Pilot Units for Continuous Supercritical Fluid Reactions
W
Shared by: taw15849
Categories
Tags
supercritical fluids, supercritical fluid, supercritical carbon dioxide, supercritical fluid extraction, carbon dioxide, supercritical co2, high pressure, supercritical water, fluid technologies, supercritical fluid technology, the fluid, chemical engineering, phase equilibria, pharmaceutical technology, pilot plant
-
Stats
- views:
- 3
- posted:
- 2/16/2010
- language:
- English
- pages:
- 1
Document Sample


6
Pilot Units
for Continuous
Supercritical
Fluid Reactions
Standard Design
Max. operating pressure 50–1,000 bar
Max. operating temperature 20– 500°C
Performing a reaction at supercritical conditions enhances the conversion rates and
the space-time yield. Smaller reactors can be used for the same amount of reaction
product.
Advantages
n Improved space-time yield
n High selectivity
n Enhanced conversation rates
n Smaller reactors
n Higher catalytic activity
n Homogeneous reactions because of unlimited solubility of reactants
n Increased catalyst endurance
Features
n Fixed-bed tube reactors, slurry reactors, recirculation reactors, down-flow column
reactors, Berty-type reactors
n Pressure generation for gases and liquids
n Mass flowmeters for gases and liquids
Options
n Data acquisition system
n Process control and batch documentation with programmable logic controller (PLC)
n External recirculation of reaction fluids
Pilot unit built for
Applications reaction engineering
n Hydrogenations n Catalytic reactions research (Germany).
n Polymerizations n Enzymatic reactions This unit is equipped
Synthesis reactions with a Berty-reactor for
n Isomerizations n
450°C max. reaction
Oxidations n Hydrolysis
n temperature.
Pilot unit designed for catalytic high-pressure reactions for a pharmaceutical company (Switzerland).
The two reactors are fixed-bed catalytic reactors which can be operated up-flow, down-flow, in
series or parallel.
Related docs
Get documents about "