2804-49-1

Usage

Uses

Used in Air Conditioning and Refrigeration Industry:
1-Chloro-1,2,3,3,3-pentafluoroprop-1-ene is used as a refrigerant for its ability to maintain lower temperatures efficiently in air conditioning and refrigeration systems, providing a more environmentally friendly alternative to traditional chlorofluorocarbons.
Used in Industrial Processes:
In various industrial applications, 1-Chloro-1,2,3,3,3-pentafluoroprop-1-ene serves as a solvent, leveraging its chemical properties to facilitate processes that require specific conditions or reactions.
Used in Aerosol Products:
As a propellant in aerosol products, 1-Chloro-1,2,3,3,3-pentafluoroprop-1-ene aids in the dispensing of substances from aerosol cans, offering a more eco-friendly option compared to some traditional propellants.
Despite its utility in these areas, the compound is being phased out due to its contribution to global warming, reflecting a global effort to seek more sustainable and environmentally benign alternatives.

InChI:InChI=1/C3ClF5/c4-2(6)1(5)3(7,8)9/b2-1-

Upstream product

• 812-30-6 1,1,2-trichloro-1,2,3,3,3-pentafluoropropane 
• 116-15-4 perfluoropropylene 

Downstream Products

• 116-15-4 perfluoropropylene 
• 431-31-2 1,1,1,2,3-pentafluoropropane 
• 431-63-0 1,1,1,2,3,3-hexafluoropropane 
• 754-12-1 2,3,3,3-tetrafluoro-propene 
• 421-48-7 1,1,1,2-tetrafluoropropane 
• 5595-10-8 (E)-1,2,3,3,3-pentafluoropropene 
• 5528-43-8 Z-1,2,3,3,3-pentafluoropropene 
• 151771-09-4 1-chloro-2,3,3,3-tetrafluoropropane 

Relevant academic research and scientific papers

HYDROGEN FLUORIDE-HFC-254EB AZEOTROPE AND ITS USES

Described is a process for separating 1,1,1,2-tetrafluoropropane and hydrogen fluoride from a mixture comprising 1,1,1,2-tetrafluoropropane, 1,1,1,2,3-pentafluoropropane and hydrogen fluoride comprising: subjecting said 1,1,1,2-tetrafluoropropane, 1,1,1,2,3-pentafluoropropane and hydrogen fluoride mixture to a distillation step, forming a column distillate composition comprising an azeotropic or near-azeotropic composition of said 1,1,1,2-tetrafluoropropane and hydrogen fluoride, and a bottoms composition of 1,1,1,2,3-pentafluoropropane. The column distillate may optionally be made essentially free of 1,1,1,2,3-pentafluoropropane and the column bottoms composition may optionally be made essentially free of HF. Also described is a process for separating 1,1,1,2-tetrafluoropropane and hydrogen fluoride from a mixture of 1,1,1,2-tetrafluoropropane and hydrogen fluoride. Also described are azeotropic and azeotrope-like compositions comprising 1,1,1,2-tetrafluoropropane and hydrogen fluoride.

PROCESS FOR THE SYNTHESIS AND SEPARATION OF HYDROFLUOROOLEFINS

A process for the synthesis of fluorinated olefins of the formula CF3CF=CHX, wherein X is F or H comprising contacting hexafluoropropene with hydrogen chloride in the vapor phase, in the presence of a catalyst, at a temperature in the range from about 200 °C to about 350 °C, wherein the mole ratio of hydrogen chloride to hexafluoropropene is from about 2:1 to about 4:1, separating the 1-chloro-1,2,3,3,3-pentafluoro-1-propene, 1,1-dichloro-2,3,3,3-tetrafluoro-1-propene and hydrogen fluoride products from unreacted hexafluoropropene, and hydrogen chloride by distillation, hydrogenating either the 1-chloro-1,2,3,3,3-pentafluoro-1-propene, 1,1-dichloro-2,3,3,3-tetrafluoro-1-propene or mixture thereof over a catalyst, and dehydrochlorinating the said hydrogenation product to produce either 1225ye or 1234yf.