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Model 1150 Dual Reactor - Thermo Fisher Scientific

Model 1150 Dual Reactor - Thermo Fisher Scientific

Reliably remove carbon monoxide and hydrocarbons from filtered ambient air using two reactors in series, providing efficient catalytic conversion of CO and HC to CO2 and H2O at ∽350C with the Thermo Scientific Model 1150 Dual Reactor.

Thermo-catalytic reforming: Sustainable efficient energy .

Thermo-catalytic reforming: Sustainable efficient energy .

© Fraunhofer UMSICHT Folie 3 A flexible, integrated waste-to-energy solution . Syngas Biochar Oil + . or animal grease, glycerol, other fats, oils and waxes

Method and apparatus for decoupled thermo-catalytic .

Method and apparatus for decoupled thermo-catalytic .

@article{osti_1175825, title = {Method and apparatus for decoupled thermo-catalytic pollution control}, author = {Tabatabaie-Raissi, Ali and Muradov, Nazim Z. and Martin, Eric}, abstractNote = {A new method for design and scale-up of thermocatalytic processes is disclosed. The method is based on optimizing process energetics by decoupling of the process energetics from the DRE for target .

Thermo-Catalytic Methane Decomposition: A Review of State .

Thermo-Catalytic Methane Decomposition: A Review of State .

Current research work on thermo-catalytic methane decomposition has concentrated on promoting the catalytic activity and stability for simultaneous production of pure hydrogen and elemental carbon. The carbon is generated as nanotubes, which are important for the use of this material in numerous new technologies. . Good reactor design allowed .

ML7038F Multi-Point Catalyst Bed Reactor Thermocouples

ML7038F Multi-Point Catalyst Bed Reactor Thermocouples

ML7038F Multi-Point Catalyst Bed Reactor Thermocouples CONAX PG Single sensor feedthrough . More info Calibration Bath LCA50, Range +30°C to +225°C . More info 5331A Universal temperature transmitter . Thermo Electra b.v. Weteringweg 10 .

DEG Thermo-Plate Reactor | DEG Engineering | a Paul .

DEG Thermo-Plate Reactor | DEG Engineering | a Paul .

DEG thermo-plate reactors are a new type of catalytic reactor with interior cooling, whereby thermo-plates are used as heat exchangers. This kind of heat exchanger has already been manufactured several hundred times and has proven itself in particular in situations in .

The Bionic Group Records: TCDP Thermo Catalytic .

The Bionic Group Records: TCDP Thermo Catalytic .

Jan 19, 2011 · TCDP Thermo Catalytic Depolymerization Its been a long time since the last 2 posts, . Now somebody might think: all you have to do is build a small reactor that allows you to mix your garden waste with zeolite, heat up the mixture to the right temperature and voila, the next day you have diesel for your car and biochar for next years .

Thermo-catalytic degradation of different plastics to drop .

Thermo-catalytic degradation of different plastics to drop .

Thermal and catalytic pyrolysis of individual plastics such as polypropylene (PP), low-density polyethylene (LDPE), high-density polyethylene (HDPE), and mixture of all three plastics (PP + LDPE + HDPE) were carried out in the presence of calcium bentonite as catalyst in a batch reactor to obtain suitable liquid fuel. The dependencies of process temperature, effect of catalyst, feed .

thermo catalytic reactor, thermo catalytic reactor .

thermo catalytic reactor, thermo catalytic reactor .

403 thermo catalytic reactor products are offered for sale by suppliers on, of which reactors accounts for 1%. A wide variety of thermo catalytic reactor options are available to you, such as manufacturing plant, energy & mining, and building material shops.

Thermo Catalytic decomposition of methane on Ni/SiO2 .

Thermo Catalytic decomposition of methane on Ni/SiO2 .

Thermo-catalytic decomposition of methane is a promising approach to produce COx-free hydrogen and carbon nanotubes at a relatively low cost through a single-step process. Ni catalysts supported on silica as textural promoter . catalyst preparation method, reaction temperature and type of support material. It was observed that the catalytic .

Thermo-Photo Catalysis for Methanol Synthesis from Syngas

Thermo-Photo Catalysis for Methanol Synthesis from Syngas

Reaction configuration . Figure S1. Thermo-photo catalytic reactor . To avoid possible leakage: (1) The reactor is maintained at doubled reaction temperature (500 oC) and pressure (5Mpa) before use. (2) The reactor top (where quartz window locates) is cooled by circulating water to prevent the overheating of the sealing PTFE gasket.

Method and apparatus for decoupled thermo-catalytic .

Method and apparatus for decoupled thermo-catalytic .

@article{osti_1175825, title = {Method and apparatus for decoupled thermo-catalytic pollution control}, author = {Tabatabaie-Raissi, Ali and Muradov, Nazim Z. and Martin, Eric}, abstractNote = {A new method for design and scale-up of thermocatalytic processes is disclosed. The method is based on optimizing process energetics by decoupling of the process energetics from the DRE for target .

(95d) Modeling Catalyst Deactivation in a Packed Bed .

(95d) Modeling Catalyst Deactivation in a Packed Bed .

catalyst deactivation in a packed bed reactor for thermo-catalytic hydrogenation of CO 2. Duo Sun and David Simakov Department of Chemical Engineering, University of Waterloo, Waterloo, ON N2L 3G1, Canada. Converting CO 2 into synthetic fuels and chemicals is an attractive route to reduce CO 2 emissions and, at the same time, fossil fuels .

How to Measure the Reaction Performance of Heterogeneous .

How to Measure the Reaction Performance of Heterogeneous .

Catalyst stabilities are typically evaluated by plotting the activity and the product distribution as functions of time-on-stream (TOS) in PFRs and the number of times the catalyst is exposed to the reaction conditions in batch reactors. We note that evaluating catalyst stability at conversion of the reactant should be avoided because the .

A new algorithm to convert a normal antibody into the .

A new algorithm to convert a normal antibody into the .

Over thousands of monoclonal antibodies (mAbs) have been produced so far, and it would be valuable if these mAbs could be directly converted into catalytic antibodies. We have designed a system to realize the above concept by deleting Pro95, a highly conserved residue in CDR-3 of the antibody light chain. The deletion of Pro95 is a key contributor to catalytic function of the light chain.

GlycoLink™ Coupling Catalyst - Thermo Fisher Scientific

GlycoLink™ Coupling Catalyst - Thermo Fisher Scientific

The Thermo Scientific GlycoLink Coupling Catalyst decreases reaction times and increases aldehyde-hydrazide coupling efficiency, resulting in greater than 90% coupling of glycoproteins in 4 hours.Features of the GlycoLink Coupling Catalyst: Optimizedcatalyzes aldehyde-hydrazide and aldehyde-alkoxyam

A Mini-Review on Hydrogen-Rich Syngas Production by Thermo .

A Mini-Review on Hydrogen-Rich Syngas Production by Thermo .

The thermo-catalytic and biochemical conversion of biomass to hydrogen-rich syngas has been widely reported with less emphasis on the environmental implications of the processes. This mini-review presents an overview of different thermo-catalytic route of converting biomass to hydrogen-rich syngas as well as their environmental impact investigated using life cycle assessment methodology.

Photo–thermo Catalytic Oxidation over a TiO2‐WO3‐Supported .

Photo–thermo Catalytic Oxidation over a TiO2‐WO3‐Supported .

Photo–thermo catalytic oxidation of propane (C 3 H 8) on Pt/TiO 2 ‐WO 3 catalyst proceeds with excellent activity at high O 2 /C 3 H 8 ratios and low temperatures. An investigation of the apparent activation energy and reaction orders (relative to thermal catalysis) reveals that oxygen poisoning of the supported Pt catalyst is mitigated and .

PRESENTATION OF REACTOR TYPES FOR THERMO- .

PRESENTATION OF REACTOR TYPES FOR THERMO- .

The selection of reactor type(s) appropriate for the solid raw material to be processed is key in the process as it affects directly both the quality and quantity of the product formed. 2.1. Batch/semi-batch reactors Many studies on thermo-catalytic plastics cracking in mixed (not in each case) batch

(PDF) THERMO-CATALYTIC REFORMING (TCR ® ): A PLATFORM .

(PDF) THERMO-CATALYTIC REFORMING (TCR ® ): A PLATFORM .

Thermo-Catalytic Reforming TCR®: A Platform Technology to use residues and to produce sustainable and storable energy carriers. . The TCR® reactor is an intermediate pyrolysis screw reactor .

DEG Thermo-Plate Reactor | DEG Engineering | a Paul .

DEG Thermo-Plate Reactor | DEG Engineering | a Paul .

DEG thermo-plate reactors are a new type of catalytic reactor with interior cooling, whereby thermo-plates are used as heat exchangers. This kind of heat exchanger has already been manufactured several hundred times and has proven itself in particular in situations in .

Thermo-Catalytic Methane Decomposition: A Review of State .

Thermo-Catalytic Methane Decomposition: A Review of State .

Current research work on thermo-catalytic methane decomposition has concentrated on promoting the catalytic activity and stability for simultaneous production of pure hydrogen and elemental carbon. The carbon is generated as nanotubes, which are important for the use of this material in numerous new technologies. . Good reactor design allowed .

Thermo-Catalytic Reforming of Woody Biomass | Energy & Fuels

Thermo-Catalytic Reforming of Woody Biomass | Energy & Fuels

Integrated thermo-catalytic reforming of residual sugarcane bagasse in a laboratory scale reactor. Fuel Processing Technology 2018, 171, 277-286. DOI: 10.1016/j.fuproc.2017.11.020.

LR43-e HAAKE MiniLab Compounder and Reactor

LR43-e HAAKE MiniLab Compounder and Reactor

Compounder and Reactor Matthias Jährling, Dr. A. Frendel, Thermo Fisher Scientific, Process Instruments, Karlsruhe, Germany. G. Isaakides Abstract The use of a conical twin screw extru-der with backflow channel combines aspects of mixing and extrusion in a batch process. Tests and results of the new HAAKE MiniLab micro compounder are discussed .

The Bionic Group Records: TCDP Thermo Catalytic .

The Bionic Group Records: TCDP Thermo Catalytic .

Jan 19, 2011 · TCDP Thermo Catalytic Depolymerization Its been a long time since the last 2 posts, . Now somebody might think: all you have to do is build a small reactor that allows you to mix your garden waste with zeolite, heat up the mixture to the right temperature and voila, the next day you have diesel for your car and biochar for next years .

Supplementary material for Thermo-catalytic pyrolysis of .

Supplementary material for Thermo-catalytic pyrolysis of .

Thermo-catalytic pyrolysis is considered as a promising process for the chemical recycling of waste polymeric materials aiming at converting them into their original monomers or other valuable chem.

ML7038F Multi-Point Catalyst Bed Reactor Thermocouples

ML7038F Multi-Point Catalyst Bed Reactor Thermocouples

ML7038F Multi-Point Catalyst Bed Reactor Thermocouples CONAX PG Single sensor feedthrough . More info Calibration Bath LCA50, Range +30°C to +225°C . More info 5331A Universal temperature transmitter . Thermo Electra b.v. Weteringweg 10 2641 KM .

Regulating the coordination structure of single-atom Fe-N .

Regulating the coordination structure of single-atom Fe-N .

Sep 19, 2019 · Catalytic test. The benzene oxidation reaction was carried out in a 50.0 mL glass reactor. 50 mg catalyst, 0.4 mL benzene, 6 mL H 2 O 2 (30 wt%), and 3.0 mL CH 3 CN was added. After reaction at 30 .

Removal of elemental mercury by TiO₂doped with WO₃ and .

Removal of elemental mercury by TiO₂doped with WO₃ and .

The catalytic removal of Hg(0) was investigated to ascertain whether the catalysts could simultaneously possess both thermo- and photo-catalytic reactivity. The immobilized V2O5/TiO2 and WO3/TiO2 catalysts were synthesized by sol-gel method and then coated on the surface of glass beads for catalytic removal of Hg(0).

An experimental study on thermo-catalytic pyrolysis of .

An experimental study on thermo-catalytic pyrolysis of .

A bench scale, two-stage, thermo-catalytic reactor equipped with a continuous feeding system was used to pyrolyse pure and waste plastics. Experiments using five zeolitic and clay-based catalysts of different forms (pellet and powders) and different plastic feedstocks - HDPE, HDPE w1aste and mixed plastic waste (MPW) were compared to the control experiments - pyrolysis without catalyst.