Catalyst selection plus water or alcohol phase splitting raises bromochloromethane yield and enables cleaner, simpler separation.
Metal oxide additives stabilize HFC-23 recycling catalysts and cut CFC-12 by-product formation while preserving HCFC-22 selectivity.
A distillable 1-halo-7-methyltricosane intermediate enables scalable, high-yield 17-methylalkane synthesis without chromatography.
Metal fluoride fluorination of halogenated ethylenes improves fluoroethylene yield while enabling selective HFO-1132 and HFO-1123 production.
A low-HF liquid-phase process limits overfluorinated coproducts, reducing purification complexity, corrosion risk, and HF usage.
Segmented gas phase fluorination with a chromium catalyst produces HFO-1234yf, resolving the trade-off between production efficiency and cost-effectiveness.
UV-driven photo-bromination with NBS mediator overcomes bromine evaporation and agent instability, achieving 73.9% yield.
An unstirred reactor conducts uncatalyzed liquid phase fluorination to achieve high conversion rates while suppressing oligomer formation.
Germanium tetrafluoride enables chlorine-fluorine exchange on chlorocarbons to produce high-purity chlorofluorocarbon compounds.
A vapor-phase catalytic fluorination process using chromia, alumina, and carbon to produce 1,1-difluoroethane with high selectivity.
Nitrogen trifluoride reactivates spent metal oxide fluorination catalysts without generating water, preventing equipment corrosion and extending useful life.
Vapor-phase disproportionation of HCFO-1233zd over chromium catalysts yields HFO-1234ze without generating corrosive hydrofluoric acid.
A two-step fluorination process converts chloropropenes into hydrofluoroolefins using liquid and gas phase reactions.
Buffered neutralization with sulfite salts prevents dehydrochlorination of 1-chloro-3,3,3-trifluoropropene, reducing trifluoropropyne formation.
Limiting chromium VI prevents chromia crystallization, maintaining catalyst stability during hydrocarbon fluorination.
Directly fluorinating trichloromethylbenzal chlorides with hydrogen fluoride eliminates halogen transfer catalysts, reducing process complexity and costs.
Anhydrous hydrogen fluoride fluorinates pentachloropropane without a catalyst to produce monofluorinated products.
A vapor-phase fluorination process converts halogenated benzenes to monofluorobenzene using anhydrous hydrogen fluoride and a chromium-based catalyst.
SiC microreactors produce HCFC-123 via catalytic fluorination, eliminating energy-intensive distillation.
Fluorinated chromium oxide catalyzes the reaction between 2-chloro-3,3,3-trifluoropropene and hydrogen fluoride to produce HFC-1234yf.
Inorganic base fluorides replace expensive complex reagents to lower production costs for semiconductor dielectric materials.
Reduced pressure synthesis eliminates prolonged distillation, cutting reaction time to one-tenth while minimizing radiation exposure.
Flash-distillation separates products while recycling catalysts to enable continuous haloalkane production.
A gas-phase fluorination process using a chromium or nickel catalyst to convert 2-chloro-3,3,3-trifluoro-1-propene with hydrofluoric acid.
Preheating 1-chloroheptafluorocyclopentene feedstock before fluorination with alkali metal fluoride.
An azeotropic composition comprising hydrochloric acid and trifluoropropyne facilitates distillation separation.
An azeotropic composition of hydrogen fluoride and 2-chloro-3,3,3-trifluoropropene enables efficient distillation-based separation.
A two-step gas phase synthesis method converts 1,1,2,3-tetrachloropropene into HFO-1234yf using sequential fluorination over chromium oxide catalysts.