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1,1-DICHLORO-3,3,3-TRIFLUORO-1-PROPENE is a chemical with a specific purpose. Lookchem provides you with multiple data and supplier information of this chemical.

460-70-8

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460-70-8 Usage

Physical state

Colorless, flammable gas

Boiling point

-30°C

Melting point

-163.5°C

Uses

a. Refrigerant
b. Production of other chemicals
c. Solvent in chemical reactions
d. Propellant in aerosol products

Environmental hazard

Potential environmental hazard

Health risks

Toxic, can cause irritation to skin, eyes, and respiratory tract

Safety measures

Appropriate safety measures and handling procedures should be followed when working with 1,1-DICHLORO-3,3,3-TRIFLUORO-1-PROPENE

Check Digit Verification of cas no

The CAS Registry Mumber 460-70-8 includes 6 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 3 digits, 4,6 and 0 respectively; the second part has 2 digits, 7 and 0 respectively.
Calculate Digit Verification of CAS Registry Number 460-70:
(5*4)+(4*6)+(3*0)+(2*7)+(1*0)=58
58 % 10 = 8
So 460-70-8 is a valid CAS Registry Number.
InChI:InChI=1/C3HCl2F3/c4-2(5)1-3(6,7)8/h1H

460-70-8SDS

SAFETY DATA SHEETS

According to Globally Harmonized System of Classification and Labelling of Chemicals (GHS) - Sixth revised edition

Version: 1.0

Creation Date: Aug 16, 2017

Revision Date: Aug 16, 2017

1.Identification

1.1 GHS Product identifier

Product name 1,1-dichloro-3,3,3-trifluoroprop-1-ene

1.2 Other means of identification

Product number -
Other names 1,1-Dichlor-3,3,3-trifluor-propen

1.3 Recommended use of the chemical and restrictions on use

Identified uses For industry use only.
Uses advised against no data available

1.4 Supplier's details

1.5 Emergency phone number

Emergency phone number -
Service hours Monday to Friday, 9am-5pm (Standard time zone: UTC/GMT +8 hours).

More Details:460-70-8 SDS

460-70-8Relevant academic research and scientific papers

Preparation process of 1, 1-dichloro-3, 3, 3-trifluoropropene

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Paragraph 0050; 0074-0092, (2020/11/01)

The invention relates to a method for producing a 1, 1-dichloro-3, 3, 3-trifluoropropene with high added value by taking trifluoromethane and trichloroethylene as raw materials. According to the method, a catalytic system composed of a main catalyst and a catalytic auxiliary agent of specific types in a special proportion is adopted; wherein the active component of the main catalyst is selected from one or more of Fe, Co, Ni, Ru, Rh, Pd, Pt, Cu, Ag and Au, multi-stage micro/mesoporous Cr2O3 is adopted as a carrier, and a metal oxide and/or a rare earth auxiliary agent is adopted as a catalyticauxiliary agent, so that the selectivity on the target product 1, 1-dichloro-3, 3, 3-trifluoropropene is effectively improved. According to the method disclosed by the invention, not only the resource utilization of the byproduct trifluoromethane is promoted, but also the types of raw materials of the 1, 1-dichloro-3, 3, 3-trifluoropropene product are expanded, and remarkable economic benefits and social benefits are generated.

PRODUCING METHOD OF 1,1-DICHLORO-3,3,3-TRIFLUOROPROPENE

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Paragraph 0091; 0092; 0099, (2016/10/27)

PROBLEM TO BE SOLVED: To provide an economically profitable method producing 1,1-dichloro-3,3,3-trifluoropropene efficiently by an industrially possible method. SOLUTION: A producing method of 1,1-dichloro-3,3,3-trifluoropropene making 1,1,1-trichloro-3,3,3-trifluoropropane contact with a base for dehydrochlorination. SELECTED DRAWING: None COPYRIGHT: (C)2016,JPOandINPIT

PROCESS FOR 1-CHLORO-3,3,3-TRIFLUOROPROPENE FROM TRIFLUOROMETHANE

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Paragraph 0061; 0063, (2015/02/25)

The present invention provides routes for making 1-chloro-3,3,3-trifluoropropene (HCFO-1233zd) from commercially available raw materials. More specifically, this invention provides routes for HCFO-1233zd from inexpensive and commercially available trifluoromethane (HFC-23).

PROCESS FOR THE PRODUCTION OF CHLORINATED AND/OR FLUORINATED PROPENES

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Page/Page column 8, (2011/04/25)

The present invention provides one-step processes for the production of chlorinated and/or fluorinated propenes. The processes provide good product yield with low, e.g., less than about 20%, or even less than 10%, concentrations of residues/by-products. Advantageously, the processes may be conducted at low temperatures than 500° C. so that energy savings are provided, and/or at higher pressures so that high throughputs may also be realized. The use of catalysts or initiators may provide additional enhancements to conversion rates and selectivity, as may adjustments to the molar ratio of the reactants.

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