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Showing 1 to 20 of 47 for “"Fixed Bed Reactor"”.

  1. A CFD Model for a Fixed Bed Reactor for Fischer Tropsch Reaction using Ansys

    … greenhouse gases minimum. Among various types of reactors used for commercial FT, fixed bed tubular reactors are among the most common type of reactor. However, there is a big challenge faced by these tubular reactors. FT is a highly exothermic process and therefore, heat removal in these reactors …

    cape-town Repository record for A CFD Model for a Fixed Bed Reactor for Fischer Tropsch Reaction using Ansys (opens in a new tab)

  2. Dimerization of naphtha-range Fischer-Tropsch olefins into diesel-range products over zeolite H-ZSM-5 and amorphous silica-alumina

    … was carried out in a tubular, continuous flow fixed-bed reactor, in the liquid phase, over zeolite H-ZSM-5 and an amorphous silica-alumina (ASA) catalyst. Both catalysts were in the form of extrudates.

    cape-town Repository record for Dimerization of naphtha-range Fischer-Tropsch olefins into diesel-range products over zeolite H-ZSM-5 and amorphous silica-alumina (opens in a new tab)

  3. ΜΕΛΕΤΗ ΤΗΣ ΔΙΑΣΠΑΣΕΩΣ ΤΗΣ ΠΡΟΠΑΝΟΛΗΣ-2 ΣΕ ΑΠΛΟΥΣ ΚΑΙ ΜΕΙΚΤΟΥΣ ΚΑΤΑΛΥΤΕΣ ΕΠΙ ΦΟΡΕΟΣ SILICA

    … WERE DETERMINED AT VARIOUS TEMPERATURES IN A FIXED BED REACTOR WORKING UNDER ATMOSPHERIC PRESSURE. (SHORTENED)

    greece Repository record for ΜΕΛΕΤΗ ΤΗΣ ΔΙΑΣΠΑΣΕΩΣ ΤΗΣ ΠΡΟΠΑΝΟΛΗΣ-2 ΣΕ ΑΠΛΟΥΣ ΚΑΙ ΜΕΙΚΤΟΥΣ ΚΑΤΑΛΥΤΕΣ ΕΠΙ ΦΟΡΕΟΣ SILICA (opens in a new tab)

  4. Reaction of meta-diisopropylbenzene on acid molecular sieves and synthesis of zeolites by a vapor phase transport method

    … at temperatures around 463 K in a flow-type fixed-bed reactor. A small amount of cracking is observed. The main reactions of meta-diisopropylbenzene are isomerization and alkylation. This alkylation is proposed as a new test reaction to characterize the effective size of the voids in larger …

    vt Repository record for Reaction of meta-diisopropylbenzene on acid molecular sieves and synthesis of zeolites by a vapor phase transport method (opens in a new tab)

  5. Design and testing of an integrated catalytic membrane reactor for deoxygenating water using hydrogen for down-hole injection and process applications.

    … They were characterised and tested in membrane reactors by feeding hydrogen saturated water under varying operating conditions and the results compared to that of a fixed-bed reactor. The catalytic activities of the different membranes resulted in different deoxygenating efficiencies. The 6000nm …

    rgu Repository record for Design and testing of an integrated catalytic membrane reactor for deoxygenating water using hydrogen for down-hole injection and process applications. (opens in a new tab)

  6. Heterogeneous catalysis in the different reactor types on the examples of ethyl benzene to styrene, methane dehydroaromatization and propylene carbonate, methanol transesterification

    … above mentioned projects. Different types of reactors for heterogeneous catalysis were applied in this work – fixed and fluidized bed rectors as well as a riser reactor. Many parameters as e.g. contact times, temperature control, catalyst regeneration procedure etc. can be varied and adjusted …

    aachen Repository record for Heterogeneous catalysis in the different reactor types on the examples of ethyl benzene to styrene, methane dehydroaromatization and propylene carbonate, methanol transesterification (opens in a new tab)

  7. Zur Mikro- und Makrokinetik mehrphasiger heterogen-katalysierter Reaktionssysteme : Untersuchungen am Modellsystem der Ni-katalysierten Hydrierung von 1-Octen

    … a commercially Ni-catalyst in a vibrating batch reactor was chosen as the model system. In such a system each mass transfer resistance can be defined stepwise and excluded by the systematical variation of the reaction condition (concentration of catalyst and octene, particle size). The effective …

    aachen Repository record for Zur Mikro- und Makrokinetik mehrphasiger heterogen-katalysierter Reaktionssysteme : Untersuchungen am Modellsystem der Ni-katalysierten Hydrierung von 1-Octen (opens in a new tab)

  8. Investigation of the activity and selectivity of the MoO3/AI2O3 catalyst and the structural investigation using in-situ raman

    … catalysts are activated at 550°C under N2 in a fixed bed reactor. The loading of the prepared catalysts was below and above monolayer capacity. It was observed that up to a loading 0.3 g Mo03 per g Ab03 the initial conversion increases more than proportional to the Mo03- loading. The catalysts …

    cape-town Repository record for Investigation of the activity and selectivity of the MoO3/AI2O3 catalyst and the structural investigation using in-situ raman (opens in a new tab)

  9. Studies of Carbon Dioxide Methanation and Related Phenomena in Porous Catalysts

    … pressures using a gradientless, spinning-basket reactor operated in batch mode and in a laboratory-scale, continuous fixed-bed reactor. Langmuir-Hinshelwood kinetic models were developed to represent the observed kinetics in each reactor: these models were then compared. For the batch reactor, a …

    cambridge Repository record for Studies of Carbon Dioxide Methanation and Related Phenomena in Porous Catalysts (opens in a new tab)

  10. Structure sensitivity of H2/D2 Isotopic Exchange on Pt/Al2O3 catalysts

    … Experiments were carried out in a quartz tubular fixed bed reactor coupled with a Mass Spectrometer to analyze the product gas by carrying out both, an integral analysis (from 0 to equilibrium conversion) by performing light-off experiments and differential analysis (low conversions) by performing …

    vt Repository record for Structure sensitivity of H2/D2 Isotopic Exchange on Pt/Al2O3 catalysts (opens in a new tab)

  11. Co-pyrolysis of torrefied biomass and coal : product evaluation and reaction modelling

    … and subsequently co-pyrolysis was conducted in a fixed bed reactor at variable mix ratios (25-75 wt.%), temperatures (400-600 °C) and pressures (1-30 bar) to investigate the extent of secondary- and synergistic reactions. The results showed that during co-pyrolysis, condensation and dehydration …

    nwu-za Repository record for Co-pyrolysis of torrefied biomass and coal : product evaluation and reaction modelling (opens in a new tab)

  12. Degradação termocatalítica de misturas de poliolefinas e biomassa

    … polyethylene (HDPE) were carried out in a fixed bed reactor in order to evaluate the influence of pyrolysis temperature (450 to 500 °C) and flow of sweeping gas (N2) (50, 80 and 100 mL min-1 ) on the yields of collected product, residueand gas. The highestyield in collected product was …

    brazil-uerj Repository record for Degradação termocatalítica de misturas de poliolefinas e biomassa (opens in a new tab)

  13. The use of ruthenium Y zeolite catalysts for the selective methanation of carbon monoxide

    … wt.% Ru/Al₂O3. These catalysts were tested in a fixed bed reactor at temperatures between 160°C and 210°C at various space velocities with a feed composition of 1% CO, 20% CO2, 10% H2O, 59% H2 and 10% Ar. The effects of loading, space velocity and reaction temperature on the CO conversion and CO …

    cape-town Repository record for The use of ruthenium Y zeolite catalysts for the selective methanation of carbon monoxide (opens in a new tab)

  14. Development and Application of in Situ/Operando Spectroscopic Techniques for Understanding Active Sites and Surface Intermediate Species in Heterogeneous Catalysis

    … favored acetate production, consistent with fixed-bed reactor studies. Modulation frequency analysis further highlighted the relative speeds of ethoxy decomposition and acetaldehyde transformations. Isotopic kinetic studies on Au/TiO2 provided deeper mechanistic insights, confirming ethoxy …

    ku Repository record for Development and Application of in Situ/Operando Spectroscopic Techniques for Understanding Active Sites and Surface Intermediate Species in Heterogeneous Catalysis (opens in a new tab)

  15. The aerobic, water-assisted selective oxidation of methane over platinum-based catalysts

    … were investigated initially in a gas-phase, fixed bed reactor that is equipped with a steam generator. Initial results from the selective oxidation of methane yielded CO2. Accidentally flooding the reactor resulted in the formation of selective oxidation products such as methanol, …

    cape-town Repository record for The aerobic, water-assisted selective oxidation of methane over platinum-based catalysts (opens in a new tab)

  16. Production of lactic acid by microbial fermentation of hemicellulose sugars

    … the immobilized enzyme (65 g) was packed in a fixed bed reactor with a permeable wall. The lactic acid productivity and yield in the novel bioreactor was higher than that of the control in both 20g/L and 50g/L xylose concentrations. The cells grew much quicker and better in the novel bioreactor …

    nus Repository record for Production of lactic acid by microbial fermentation of hemicellulose sugars (opens in a new tab)

  17. ENGINEERING NI/AL2O3 CATALYSTS BY ATOMIC LAYER DEPOSITION FOR METHANE REFORMING

    … hollow fibers for DRM. The design of a fixed bed reactor and better distribution of gas flow in the reactor could significantly improve the performance of Ni/Al<sub>2</sub>O<sub>3</sub>-HF catalysts by reducing the void space.</p> <p>ALD-prepared ultrathin ZrO<sub>2</sub> or …

    must-thes Repository record for ENGINEERING NI/AL2O3 CATALYSTS BY ATOMIC LAYER DEPOSITION FOR METHANE REFORMING (opens in a new tab)

  18. Flow-through membrane microreactor for intensified heterogeneous catalysis

    … of process intensification several innovative reactor types for heterogeneous catalysis are discussed, including membrane reactors, microreactors and monolithic reactors. A novel reactor concept called flow-through catalytic membrane microchannel reactor contains aspects of each of the three …

    aachen Repository record for Flow-through membrane microreactor for intensified heterogeneous catalysis (opens in a new tab)

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