23153-23-3

Basic information

• Product Name: PROPANE,1,1,1,3,3-PENTACHLORO-
• Synonyms: PROPANE,1,1,1,3,3-PENTACHLORO-;1H,2H,2H-Perchloropropane;240fa, 1,1,1,3,3-Pentachloropropane
• CAS NO: 23153-23-3
• Molecular Formula: C₃H₃Cl₅
• Molecular Weight: 216.32
• Mol File: 23153-23-3.mol
• Article Data: 20

Chemical Properties

• Boiling Point: 191.3°Cat760mmHg
• Flash Point: 69.2°C
• Appearance: /
• Density: 1.597g/cm³
• Vapor Pressure: 0.72mmHg at 25°C
• Refractive Index: 1.504
• CAS DataBase Reference: PROPANE,1,1,1,3,3-PENTACHLORO-(CAS DataBase Reference)
• NIST Chemistry Reference: PROPANE,1,1,1,3,3-PENTACHLORO-(23153-23-3)
• EPA Substance Registry System: PROPANE,1,1,1,3,3-PENTACHLORO-(23153-23-3)

Safety Data

• Hazardous Substances Data: 23153-23-3(Hazardous Substances Data)

Usage

General Description

Propane, 1,1,1,3,3-pentachloro- is a synthetic chemical compound with the molecular formula C5H12Cl5. It is a member of the chlorinated hydrocarbon family and is used primarily as a pesticide. This chemical is highly toxic and is known to be harmful to the environment, particularly to aquatic organisms. It is a colorless, odorless liquid with a high potential for bioaccumulation, and it is considered a significant environmental pollutant. Exposure to propane, 1,1,1,3,3-pentachloro- can lead to a range of health issues, including respiratory problems, skin irritation, and potentially more serious health impacts with prolonged or high-level exposure. Due to its toxicity and potential environmental harm, the use and production of this chemical are heavily regulated in many countries.

InChI:InChI=1/C3H3Cl5/c4-2(5)1-3(6,7)8/h2H,1H2

Upstream product

• 7789-89-1 1,1,1-trichloropropane 
• 1070-78-6 1,1,1,3-tetrachloropropane 
• 56-23-5 tetrachloromethane 
• 53220-05-6 1,3,3,3-tetrachloro-propyl 
• 7791-25-5 sulfuryl dichloride 
• 2088-35-9 1,1-dichlorocyclopropane 
• 94-36-0 dibenzoyl peroxide 
• 7782-50-5 chlorine 
• 75-01-4 chloroethylene 

Downstream Products

• 5406-70-2 1,1,1,2,3,3-hexachloropropane 
• 3607-78-1 1,1,1,3,3,3-hexachloropropane 
• 431-51-6 2,3,3-trichloro-1,1,1-trifluoropropane 
• 460-69-5 1,1-dichloro-3,3,3-trifluoropropane 
• 431-52-7 1,1,2-trichloro-3,3,3-trifluoropropene 
• 149329-29-3 1-chloro-1,3,3,3-tetrafluoropropane 
• 306-83-2 1,1,1-trifluoro-2,2-dichloroethane 
• 338-75-0 2,3-dichloro-1,1,1-trifluoropropane 
• 431-27-6 1,2-dichloro-3,3,3-trifluoropropene 
• 2730-43-0 1-chloro-3,3,3-trifluoropropene 
• 1645-83-6 1,3,3,3-tetrafluoro-propene 
• 460-73-1 1,1,1,3,3-Pentafluoropropane 
• 60027-77-2 1,1,3,3,5,5-hexachloro-pentane 
• 102687-65-0 trans-1-chloro-3,3,3-trifluoropropene 

Relevant articles and documents

Process for coproducing trans - HFO-1234 ze and cis - HFO-1234 ze

The invention relates to a vinyl chloride (CH). 2 ＝ CHCl) And carbon tetrachloride (CCl)4 For the production of trans HFO-1234 ze and cis HFO-1234 ze from the starting materials. Vinyl chloride (CH)2 ＝ CHCl) And carbon tetrachloride (CCl)4 In a catalytic system composed of a chlorinated metal salt/molecular sieve catalyst and N and N - dimethylethylamine, HCC-240 fa is synthesized by telomerization and is subjected to a fluorination reaction in HCC reactor, 240 is alumina in a second reactor, and contains θ-Al and 3rd. 2 O3 Sum α-Al2 O3 The trans - HFO-1234 ze is converted into cis - HFO-1234 ze under the action of the isomerization catalyst of the mixed crystal phase, and finally, trans HFO-1234 ze is obtained through multistage separation tower and extraction separation. Cis HFO-1234 ze product.

Preparation method of 2,3,3,3-tetrafluoropropene

The invention discloses a preparation method of 2,3,3,3-tetrafluoropropene. The preparation method comprises the steps: performing telomerization on chloroethylene and CCl4 so as to produce 1,1,1,3,3-pentachloropropane, then performing dehydrochlorination so as to generate 1,1,3,3-tetrachloro-1-propylene, performing exchange of fluorine and chlorine and dehydrochlorination so as to prepare 3,3,3-trifluoro-1-chloropropene, then performing an isomerization reaction so as to obtain 3,3,3-trifluoro-2-chloropropene, performing a liquid phase fluorination reaction so as to synthesize 1,1,1,2-tetrafluoro-2-chloropropane, and finally performing dehydrochlorination so as to obtain 2,3,3,3-tetrafluoropropene. The raw materials have low price, and are easy to obtain, so that the raw material cost inthe production process of 2,3,3,3-tetrafluoropropene is reduced; an industrial chain is formed in the reaction process, and highly-economic values are provided through purification of the intermediateproducts; the reaction conditions are mild, the equipment has simple operation, the raw material conversion rate and product selectivity are high at the reaction stages, and by-products are few, so that a large industrial application prospect is achieved.

METHOD FOR PRODUCING FLUOROCARBON USING HYDROHALOFLUOROPROPENE

PROBLEM TO BE SOLVED: To provide a method for selectively producing fluorocarbon by efficiently isomerizing a hydrofluoropropene isomer (isomer 1) under the reduction of catalytic performance to produce a corresponding hydrohalofluoropropene isomer (isomer 2) and using the same. SOLUTION: Provided is a method for producing 3,3,3-trifluoropropene by contacting a 1-halogeno-3,3,3-trifluoropropene isomer with a moisture concentration of 100 ppm or lower (isomer 1) in a vapor phase so as to be isomerized to produce a corresponding 1-halogeno-3,3,3-trifluoropropene isomer (isomer 2), and subjecting the 1-halogeno-3,3,3-trifluoropropene isomer (isomer 2) to dehalogenation. SELECTED DRAWING: Figure 1 COPYRIGHT: (C)2018,JPOandINPIT