Hydrocracking of Model Substances on Pt/H-ZSM-5 under an Imitated Fischer-Tropsch Product Gas Composition
- Standort
-
Deutsche Nationalbibliothek Frankfurt am Main
- Umfang
-
Online-Ressource
- Sprache
-
Englisch
- Erschienen in
-
In: Chemical Engineering & Technology 2023, 46(9), 1924-1934; https://doi.org/10.1002/ceat.202300203
- Ereignis
-
Veröffentlichung
- (wo)
-
Bayreuth
- (wer)
-
Universität Bayreuth
- (wann)
-
2023
- Urheber
-
Oppmann, Nicolas
Jess, Andreas
- DOI
-
10.15495/EPub_UBT_00007227
- URN
-
urn:nbn:de:bvb:703-epub-7227-8
- Rechteinformation
-
Der Zugriff auf das Objekt ist unbeschränkt möglich.
- Letzte Aktualisierung
-
14.08.2025, 11:01 MESZ
Datenpartner
Dieses Objekt wird bereitgestellt von:
Deutsche Nationalbibliothek. Bei Fragen zum Objekt wenden Sie sich bitte an den Datenpartner.
Deutsche Nationalbibliothek. Bei Fragen zum Objekt wenden Sie sich bitte an den Datenpartner.
Beteiligte
- Oppmann, Nicolas
- Jess, Andreas
- Universität Bayreuth
Entstanden
- 2023
Ähnliche Objekte (12)
Hydrocracking of Model Substances on Pt/H‐ZSM‐5 under an Imitated Fischer‐Tropsch Product Gas Composition
Design and Technoeconomic Analysis of Fischer–Tropsch Fixed‐Bed Synthesis with Cobalt‐Based Catalysts
Improving the Selectivity to Liquefied Petroleum Gas by Combining Fischer‐Tropsch Synthesis with Zeolite Cracking
Enhancing Kerosene Selectivity of Fischer-Tropsch Synthesis by Periodical Pore Drainage Via Hydrogenolysis
On the Role of Radial Dispersion in the Behavior of a Cooled Fixed‐Bed Reactor: Numerical Investigation of Fischer–Tropsch Synthesis with a Cobalt‐Based Catalyst
Design and Technoeconomic Analysis of Fischer–Tropsch Fixed-Bed Synthesis with Cobalt-Based Catalysts
Cobalt Catalyzed Fischer-Tropsch Synthesis with O₂-Containing Syngas
Improving the Selectivity to Liquefied Petroleum Gas by Combining Fischer-Tropsch Synthesis with Zeolite Cracking
Catalytic Behavior and In Situ X‐Ray Diffraction of Promoted Iron Catalysts for Fischer‐Tropsch Synthesis
Significance of Pressure Drop, Changing Molar Flow, and Formation of Steam in the Accurate Modeling of a Multi-Tubular Fischer–Tropsch Reactor with Cobalt as Catalyst
On the Role of Radial Dispersion in the Behavior of a Cooled Fixed-Bed Reactor : Numerical Investigation of Fischer–Tropsch Synthesis with a Cobalt-Based Catalyst
Catalytic Behavior and In Situ X-Ray Diffraction of Promoted Iron Catalysts for Fischer-Tropsch Synthesis
Hydrocracking of Model Substances on Pt/H‐ZSM‐5 under an Imitated Fischer‐Tropsch Product Gas Composition
Design and Technoeconomic Analysis of Fischer–Tropsch Fixed‐Bed Synthesis with Cobalt‐Based Catalysts
Improving the Selectivity to Liquefied Petroleum Gas by Combining Fischer‐Tropsch Synthesis with Zeolite Cracking
Enhancing Kerosene Selectivity of Fischer-Tropsch Synthesis by Periodical Pore Drainage Via Hydrogenolysis
On the Role of Radial Dispersion in the Behavior of a Cooled Fixed‐Bed Reactor: Numerical Investigation of Fischer–Tropsch Synthesis with a Cobalt‐Based Catalyst
Design and Technoeconomic Analysis of Fischer–Tropsch Fixed-Bed Synthesis with Cobalt-Based Catalysts
Cobalt Catalyzed Fischer-Tropsch Synthesis with O₂-Containing Syngas
Improving the Selectivity to Liquefied Petroleum Gas by Combining Fischer-Tropsch Synthesis with Zeolite Cracking
Catalytic Behavior and In Situ X‐Ray Diffraction of Promoted Iron Catalysts for Fischer‐Tropsch Synthesis
Significance of Pressure Drop, Changing Molar Flow, and Formation of Steam in the Accurate Modeling of a Multi-Tubular Fischer–Tropsch Reactor with Cobalt as Catalyst
On the Role of Radial Dispersion in the Behavior of a Cooled Fixed-Bed Reactor : Numerical Investigation of Fischer–Tropsch Synthesis with a Cobalt-Based Catalyst
Catalytic Behavior and In Situ X-Ray Diffraction of Promoted Iron Catalysts for Fischer-Tropsch Synthesis
Hydrocracking of Model Substances on Pt/H‐ZSM‐5 under an Imitated Fischer‐Tropsch Product Gas Composition
Design and Technoeconomic Analysis of Fischer–Tropsch Fixed‐Bed Synthesis with Cobalt‐Based Catalysts
Improving the Selectivity to Liquefied Petroleum Gas by Combining Fischer‐Tropsch Synthesis with Zeolite Cracking
Enhancing Kerosene Selectivity of Fischer-Tropsch Synthesis by Periodical Pore Drainage Via Hydrogenolysis
On the Role of Radial Dispersion in the Behavior of a Cooled Fixed‐Bed Reactor: Numerical Investigation of Fischer–Tropsch Synthesis with a Cobalt‐Based Catalyst
Design and Technoeconomic Analysis of Fischer–Tropsch Fixed-Bed Synthesis with Cobalt-Based Catalysts
Cobalt Catalyzed Fischer-Tropsch Synthesis with O₂-Containing Syngas
Improving the Selectivity to Liquefied Petroleum Gas by Combining Fischer-Tropsch Synthesis with Zeolite Cracking
Catalytic Behavior and In Situ X‐Ray Diffraction of Promoted Iron Catalysts for Fischer‐Tropsch Synthesis
Significance of Pressure Drop, Changing Molar Flow, and Formation of Steam in the Accurate Modeling of a Multi-Tubular Fischer–Tropsch Reactor with Cobalt as Catalyst
On the Role of Radial Dispersion in the Behavior of a Cooled Fixed-Bed Reactor : Numerical Investigation of Fischer–Tropsch Synthesis with a Cobalt-Based Catalyst