209 results on '"Freund, Hannsjörg"'
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2. Reaction Kinetic Modeling of the COx Methanation over a Broad Range of Operation Conditions on an Impregnated Ni/Al2O3 Catalyst
3. Die Fachsektion Chemische Reaktionstechnik von DECHEMA und VDI hat sich neu formiert
4. Periodic Open Cellular Structures in Chemical Engineering: Application in Catalysis and Separation Processes
5. Reaction Kinetic Modeling of the COx Methanation over a Broad Range of Operation Conditions on an Impregnated Ni/Al2O3 Catalyst.
6. Process intensification in mass-transfer limited catalytic reactors through anisotropic periodic open cellular structures
7. Detailed numerical investigations of the in operando adjustable flow field in a diamond unit cell-based interpenetrating periodic open cellular structure (interPOCS)
8. Identification of Mass Transfer Limitations by Kinetic Modeling of a Technical-Scale Trickle Bed Reactor for the Hydrogenation of Viscous Aromatics.
9. Kinetic modeling of dynamically operated heterogeneously catalyzed reactions: Microkinetic model reduction and semi-mechanistic approach on the example of the CO2 methanation
10. „Digitalisierung der Reaktionstechnik“: ein Themenfeld mit vielen Facetten!
11. Tap Reactor for Temporally and Spatially Resolved Analysis of the CO 2 Methanation Reaction
12. Complementary mass transport investigations in open-cell foams: Full-field CFD simulation with random-walk microscopic particle tracking and PFG NMR displacement measurements
13. Influence of Resolution of Rasterized Geometries on Porosity and Specific Surface Area Exemplified for Model Geometries of Porous Media
14. Sugar acid production on gold nanoparticles in slurry reactor: Kinetics, solubility and modelling
15. Quo vadis multiscale modeling in reaction engineering? – A perspective
16. Tap Reactor for Temporally and Spatially Resolved Analysis of the CO2 Methanation Reaction.
17. Wie verändert sich die Reaktions‐ und Reaktortechnik durch die Elektrifizierung chemischer Prozesse?
18. Conceptual study on the intensification of gas–liquid mass transfer in trickle bed reactors by the application of strut-based and novel sheet-based periodic open cellular structures (POCS).
19. Development and evaluation of a new particle tracking solver for hydrodynamic and mass transport characterization of porous media – A case study on periodic open cellular structures
20. Detailed investigation of liquid distribution and holdup in periodic open cellular structures using computed tomography
21. „Circular Economy” – ein neues und zugleich altes Arbeitsgebiet der Reaktionstechnik
22. Systematic Experimental Investigations and Modeling of the Heat Transfer in Additively Manufactured Periodic Open Cellular Structures with Diamond Unit Cell
23. Intensification of load flexible fixed bed reactors by optimal design of staged reactor setups
24. Kinetic modelling of reactions for the synthesis of 2-methyl-5-ethyl pyridine
25. Model-based development of optimal reaction concepts for plant wide process intensification
26. Optimal Reactor Design for the Hydroformylation of Long Chain Alkenes in Biphasic Liquid Systems
27. Periodic open cellular structures (POCS) as catalyst support for intensified heat transport in the partial oxidation of methanol to formaldehyde.
28. Packed Periodic Open Cellular Structures – an Option for the Intensification of Non-Adiabatic Catalytic Processes
29. On the optimal design of load flexible fixed bed reactors: Integration of dynamics into the design problem
30. Influence of statistical activity variations in diluted catalyst beds on the thermal reactor behavior: Derivation of an a priori criterion
31. A new heat transfer correlation suited for the design of fixed-bed reactors via numerical optimization
32. Identification of Reaction Pathways and Kinetic Modeling of Olefin Interconversion over an H-ZSM-5 Catalyst
33. Technische Chemie
34. Multi-objective reactor design under uncertainty: A decomposition approach based on cubature rules
35. Additive manufacturing of interpenetrating periodic open cellular structures (interPOCS) with in operando adjustable flow characteristics
36. Comparative evaluation of heat transfer correlations with different fluid property considerations for fixed-bed reactor modeling
37. Optimization of the direct synthesis of dimethyl ether from CO2 rich synthesis gas: closing the loop between experimental investigations and model-based reactor design
38. Process intensification by model-based design of tailor-made reactors
39. Detailed Simulation of Transport Processes in Reacting Multi-Species Flows Through Complex Geometries by Means of Lattice Boltzmann Methods
40. A multimodular pseudoheterogeneous model framework for optimal design of catalytic reactors exemplified by methanol synthesis
41. Dynamic Carbon Dioxide Methanation in a Wall-Cooled Fixed Bed Reactor: Comparative Evaluation of Reactor Models
42. Detailed geometrical analysis of statistical activity variations in diluted catalyst beds
43. Systematic model‐based design of tolerant chemical reactors
44. Kinetic Modeling of the Partial Oxidation of Propylene to Acrolein: A Systematic Procedure for Parameter Estimation Based on Non-isothermal Data
45. Efficient calculation of constraint back-offs for optimization under uncertainty: A case study on maleic anhydride synthesis
46. Optimization of the direct synthesis of dimethyl ether from CO2 rich synthesis gas: closing the loop between experimental investigations and model-based reactor design.
47. Tailored catalyst pellet specification for improved fixed-bed transport characteristics: A shortcut method for the model-based reactor design
48. Optimization under uncertainty in chemical engineering: Comparative evaluation of unscented transformation methods and cubature rules
49. Modellbasierter Entwurf energieeffizienter Reaktoren
50. Periodic open cellular structures (POCS) for intensification of multiphase reactors: Liquid holdup and two-phase pressure drop
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