Catalytic Dehydrogenation
Linde has developed a new process for selective catalytic dehydrogenation of propane to polymer-grade propylene.
The Linde PDH process offers remarkable economical advantages compared to competing technologies. It's moderate reaction temperature and isothermal operating conditions result in maximum selectivity to propylene.
The reaction section includes three identical gas fired dehydrogenation reactors of the well proven steamreformer type. Two of these reactors operate under dehydrogenation conditions, while the third reactor is regenerated by combustion of the coke deposit on the catalyst with a steam/air mixture. The dehydrogenation product from the reaction section is routed to the separation section, in which polymer grade propylene and as by products a hydrogen-rich tailgas and a (C4+)- fraction are separated by the application of proven technique, like low temperature fractionation and a C3-splitter.
Website Finder
Choose Website... Linde Werk Schalchen (D) Selas-Linde GmbH (D) Linde-KCA-Dresden GmbH (D) Linde Kryotechnik AG (CH) Bertrams Heatec AG (CH) Cryostar SAS (F) Linde CryoPlants Ltd. (GB) Linde Impianti Italia S.p.A. (I) Linde Engineering India Pvt. Ltd. (IND) Cryo AB (S) Linde Process Plants, Inc. (USA) Selas Fluid Proc.Corp. (USA)
Product Finder
Choose Product...
--------------------
Chemical and
Petrochemical
Plants
--------------------
Ethylene Technology
--------------------
Pyrocrack Furnace
Technology
--------------------
Ultrarec Recovery
of Olefins
--------------------
Recovery of Olefins
in Gas Feedstock
Cracking Plants
--------------------
Recovery of Olefins
in Liquid Feedstock
Cracking Plants
--------------------
Acetylene Recovery
--------------------
Catalytic
Dehydrogenation
--------------------
Polyolefin Plants
--------------------
Distillation for
Aromatics Recovery
--------------------
Hydrogen and
Synthesis Gas
Plants
--------------------
Contact
--------------------
Inquiry
--------------------
Publications
--------------------
Gas Products
--------------------
Hydrogen
--------------------
Carbon Monoxide
--------------------
Synthesis Gas
--------------------
Ammonia
--------------------
Methanol
--------------------
Gas Generation
--------------------
Steam Reforming
--------------------
Partial Oxidation
--------------------
Tandem Reforming
--------------------
CO Shift Conversion
--------------------
Isothermal Reactor
--------------------
Gas Processing
--------------------
H2/CO Separation
--------------------
H2/HC Separation
--------------------
Acid Gas Removal
--------------------
Rectisol Wash
--------------------
Liquid Nitrogen
Wash
--------------------
Pressure Swing
Adsorption
--------------------
Gas Processing
Plants
--------------------
Partial
Condensation
Process and Liquid
Methane Wash
--------------------
Separation of
Hydrogen and LPG
from Refinery Fuel
Gas
--------------------
Rare Gas Processing
--------------------
Acid Gas Removal
and Sulfur Recovery
--------------------
Purge Gas Plants
--------------------
Purification &
Liquefaction of CO2
--------------------
Natural Gas
Treatment
--------------------
Condensate and LPG
Recovery
--------------------
Linear Alpha
Olefins
--------------------
Air Separation
Plants
--------------------
Air Separation
History
--------------------
Tonnage Air
Separation Plants
--------------------
Packaged Air
Separation Plants
--------------------
Pressure Swing
Adsorption Plants
--------------------
Inquiry Form
--------------------
Cryogenics and
Space Cryogenics
--------------------
Tanks for liquids,
liquid gases and
bulk material
--------------------
Biotechnological
Plants
--------------------
Process and
Refinery Furnaces
--------------------
Pyrolysis Furnaces
for Ethylene
Production
--------------------
Steam Reformers for
H2-Production
--------------------
Steam Reformers for
Syngas Production
--------------------
Special Furnaces
--------------------
Environmental
Protection Plants
--------------------