Aufbau und katalytische Aktivität hierarchisch strukturierter Oxid-Katalysatoren: Teil 2

Research output: Contribution to specialist publicationContribution in non-scientific journalTransfer

Authors

  • Jean Boris Stelzer
  • Daniela Habel
  • Marga Martina Pohl
  • Hendrick Kosslick
  • Egbert Feike
  • Jürgen Caro
  • Helmut Schubert

External Research Organisations

  • Technische Universität Berlin
  • Institut für Angewandte Chemie Berlin-Adlershof e.V
View graph of relations

Details

Translated title of the contributionStructure and catalytic activity of hierarchically structured oxide catalysts - 2
Original languageGerman
Pages1581,1656-1660
Volume75
Issue number11
JournalChemie-Ingenieur-Technik
Publication statusPublished - Nov 2003

Abstract

The catalytic oxidation dehydrogenation of propane to propylene was studied. Three possible active components, namely, TiO2, V2O5 and MoO3, were mustered onto two TiO2 carriers in a combinatorial sequence. The two TiO2 carriers were in the anatase modification (micrometer-TiO2 spray granulate and nanometer TiO2 from titanyl sulfate hydrolysis) with various BET surfaces. Using these two TiO2 carriers it is indicated that through a hierarchically constructed catalyst the propylene yield can be increased. The catalysts that contained the active component V2O5 or MoO3 in a nonostructured TiO2 intermediate layer in the TiO2 carrier proper, have a higher propylene yield in the oxidative propane dehydrogenation than catalyst without nanostructured TiO2 intermediate layer. Activity and propylene yields of the catalytically effective oxides increase in the sequence TiO2 < MoO3 < V2O5. Considering the various morphologies of the catalysts, the influence of an exchange effect of the carrier with the active components is clear. Although the content in active components was about equal, different catalyst morphologies gave different catalytic results. With the measurements to date the proposition of free reaction centers can not be completely confirmed or refuted. It remains to establish an influence of the carrier as the object of further studies using special high resolution structure studies (TEM, EXAFS, fine structure studies).

ASJC Scopus subject areas

Cite this

Aufbau und katalytische Aktivität hierarchisch strukturierter Oxid-Katalysatoren: Teil 2. / Stelzer, Jean Boris; Habel, Daniela; Pohl, Marga Martina et al.
In: Chemie-Ingenieur-Technik, Vol. 75, No. 11, 11.2003, p. 1581,1656-1660.

Research output: Contribution to specialist publicationContribution in non-scientific journalTransfer

Stelzer, JB, Habel, D, Pohl, MM, Kosslick, H, Feike, E, Caro, J & Schubert, H 2003, 'Aufbau und katalytische Aktivität hierarchisch strukturierter Oxid-Katalysatoren: Teil 2' Chemie-Ingenieur-Technik, vol. 75, no. 11, pp. 1581,1656-1660.
Stelzer, J. B., Habel, D., Pohl, M. M., Kosslick, H., Feike, E., Caro, J., & Schubert, H. (2003). Aufbau und katalytische Aktivität hierarchisch strukturierter Oxid-Katalysatoren: Teil 2. Chemie-Ingenieur-Technik, 75(11), 1581,1656-1660.
Stelzer JB, Habel D, Pohl MM, Kosslick H, Feike E, Caro J et al. Aufbau und katalytische Aktivität hierarchisch strukturierter Oxid-Katalysatoren: Teil 2. Chemie-Ingenieur-Technik. 2003 Nov;75(11):1581,1656-1660.
Stelzer, Jean Boris ; Habel, Daniela ; Pohl, Marga Martina et al. / Aufbau und katalytische Aktivität hierarchisch strukturierter Oxid-Katalysatoren : Teil 2. In: Chemie-Ingenieur-Technik. 2003 ; Vol. 75, No. 11. pp. 1581,1656-1660.
Download
@misc{6a2531a0da0a4bf59eeafb5ddf9f764f,
title = "Aufbau und katalytische Aktivit{\"a}t hierarchisch strukturierter Oxid-Katalysatoren: Teil 2",
abstract = "The catalytic oxidation dehydrogenation of propane to propylene was studied. Three possible active components, namely, TiO2, V2O5 and MoO3, were mustered onto two TiO2 carriers in a combinatorial sequence. The two TiO2 carriers were in the anatase modification (micrometer-TiO2 spray granulate and nanometer TiO2 from titanyl sulfate hydrolysis) with various BET surfaces. Using these two TiO2 carriers it is indicated that through a hierarchically constructed catalyst the propylene yield can be increased. The catalysts that contained the active component V2O5 or MoO3 in a nonostructured TiO2 intermediate layer in the TiO2 carrier proper, have a higher propylene yield in the oxidative propane dehydrogenation than catalyst without nanostructured TiO2 intermediate layer. Activity and propylene yields of the catalytically effective oxides increase in the sequence TiO2 < MoO3 < V2O5. Considering the various morphologies of the catalysts, the influence of an exchange effect of the carrier with the active components is clear. Although the content in active components was about equal, different catalyst morphologies gave different catalytic results. With the measurements to date the proposition of free reaction centers can not be completely confirmed or refuted. It remains to establish an influence of the carrier as the object of further studies using special high resolution structure studies (TEM, EXAFS, fine structure studies).",
author = "Stelzer, {Jean Boris} and Daniela Habel and Pohl, {Marga Martina} and Hendrick Kosslick and Egbert Feike and J{\"u}rgen Caro and Helmut Schubert",
year = "2003",
month = nov,
language = "Deutsch",
volume = "75",
pages = "1581,1656--1660",
journal = "Chemie-Ingenieur-Technik",
issn = "0009-286X",
publisher = "Wiley-VCH Verlag",

}

Download

TY - GEN

T1 - Aufbau und katalytische Aktivität hierarchisch strukturierter Oxid-Katalysatoren

T2 - Teil 2

AU - Stelzer, Jean Boris

AU - Habel, Daniela

AU - Pohl, Marga Martina

AU - Kosslick, Hendrick

AU - Feike, Egbert

AU - Caro, Jürgen

AU - Schubert, Helmut

PY - 2003/11

Y1 - 2003/11

N2 - The catalytic oxidation dehydrogenation of propane to propylene was studied. Three possible active components, namely, TiO2, V2O5 and MoO3, were mustered onto two TiO2 carriers in a combinatorial sequence. The two TiO2 carriers were in the anatase modification (micrometer-TiO2 spray granulate and nanometer TiO2 from titanyl sulfate hydrolysis) with various BET surfaces. Using these two TiO2 carriers it is indicated that through a hierarchically constructed catalyst the propylene yield can be increased. The catalysts that contained the active component V2O5 or MoO3 in a nonostructured TiO2 intermediate layer in the TiO2 carrier proper, have a higher propylene yield in the oxidative propane dehydrogenation than catalyst without nanostructured TiO2 intermediate layer. Activity and propylene yields of the catalytically effective oxides increase in the sequence TiO2 < MoO3 < V2O5. Considering the various morphologies of the catalysts, the influence of an exchange effect of the carrier with the active components is clear. Although the content in active components was about equal, different catalyst morphologies gave different catalytic results. With the measurements to date the proposition of free reaction centers can not be completely confirmed or refuted. It remains to establish an influence of the carrier as the object of further studies using special high resolution structure studies (TEM, EXAFS, fine structure studies).

AB - The catalytic oxidation dehydrogenation of propane to propylene was studied. Three possible active components, namely, TiO2, V2O5 and MoO3, were mustered onto two TiO2 carriers in a combinatorial sequence. The two TiO2 carriers were in the anatase modification (micrometer-TiO2 spray granulate and nanometer TiO2 from titanyl sulfate hydrolysis) with various BET surfaces. Using these two TiO2 carriers it is indicated that through a hierarchically constructed catalyst the propylene yield can be increased. The catalysts that contained the active component V2O5 or MoO3 in a nonostructured TiO2 intermediate layer in the TiO2 carrier proper, have a higher propylene yield in the oxidative propane dehydrogenation than catalyst without nanostructured TiO2 intermediate layer. Activity and propylene yields of the catalytically effective oxides increase in the sequence TiO2 < MoO3 < V2O5. Considering the various morphologies of the catalysts, the influence of an exchange effect of the carrier with the active components is clear. Although the content in active components was about equal, different catalyst morphologies gave different catalytic results. With the measurements to date the proposition of free reaction centers can not be completely confirmed or refuted. It remains to establish an influence of the carrier as the object of further studies using special high resolution structure studies (TEM, EXAFS, fine structure studies).

UR - http://www.scopus.com/inward/record.url?scp=0347930362&partnerID=8YFLogxK

M3 - Beitrag in Publikumszeitung/-zeitschrift

AN - SCOPUS:0347930362

VL - 75

SP - 1581,1656-1660

JO - Chemie-Ingenieur-Technik

JF - Chemie-Ingenieur-Technik

SN - 0009-286X

ER -