Progressive catalyst activity manages exothermic heat during hydrogenation, eliminating complex cooling systems while maintaining high conversion rates.
Serial reactors with manganese and copper catalysts convert chloropropane intermediates into HFO-1234yf, eliminating stoichiometric hydrogen use.
Copper catalyst converts chlorofluoroalkenes to fluorinated olefins, eliminating ozone depletion potential.
Replacing chromium catalysts with iron-aluminum-zinc systems eliminates carcinogenic risks while maintaining reaction effectiveness.
Maintain specific reactant concentrations during dehydrochlorination to suppress impurity formation and preserve catalyst activity.
Periodic fresh catalyst injection sustains HCFC-244bb production while suppressing HFC-245cb byproduct formation.
A catalyst with a noble metal concentration gradient produces fluoroethane from fluoroethylene and hydrogen gas.
A fixed catalytic bed process for trifluoroethylene production uses dynamic temperature control to maintain catalyst activity.
The integrated process avoids azeotropic separation difficulties by converting 240fa through a 244fa intermediate, enabling flexible production of pure HFO products.
Continuous steam stripping during semi-batch dehydrohalogenation reduces batch cycle time and water content, improving hydrofluoroolefin yield and selectivity.
Mixed metal fluoride catalysts achieve high selectivity and yield in dehydrochlorination by balancing reaction rate with catalyst stability.
A three-step chemical process converts petroleum-derived alkynes into perfluoroalkynes using halogen addition, fluorine gas reaction, and metal dehalogenation.