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Conversion of methane and carbon dioxide using catalytic membranes: New effective method for syngas production (Omn.Univ.Europ.)

Conversion of methane and carbon dioxide using catalytic membranes: New effective method for syngas production (Omn.Univ.Europ.)

Conversion of methane and carbon dioxide using catalytic membranes: New
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Conversion of methane and carbon dioxide using catalytic membranes: New effective method for syngas production (Omn.Univ.Europ.) Paperback - 2011

by Fedotov, Alexey

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Omniscriptum, 2011-05-10. paperback. New. 5.91x0.17x8.66. Buy with confidence. Excellent Customer Service & Return policy.
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  • Title Conversion of methane and carbon dioxide using catalytic membranes: New effective method for syngas production (Omn.Univ.Europ.)
  • Author Fedotov, Alexey
  • Binding Paperback
  • Condition New
  • Pages 72
  • Volumes 1
  • Language FRE
  • Publisher Omniscriptum
  • Publication date 2011-05-10
  • Bookseller's Inventory # DADAX6131574863
  • ISBN 9786131574863 / 6131574863
  • Weight 0.26 lbs (0.12 kg)
  • Dimensions 9 x 6 x 0.17 in (22.86 x 15.24 x 0.43 cm)
  • Size 5.91x0.17x8.66
  • Category Science
  • Quantity available 6

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Reader reviews for Conversion of methane and carbon dioxide using catalytic membranes: New effective method for syngas production (Omn.Univ.Europ.)

From the publisher

This study reports the development of a new process to convert methane and carbon dioxide into syngas from non-oil resources. The process uses membrane catalytic systems (MCS) that support heterogeneous catalytic reactions in gaseous phase in membrane channels. An active surface of the catalysts formed inside the micro- channels is low in term of area, but it is characterized by a high value of the catalyst surface/volume ratio, which induces a high efficiency of heterogeneous catalysis. Such MCS, having 10⌃8 pores per cm2 of surface, can be considered as a set of nano reactors. MCS are formed from alkoxy derivatives and precursor metal complex containing between 0.008 and 0.055% by weight of nano- components mono-and bimetallic active distributed evenly in the channels. For systems La-Ce/Ni-Al and Pd-Mn/Ni-Al, productivities of 10500 and 7500 l/h∙dm3 were respectively obtained at 650 C with a composition of syngas H2/СО ranging from 0.63 to 1.25 and a conversion rate of 50% with a CH4/СО2 (1/1) feed. Thus MCS is an order of magnitude more efficient than a fixed bed reactor of the same catalyst. A catalytic synergy has been demonstrated for the system Pd-Mn.
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