679-85-6 Usage
Uses
Used in Air Conditioning Systems:
1-Chloro-2,2,3,3-tetrafluoropropane is used as a refrigerant in air conditioning systems for its low global warming potential and high stability, making it an eco-friendly alternative to traditional hydrofluorocarbons.
Used in Commercial Refrigeration:
In commercial refrigeration, 1-Chloro-2,2,3,3-tetrafluoropropane is used as a refrigerant due to its non-toxic and non-flammable properties, ensuring safety and environmental friendliness.
Used in Heat Pump Equipment:
1-Chloro-2,2,3,3-tetrafluoropropane is utilized as a refrigerant in heat pump equipment, taking advantage of its low global warming potential and high chemical and thermal stability for efficient and eco-friendly operation.
Used in Eco-friendly Alternatives:
1-Chloro-2,2,3,3-tetrafluoropropane is used as an eco-friendly alternative to traditional hydrofluorocarbons in various applications, such as air conditioning systems, commercial refrigeration, and heat pump equipment, due to its low global warming potential and high stability. However, it is important to manage its release into the atmosphere to minimize potential harm.
Check Digit Verification of cas no
The CAS Registry Mumber 679-85-6 includes 6 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 3 digits, 6,7 and 9 respectively; the second part has 2 digits, 8 and 5 respectively.
Calculate Digit Verification of CAS Registry Number 679-85:
(5*6)+(4*7)+(3*9)+(2*8)+(1*5)=106
106 % 10 = 6
So 679-85-6 is a valid CAS Registry Number.
InChI:InChI=1/C3H3ClF4/c4-1-3(7,8)2(5)6/h2H,1H2
679-85-6Relevant academic research and scientific papers
Method and device for preparing 2,3,3,3-tetrafluoropropene
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Paragraph 0084; 0088-0090; 0094; 0098-0100, (2019/01/14)
The invention provides a method and a device for preparing 2,3,3,3-tetrafluoropropene. The device for preparing 2,3,3,3-tetrafluoropropene comprises a circulation flow reactor, a first rectifying tower, a first cooling tower, a second rectifying tower and a second cooling tower. The method provided by the invention adopts a continuous loop reactor technology to realize the technology of separatinghydrogen chloride by-products in real time under the reaction conditions, so that the selectivity of the reaction is greatly improved; since the continuous circulation operation of the raw materialsis realized, the total conversion rate of the reaction is very high. 2,3,3,3-tetrafluoropropene obtained by the method is low in cost; the production technology has the advantages of being few in by-products and wastes and suitable for industrial large-scale production.
