, general kinetics. Catalysis. 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The samples were tested for their textural properties using SEM, XRD, BET surface area, pore volume and NH₃-TPD techniques revealing the formation of ZMF exhibiting about 100-300 μm range macro pores created by packed assembly of 5 μm size orthorhombic shaped ZSM-5 crystals. The ZMF samples exhibited effective activity in methanol to olefin conversion, with superior product selectivities at optimum Si/Al ratio of 250. Further, the ZMF catalyst with high macro porosity exhibited superior catalytic activity compared to its pelletized form, especially at higher feed flow rates, that signifies the importance of macro porous structure of ZMF in facilitating the enhanced mass transport for the labile diffusion of light olefins. Reaction temperature also played a vital role in determining product selectivity. At 500 °C, the catalysts exhibited the highest light olefin (C₂ [superscript equals sign]-C₄ [superscript equals sign]) selectivity and above this temperature, formation of C₅ ⁺ is prevailed at the cost of C₂ [superscript equals sign]-C₄ [superscript equals sign] revealing the accelerated occurrence of oligomerization reactions at these conditions. At optimized catalytic properties and reaction conditions, the catalyst exhibited as high as 75% selectivity to C₂-C₄ olefins, with propylene as major component (~44%).</abstract><cop>Boston</cop><pub>Boston : Springer US</pub><doi>10.1007/s10562-008-9811-z</doi><tpages>8</tpages></addata></record>
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subjects Alkenes
Aluminum
Ammonia
Catalysis
Catalysts
Catalytic activity
Catalytic converters
Chemistry
Chemistry and Materials Science
Colloidal state and disperse state
Conversion
Emulsions. Microemulsions. Foams
Exact sciences and technology
Flow velocity
General and physical chemistry
Industrial Chemistry/Chemical Engineering
Ion-exchange
Methanol
Oligomerization
Organometallic Chemistry
Physical Chemistry
Polyurethane foam
Porosity
Porous materials
Properties (attributes)
Propylene
Selectivity
Silicon
Surface physical chemistry
Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry
Zeolites: preparations and properties
title Textural Properties and Catalytic Applications of ZSM-5 Monolith Foam for Methanol Conversion
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