Catalyst Reactor

When the feed gas passes through the solid catalyst layer, the particles of the catalyst are stationary, so the thermal conductivity of the bed is not good, and the temperature distribution of the bed may be uneven. Accordingly, the reactor must be designed to ensure good gas-solid contact, and includes a supply / take away the heat, and the reaction can be performed at a suitable temperature. Usually the reaction bed is difficult to maintain isothermal, so most fixed bed reactors are non-isothermal reactors. The non-isothermal reactor is further divided into adiabatic variable temperature type and non-adiabatic temperature change type.

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Description

Metal material tank, for high temperature and high pressure using, acid and alkali resistant design.

This model is designed to test catalyst reaction, performance, conversion, kinetics and reactivation in a continuous flow mode at various temperatures and pressures.

Customized design according to requirements, such as fixed bed with fluidized bed reaction system.

Software remote control system for remote monitoring of reaction processes.

FT Reaction (Fischer Tropsch Synthesis)

WGS Reaction (water-gas shift reaction)

Hydrogen Production

Methanation

Degradation (Short, Long term)

Syngas Production, Treating Proces

Technical Parameters

Volume	5mL~500L
Temp Range	-35 ~ 1200℃
Pressure Range(Depending on the Vessel)	Vacuum ~ 413 bar
Control Panel	Regular
Heating	Electric heater, Furnace
Material	304SS, 316SS, Hastelloy C-276, Inconel, Titanium, Quartze…etc
Contorl Type	Manual operation or fully automatic computer control
Closure Type	Bolt type, VCR type, HP Thread type
Others Components	Mass flow controller, Liquid metering pump, Dry/Wet flow meter, Condenser, Separater...

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