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.
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... |
快速链接
Tel.: +86 769 8185 5667
Mob.: +86 134 1596 1411
Fax: +86 769 8185 5569
E-mail: Sarah@essenton.com
WhatsApp: +86 134 1596 1411
WeChat: +86 134 1596 1411
地址: 广东省东莞市茶山镇南塘路7号
