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Vinyl chloride, also known as chloroethene, is a colorless gas with a faintly sweet odor. It is primarily used to produce the polymer polyvinyl chloride (PVC). Despite its widespread industrial use, vinyl chloride is considered a hazardous chemical due to its toxic and carcinogenic properties. Exposure to vinyl chloride can occur through inhalation, ingestion, or skin contact, and long-term exposure has been linked to serious health effects such as liver damage, immune system disorders, and an increased risk of developing liver and other types of cancer.

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  • 75-01-4 Structure
  • Basic information

    1. Product Name: Vinyl chloride
    2. Synonyms: Vinyl chloride;Vinylchloride monomer;Ethylene,chloro- (8CI);1-Chloroethene;1-Chloroethylene;Chloroethene;Chloroethylene;F 1140;Monochloroethylene;VCM;Vinyl C monomer;
    3. CAS NO:75-01-4
    4. Molecular Formula: C2H3Cl
    5. Molecular Weight: 62.50
    6. EINECS: 200-831-0
    7. Product Categories: N/A
    8. Mol File: 75-01-4.mol
  • Chemical Properties

    1. Melting Point: N/A
    2. Boiling Point: -13.4 °C(lit.)
    3. Flash Point: -78 °F
    4. Appearance: colourless gas
    5. Density: 0.918 g/cm3
    6. Refractive Index: N/A
    7. Storage Temp.: N/A
    8. Solubility: N/A
    9. CAS DataBase Reference: Vinyl chloride(CAS DataBase Reference)
    10. NIST Chemistry Reference: Vinyl chloride(75-01-4)
    11. EPA Substance Registry System: Vinyl chloride(75-01-4)
  • Safety Data

    1. Hazard Codes: N/A
    2. Statements: N/A
    3. Safety Statements: N/A
    4. WGK Germany:
    5. RTECS:
    6. HazardClass: N/A
    7. PackingGroup: N/A
    8. Hazardous Substances Data: 75-01-4(Hazardous Substances Data)

75-01-4 Usage

Uses

Used in Plastics and Vinyl Manufacturing Industry:
Vinyl chloride is used as a monomer for the production of polyvinyl chloride (PVC), a versatile polymer with a wide range of applications in various industries. PVC is valued for its durability, flexibility, and resistance to chemicals, making it suitable for manufacturing products such as pipes, fittings, films, and containers.
Used in Chemical Industry:
Vinyl chloride is also used as a raw material in the production of other chemicals, including vinyl chloride monomers, which are used in the synthesis of various polymers and copolymers.
Occupational Exposure:
Workers in industries that produce or use PVC, such as the plastics and vinyl manufacturing industries, may be occupationally exposed to vinyl chloride. To minimize the risk of exposure and protect the health and safety of workers, strict safety measures and regulations are in place. These measures include proper ventilation, use of personal protective equipment, and adherence to exposure limits and guidelines.
Public Health and Safety:
Due to the toxic and carcinogenic properties of vinyl chloride, strict regulations are also in place to protect the general public from exposure. This includes monitoring and controlling the release of vinyl chloride into the environment, as well as ensuring the safe disposal and handling of PVC products and waste materials.

Check Digit Verification of cas no

The CAS Registry Mumber 75-01-4 includes 5 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 2 digits, 7 and 5 respectively; the second part has 2 digits, 0 and 1 respectively.
Calculate Digit Verification of CAS Registry Number 75-01:
(4*7)+(3*5)+(2*0)+(1*1)=44
44 % 10 = 4
So 75-01-4 is a valid CAS Registry Number.
InChI:InChI=1/C2H3Cl/c1-2-3/h2H,1H2

75-01-4 Well-known Company Product Price

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  • Supelco

  • (48625)  Vinylchloridesolution  200 μg/mL in methanol, analytical standard

  • 75-01-4

  • 000000000000048625

  • 188.37CNY

  • Detail
  • Supelco

  • (500976)  Vinylchloridesolution  certified reference material, 2000 μg/mL in methanol

  • 75-01-4

  • 000000000000500976

  • 347.49CNY

  • Detail

75-01-4SDS

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 chloroethene

1.2 Other means of identification

Product number -
Other names Ethene, chloro-

1.3 Recommended use of the chemical and restrictions on use

Identified uses For industry use only. Volatile organic compounds
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:75-01-4 SDS

75-01-4Synthetic route

acetylene
74-86-2

acetylene

chloroethylene
75-01-4

chloroethylene

Conditions
ConditionsYield
With hydrogenchloride; oxygen at 199.84℃; under 750.075 Torr; for 12h; Reagent/catalyst; Flow reactor; Inert atmosphere;100%
With hydrogenchloride at 180℃; Reagent/catalyst;99.9%
With hydrogenchloride In water at 250℃; under 825.083 - 900.09 Torr; Temperature; Reagent/catalyst;68%
1,2-dichloro-ethane
107-06-2

1,2-dichloro-ethane

A

hydrogenchloride
7647-01-0

hydrogenchloride

B

chloroethylene
75-01-4

chloroethylene

Conditions
ConditionsYield
at 450 - 550℃; under 10501.1 - 26252.6 Torr; for 0.00416667 - 0.00833333h;A n/a
B 99.52%
at 362 - 485℃; eine nahezu homogene Reaktion erster Ordnung, die wahrscheinlich von Chloratomen und 1.2-Dichlor-aethyl-Radikalen unterhalten wird.Thermolysis;
at 600℃; Conversion of starting material;
at 615℃; Rate constant;
at 650℃; Rate constant;
1,2-dichloro-ethane
107-06-2

1,2-dichloro-ethane

chloroethylene
75-01-4

chloroethylene

Conditions
ConditionsYield
With triethylbenzylammonium ethanolate at -20 - 20℃;99%
75%
With polyacrylonitrile-based active carbon fiber at 350℃; under 760 Torr; for 2h; other catalyst, var. reaction time;57%
-butyl vinyl ether
111-34-2

-butyl vinyl ether

Phenyltrichlorosilane
98-13-5

Phenyltrichlorosilane

A

chloroethylene
75-01-4

chloroethylene

B

dichloro(butoxy)phenylsilane
17887-35-3

dichloro(butoxy)phenylsilane

Conditions
ConditionsYield
at 20℃; for 24h;A n/a
B 96%
methylchlorodiazirine
4222-21-3

methylchlorodiazirine

chloroethylene
75-01-4

chloroethylene

Conditions
ConditionsYield
In n-heptane Quantum yield; Irradiation;90%
β-chlorovinyl(methyl)dichlorosilane
13852-29-4

β-chlorovinyl(methyl)dichlorosilane

A

Methyltrichlorosilane
75-79-6

Methyltrichlorosilane

B

1,1-dichloroethane
75-34-3

1,1-dichloroethane

C

chloroethylene
75-01-4

chloroethylene

D

dichloro-(2,2-dichloro-ethyl)-methyl-silane

dichloro-(2,2-dichloro-ethyl)-methyl-silane

Conditions
ConditionsYield
With hydrogenchloride; iron(III) chloride at 25 - 31℃; for 4h; Product distribution; Further Variations:; Temperatures; reaction time, reagent concentration; Addition; elimination;A n/a
B n/a
C n/a
D 89%
1,2-dichloro-ethane
107-06-2

1,2-dichloro-ethane

A

ethene
74-85-1

ethene

B

chloroethane
75-00-3

chloroethane

C

chloroethylene
75-01-4

chloroethylene

Conditions
ConditionsYield
With hydrogen; Ni on pumice at 350℃; Product distribution; other temperature;A 83.7%
B 0.6%
C 0.7%
Trichloroethylene
79-01-6

Trichloroethylene

A

cis-1,2-Dichloroethylene
156-59-2

cis-1,2-Dichloroethylene

B

chloroethylene
75-01-4

chloroethylene

C

acetylene
74-86-2

acetylene

Conditions
ConditionsYield
With iron sulfide In water for 2922h; pH=8.3; Kinetics; Product distribution; Dehydrochlorination;A 6%
B 1%
C 65%
-butyl vinyl ether
111-34-2

-butyl vinyl ether

(chloromethyl)trichlorosilane
1558-25-4

(chloromethyl)trichlorosilane

A

chloroethylene
75-01-4

chloroethylene

B

dichloro(chloromethyl)butoxysilane

dichloro(chloromethyl)butoxysilane

Conditions
ConditionsYield
at 20℃; for 24h;A n/a
B 57%
Methyltrichlorosilane
75-79-6

Methyltrichlorosilane

-butyl vinyl ether
111-34-2

-butyl vinyl ether

A

chloroethylene
75-01-4

chloroethylene

B

dichloro(butoxy)methylsilane
1825-78-1

dichloro(butoxy)methylsilane

Conditions
ConditionsYield
at 20℃; for 24h;A n/a
B 45%
(tris(3,5-dimethylpyrazolyl)borate)Rh(PMe3)(CH3)H

(tris(3,5-dimethylpyrazolyl)borate)Rh(PMe3)(CH3)H

1,2-dichloro-ethane
107-06-2

1,2-dichloro-ethane

A

ethene
74-85-1

ethene

B

chloroethylene
75-01-4

chloroethylene

C

(η(3)-tris(3,5-dimethylpyrazolyl)borato)Rh(PMe3)(Cl)2

(η(3)-tris(3,5-dimethylpyrazolyl)borato)Rh(PMe3)(Cl)2

D

[(HB(N2C3H(CH3)2)3)RhH(P(CH3)3)Cl]

[(HB(N2C3H(CH3)2)3)RhH(P(CH3)3)Cl]

Tp’RhCl(PMe3)(η1-CH=CH2)

Tp’RhCl(PMe3)(η1-CH=CH2)

Conditions
ConditionsYield
at 22℃; for 72h; Sealed tube; Inert atmosphere;A Ca. 10 %Spectr.
B Ca. 15 %Spectr.
C 41%
D 44%
E 15%
methylene chloride
74-87-3

methylene chloride

chloroethylene
75-01-4

chloroethylene

Conditions
ConditionsYield
With oxygen at 600℃; Reagent/catalyst;42%
-butyl vinyl ether
111-34-2

-butyl vinyl ether

A

chloroethylene
75-01-4

chloroethylene

B

n-butoxytrichlorosilane
1825-85-0

n-butoxytrichlorosilane

Conditions
ConditionsYield
With tetrachlorosilane at 20℃; for 24h;A n/a
B 37%
-butyl vinyl ether
111-34-2

-butyl vinyl ether

dichloromethylphenylsilane
149-74-6

dichloromethylphenylsilane

A

chloroethylene
75-01-4

chloroethylene

B

chloro(butoxy)(methyl)phenylsilane
18001-27-9

chloro(butoxy)(methyl)phenylsilane

Conditions
ConditionsYield
at 20℃; for 24h;A n/a
B 32%
dichloromethane
75-09-2

dichloromethane

chloroethylene
75-01-4

chloroethylene

Conditions
ConditionsYield
With hydrogen at 500℃; under 1520.1 Torr; Reagent/catalyst; Temperature; Pressure;23.2%
1,1-dichloroethane
75-34-3

1,1-dichloroethane

ethene
74-85-1

ethene

A

chloroethane
75-00-3

chloroethane

B

chloroethylene
75-01-4

chloroethylene

Conditions
ConditionsYield
With calcium sulfate at 260℃; under 14710.2 Torr;
1,1-dichloroethane
75-34-3

1,1-dichloroethane

chloroethylene
75-01-4

chloroethylene

Conditions
ConditionsYield
With sodium ethanolate
With pumice stone
With Y-type zeolite In chloroform at 125℃; under 760.051 Torr; Temperature;
With aluminum oxide at 300℃;
cis-dichloro(2-chlorovinyl) arsine
34461-56-8

cis-dichloro(2-chlorovinyl) arsine

1-methyl-4-nitrosobenzene
623-11-0

1-methyl-4-nitrosobenzene

chloroethylene
75-01-4

chloroethylene

Conditions
ConditionsYield
at 40℃;
ethane
74-84-0

ethane

chloroethylene
75-01-4

chloroethylene

Conditions
ConditionsYield
With aluminum oxide; chlorine at 400℃;
at 380℃; bei der thermischen Chlorieren;
bei der photochemischen Chlorierung;
With chlorine at 500℃;
With hydrogenchloride In neat (no solvent, gas phase) at 400℃; Kinetics; Catalytic behavior; Temperature; Reagent/catalyst;
ethene
74-85-1

ethene

chloroethylene
75-01-4

chloroethylene

Conditions
ConditionsYield
With chlorine at 400℃;
With chlorine anschl. HCl-Abspaltung ueber Aktivkohle bei 400grad-450grad;
With chlorine
1-chloro-1-fluoroethane
1615-75-4

1-chloro-1-fluoroethane

A

1-fluoroethylene
75-02-5

1-fluoroethylene

B

chloroethylene
75-01-4

chloroethylene

Conditions
ConditionsYield
at 600℃;
1,1,2-trichloroethane
79-00-5

1,1,2-trichloroethane

chloroethylene
75-01-4

chloroethylene

Conditions
ConditionsYield
With sodium amalgam; nickel(I)octaethylisobacteriochlorin In N,N-dimethyl-formamide at 23℃; Rate constant;
With water; iron at 100 - 120℃; unter Druck;
With water; zinc at 50 - 60℃;
2-chloro-1-acetoxyethane
542-58-5

2-chloro-1-acetoxyethane

A

chloroethylene
75-01-4

chloroethylene

B

acetic acid
64-19-7

acetic acid

Conditions
ConditionsYield
Erhitzen;
2-chloroethyl benzenesulfonate
16670-48-7

2-chloroethyl benzenesulfonate

A

chloroethylene
75-01-4

chloroethylene

B

acetaldehyde
75-07-0

acetaldehyde

C

benzenesulfonic acid
98-11-3

benzenesulfonic acid

Conditions
ConditionsYield
at 285 - 290℃;
1,2-dichloro-ethane
107-06-2

1,2-dichloro-ethane

acetylene
74-86-2

acetylene

chloroethylene
75-01-4

chloroethylene

Conditions
ConditionsYield
With mercury(I) chloride; potassium chloride at 375℃;
With mercury dichloride; barium(II) chloride at 350 - 450℃;
ethylene dibromide
106-93-4

ethylene dibromide

A

2-fluoroethyl bromide
762-49-2

2-fluoroethyl bromide

B

chloroethylene
75-01-4

chloroethylene

Conditions
ConditionsYield
With potassium fluoride; ethylene glycol at 150℃;
With potassium fluoride at 200℃;
3-oxa-1,5-dichloropentane
111-44-4

3-oxa-1,5-dichloropentane

A

chloroethylene
75-01-4

chloroethylene

B

2-chloroetyl vinyl ether
110-75-8

2-chloroetyl vinyl ether

Conditions
ConditionsYield
at 450℃;
chlorobenzene
108-90-7

chlorobenzene

chloroethylene
75-01-4

chloroethylene

chloroethylene
75-01-4

chloroethylene

bis-trifluoromethyl-aminooxyl
2154-71-4

bis-trifluoromethyl-aminooxyl

1,2-bischloroethane
67329-57-1

1,2-bischloroethane

Conditions
ConditionsYield
for 0.833333h; Ambient temperature;99%
chloroethylene
75-01-4

chloroethylene

perfluoro(2,4-dimethyl-3-oxa-2,4-diazapentane)
6141-72-6

perfluoro(2,4-dimethyl-3-oxa-2,4-diazapentane)

O-[2-(Bis-trifluoromethyl-amino)-1-chloro-ethyl]-N,N-bis-trifluoromethyl-hydroxylamine

O-[2-(Bis-trifluoromethyl-amino)-1-chloro-ethyl]-N,N-bis-trifluoromethyl-hydroxylamine

Conditions
ConditionsYield
for 120h; Ambient temperature; in vacuo;98%
chloroethylene
75-01-4

chloroethylene

1-chloro-1,3-bis(2,4,6-trichlorophenyl)triazene
187464-05-7

1-chloro-1,3-bis(2,4,6-trichlorophenyl)triazene

1,3-bis(2,4,6-trichlorophenyl)-1,2,3-triazolium hexachloroantimonate

1,3-bis(2,4,6-trichlorophenyl)-1,2,3-triazolium hexachloroantimonate

Conditions
ConditionsYield
With antimonypentachloride In dichloromethane at -60 - 23℃; for 1.75h;98%
3-[2-(7-chloro-2-quinolinyl)ethenyl]benzaldehyde
115104-40-0

3-[2-(7-chloro-2-quinolinyl)ethenyl]benzaldehyde

chloroethylene
75-01-4

chloroethylene

1‐[3‐(2‐(7-chloro‐2‐quinolinyl)vinyl)phenyl]‐2-propen-1-ol

1‐[3‐(2‐(7-chloro‐2‐quinolinyl)vinyl)phenyl]‐2-propen-1-ol

Conditions
ConditionsYield
With ammonium acetate In toluene at -2 - 5℃; Reagent/catalyst; Inert atmosphere;97.2%
methanol
67-56-1

methanol

chloroethylene
75-01-4

chloroethylene

chloroacetaldehyde dimethyl acetal
97-97-2

chloroacetaldehyde dimethyl acetal

Conditions
ConditionsYield
With sodium methylate; chlorine at 25 - 27℃; for 5.5h; pH=3 - 7; Temperature; Large scale;97.2%
chloroethylene
75-01-4

chloroethylene

1,2-dibromo-1-chloroethane
598-20-9

1,2-dibromo-1-chloroethane

Conditions
ConditionsYield
With bromine at 20℃; for 17h; Cooling;97%
With bromine
With bromine In tetrachloromethane
With bromine; dinitrogen tetraoxide In chloroform
With bromine; Nitrogen dioxide at 325℃;
tetrachloromethane
56-23-5

tetrachloromethane

chloroethylene
75-01-4

chloroethylene

1,1,1,3,3-pentachloropropane
23153-23-3

1,1,1,3,3-pentachloropropane

Conditions
ConditionsYield
With iron; orthoformic acid triethyl ester at 130℃; under 2250.23 Torr; for 0.5h; Temperature; Pressure; Reagent/catalyst;96.6%
With iron(III) chloride; phosphoric acid tributyl ester under 1125.11 Torr; for 100h; Flow reactor; Large scale;95.6%
Stage #1: tetrachloromethane With N,N,N,N,N,N-hexamethylphosphoric triamide; chloroform; iron at 140℃; for 0.5h; Autoclave; Inert atmosphere;
Stage #2: chloroethylene at 140℃; for 3h; Reagent/catalyst; Autoclave; Inert atmosphere;
93.1%
benzophenone
119-61-9

benzophenone

chloroethylene
75-01-4

chloroethylene

1,1-diphenylprop-2-en-1-ol
3923-51-1

1,1-diphenylprop-2-en-1-ol

Conditions
ConditionsYield
Stage #1: chloroethylene; zinc(II) chloride In tetrahydrofuran at 20℃; for 1h;
Stage #2: benzophenone In tetrahydrofuran at 0℃; for 2h;
96%
chloroethylene
75-01-4

chloroethylene

[Li(Et2O)2.8][B(C6F5)4]

[Li(Et2O)2.8][B(C6F5)4]

chloro(4,4'-di-tert-butyl-2,2'-bipyridine)methylpalladium(II)
524936-75-2

chloro(4,4'-di-tert-butyl-2,2'-bipyridine)methylpalladium(II)

carbon monoxide
201230-82-2

carbon monoxide

[(4,4'-di-tert-butyl-2,2'-bipyridine)Pd(CHClCH2COMe)][B(C6F5)4]
524936-99-0

[(4,4'-di-tert-butyl-2,2'-bipyridine)Pd(CHClCH2COMe)][B(C6F5)4]

Conditions
ConditionsYield
In dichloromethane-d2 byproducts: LiCl, Et2O; stirring of ((t-Bu)2bipy)PdMeCl, (Li(Et2O)2.8)B(C6F5)4 (1 eqiuv.) and CH2Cl2 in Schlenk flask at -78°C for 10 min, exposure to CO (1 atm)at -78°C for 30 min, freezing to -196°C, evacuating, addn . of CH2CHCl, stirring at 23°C; filtration, drying of filtrate under vac., elem. anal.;96%
chloroethylene
75-01-4

chloroethylene

1,8-diazabicyclo[5.4.0]undec-7-ene
6674-22-2

1,8-diazabicyclo[5.4.0]undec-7-ene

6-vinyl DBU
1268387-98-9

6-vinyl DBU

Conditions
ConditionsYield
Stage #1: 1,8-diazabicyclo[5.4.0]undec-7-ene With n-butyllithium In tetrahydrofuran; hexane at -78℃; for 1h;
Stage #2: chloroethylene In tetrahydrofuran; hexane at -78 - 20℃;
96%
chloroethylene
75-01-4

chloroethylene

4-(Methylthio)benzaldehyde
3446-89-7

4-(Methylthio)benzaldehyde

1-[4-(methylsulfanyl)phenyl]-2-propen-1-ol
701935-64-0

1-[4-(methylsulfanyl)phenyl]-2-propen-1-ol

Conditions
ConditionsYield
Stage #1: chloroethylene With magnesium In tetrahydrofuran at 0 - 20℃; for 0.5h; Inert atmosphere;
Stage #2: 4-(Methylthio)benzaldehyde In tetrahydrofuran at 0 - 20℃; Grignard reaction;
Stage #3: With water; ammonium chloride In tetrahydrofuran Grignard reaction;
96%
chloroethylene
75-01-4

chloroethylene

9H-carbazole
86-74-8

9H-carbazole

9-vinyl-9H-carbazole
1484-13-5

9-vinyl-9H-carbazole

Conditions
ConditionsYield
With bis(η3-allyl-μ-chloropalladium(II)); sodium hydroxide; tri tert-butylphosphoniumtetrafluoroborate In toluene at 100℃; for 10h; Reagent/catalyst; Inert atmosphere;96%
tertiary butyl chloride
507-20-0

tertiary butyl chloride

chloroethylene
75-01-4

chloroethylene

1,1-dichloro-3,3-dimethylbutane
6130-96-7

1,1-dichloro-3,3-dimethylbutane

Conditions
ConditionsYield
With aluminium trichloride In dichloromethane at -40 - -10℃; for 0.5h;95%
With iron(III) chloride unter Stickstoffdruck;
With aluminium trichloride at -25℃;
With iron(III) chloride
With aluminium trichloride
chloroethylene
75-01-4

chloroethylene

rac-(EBI)Zr(Me)(μ-Me)B(C6F5)3

rac-(EBI)Zr(Me)(μ-Me)B(C6F5)3

oligopropylene, atactic, Mn = 500

oligopropylene, atactic, Mn = 500

Conditions
ConditionsYield
In dichloromethane-d2 at 25℃; for 24h; Polymerization; dechlorination; methylation;95%
chloroethylene
75-01-4

chloroethylene

carbon monoxide
201230-82-2

carbon monoxide

dimethyl amine
124-40-3

dimethyl amine

3-(dimthylamino)-N,Ndimethylpropanamide hydrochloride
110570-37-1

3-(dimthylamino)-N,Ndimethylpropanamide hydrochloride

Conditions
ConditionsYield
With tetrakis(triphenylphosphine) palladium(0) at 100℃; Product distribution; Mechanism; other substituted vinyl chlorides, other amines and NH3, var. temp.;94%
chloroethylene
75-01-4

chloroethylene

bis-(3,5-dimethylphenyl)chlorophosphine
74289-57-9

bis-(3,5-dimethylphenyl)chlorophosphine

vinyl bis(3,5-dimethylphenyl)phosphine

vinyl bis(3,5-dimethylphenyl)phosphine

Conditions
ConditionsYield
In tetrahydrofuran at 0 - 20℃; for 10h; Inert atmosphere;94%
chloroethylene
75-01-4

chloroethylene

N-phenylbenzohydrazonoyl chloride
15424-14-3

N-phenylbenzohydrazonoyl chloride

1,3-diphenyl-1H-pyrazole
4492-01-7

1,3-diphenyl-1H-pyrazole

Conditions
ConditionsYield
With triethylamine; hydroquinone In benzene for 48h; Ambient temperature;93%
chloroethylene
75-01-4

chloroethylene

1,1,2,2,3,3-Hexafluoro-cyclopropane
931-91-9

1,1,2,2,3,3-Hexafluoro-cyclopropane

A

polytetrafluoroethylene
116-14-3

polytetrafluoroethylene

B

Octafluorocyclobutane
115-25-3

Octafluorocyclobutane

C

1,1-difluoro-2-chlorocyclopropane
54944-21-7

1,1-difluoro-2-chlorocyclopropane

Conditions
ConditionsYield
at 294℃; for 1h; sealed tube in vacuo;A 91%
B 19%
C 55%
chloroethylene
75-01-4

chloroethylene

[Li(Et2O)2.8][B(C6F5)4]

[Li(Et2O)2.8][B(C6F5)4]

[(4,4'-dimethyl-2,2'-bipyridine)Pd(Me)Cl]
524936-74-1

[(4,4'-dimethyl-2,2'-bipyridine)Pd(Me)Cl]

carbon monoxide
201230-82-2

carbon monoxide

[(4,4'-dimethyl-2,2'-bipyridine)Pd(CHClCH2COMe)][B(C6F5)4]
524936-97-8

[(4,4'-dimethyl-2,2'-bipyridine)Pd(CHClCH2COMe)][B(C6F5)4]

Conditions
ConditionsYield
In dichloromethane-d2 byproducts: LiCl, Et2O; stirring of (Me2bipy)PdMeCl, (Li(Et2O)2.8)(B(C6F5)4) (1 equiv.) and CH2Cl2 in Schlenk flask at -78°C for 10 min, exposure to CO (1 atm) at -78°C for 30 min, freezing to -196°C, evacuating, addn. of CH2CHCl, stirring at 23°C; filtration, drying of filtrate under vac., elem. anal.;91%
chloroethylene
75-01-4

chloroethylene

1-{2-[2-(2-vinyloxyethoxy)ethoxy]ethoxy}-2,3-epoxypropane
16801-24-4

1-{2-[2-(2-vinyloxyethoxy)ethoxy]ethoxy}-2,3-epoxypropane

1-{2-[2-(2-vinyloxyethoxy)ethoxy]ethoxy}-2,3-epoxypropane - vinyl chloride copolymer, vinyl chloride 74.24 mol percent; monomer(s): 1-{2-[2-(2-vinyloxyethoxy)ethoxy]ethoxy}-2,3-epoxypropane; vinyl chloride

1-{2-[2-(2-vinyloxyethoxy)ethoxy]ethoxy}-2,3-epoxypropane - vinyl chloride copolymer, vinyl chloride 74.24 mol percent; monomer(s): 1-{2-[2-(2-vinyloxyethoxy)ethoxy]ethoxy}-2,3-epoxypropane; vinyl chloride

Conditions
ConditionsYield
With 2,2'-azobis(isobutyronitrile) In dimethyl sulfoxide at 70℃;88.9%
chloroethylene
75-01-4

chloroethylene

1-{2-[2-(2-vinyloxyethoxy)ethoxy]ethoxy}-2,3-epoxypropane
16801-24-4

1-{2-[2-(2-vinyloxyethoxy)ethoxy]ethoxy}-2,3-epoxypropane

1-{2-[2-(2-vinyloxyethoxy)ethoxy]ethoxy}-2,3-epoxypropane - vinyl chloride copolymer, vinyl chloride 77.78 mol percent; monomer(s): 1-{2-[2-(2-vinyloxyethoxy)ethoxy]ethoxy}-2,3-epoxypropane; vinyl chloride

1-{2-[2-(2-vinyloxyethoxy)ethoxy]ethoxy}-2,3-epoxypropane - vinyl chloride copolymer, vinyl chloride 77.78 mol percent; monomer(s): 1-{2-[2-(2-vinyloxyethoxy)ethoxy]ethoxy}-2,3-epoxypropane; vinyl chloride

Conditions
ConditionsYield
With 2,2'-azobis(isobutyronitrile) In acetone at 70℃;88.6%
[PdCl(CH3)(bis(diphenylphosphino)propane)]
139168-06-2

[PdCl(CH3)(bis(diphenylphosphino)propane)]

chloroethylene
75-01-4

chloroethylene

[Li(Et2O)2.8][B(C6F5)4]

[Li(Et2O)2.8][B(C6F5)4]

carbon monoxide
201230-82-2

carbon monoxide

[(1,3-bis(diphenylphosphino)propane)Pd(CHClCH2COMe)][B(C6F5)4]
524937-01-7

[(1,3-bis(diphenylphosphino)propane)Pd(CHClCH2COMe)][B(C6F5)4]

Conditions
ConditionsYield
In dichloromethane-d2 byproducts: LiCl, Et2O; stirring of (dppp)PdMeCl, (Li(Et2O)2.8)B(C6F5)4 (1 eqiuv.) and CH2Cl2 inSchlenk flask at -78°C for 10 min, exposure to CO (1 atm) at -78 °C for 30 min, freezing to -196°C, evacuating, addn. of CH2CHCl, stirring at 23°C; filtration, drying of filtrate under vac., elem. anal.;88%

75-01-4Relevant articles and documents

Non-mercury catalytic acetylene hydrochlorination over a NH4F-urea-modified Pd/HY catalyst for vinyl chloride monomer production

Wang, Lu,Wang, Feng,Wang, Jide

, p. 3019 - 3023 (2016)

A Pd/HY zeolite catalyst modified with ammonium fluoride and urea (Pd/NH4F-urea-HY) was efficiently applied in an acetylene hydrochlorination reaction. It exhibited an enhanced catalytic performance compared to the untreated Pd/HY catalyst, which was attributed to the presence of ammonium fluoride and urea partly inhibiting carbon deposition and Pd2+ reduction.

High performance of supported Cu-based catalysts modulated via phosphamide coordination in acetylene hydrochlorination

Hu, Yubing,Wang, Yan,Wang, Yulian,Li, Wei,Zhang, Jinli,Han, You

, (2020)

In order to develop a cut-price, high-efficiency non-mercuric catalyst for acetylene hydrochlorination reaction, several kinds of supported Cu-based catalysts containing phosphoramide ligands have been synthesized by wet impregnation method. The outstanding catalytic activity was obtained over 15 %Cu10 %HMPA/SAC catalyst with acetylene conversion of 87.25 % in the test conditions of T =180 °C, GHSV(C2H2) =180 h?1 and V(HCl): V(C2H2) = 1.2. The catalyst with optimal HMPA ligand also exhibited splendid stability in 100 h lifetime test. The analysis for XRD, TEM, TGA, ICP, H2-TPR and XPS indicated that HMPA ligand can improve Cu species dispersion, restrain coke deposition, suppress loss of loading Cu, and stabilize valence state of active Cu species. Due to electron transfer mechanism, steady coordination structure between Cu and HMPA led to favorable properties of Cu-based catalyst, which was further proved by FT-IR, Raman spectra, O 1s XPS spectra integrated with DFT calculations.

An efficient Au catalyst supported on hollow carbon spheres for acetylene hydrochlorination

Kang, Lihua,Zhu, Mingyuan

, p. 31812 - 31818 (2019)

Mesoporous hollow carbon spheres (HCSs) were prepared using SiO2 spheres as a hard template, and Au nanoparticles were then synthesized using NaBH4 as a reducing agent on the surface of the HCS support. Transmission electron microscopy characterization indicated that Au nanoparticles were much smaller on the HCS support than those on the active carbon (AC) support. HCl-TPD showed that the Au/HCS catalyst displayed a more active site than on Au/AC. The resulting Au/HCS catalyst showed excellent catalytic activity and stability for acetylene hydrochlorination. Acetylene conversion of Au/HCS can be maintained above 92% even after 500 h of lifetime. The excellent catalytic performance of Au/HCS was attributed to the presence of the HCS support, which limited the aggregation of Au nanoparticles.

Active carbon supported S-promoted Bi catalysts for acetylene hydrochlorination reaction

Hu, Di,Wang, Lu,Wang, Feng,Wang, Jide

, p. 1413 - 1416 (2018)

In the present work, the sulfur doped bismuth-based catalysts were prepared by incipient wetness impregnation method and used for the hydrochlorination of acetylene to vinyl chloride monomer (VCM) in a fixed-bed reactor. The effect of introduction of S was characterized by N2 adsorption-desorption, powder X-ray diffraction, transmission electron microscopy, thermogravimetric analysis, temperature-programmed reduction and X-ray photoelectron spectroscopy. The characterization results indicated that the doping of S resulted in the increase of Brunauer-Emmett-Teller (BET) surface areas and decrease of active species particle size for the Bi-based catalysts, which led to more accessible active sites, and consequently boosted the catalytic hydrochlorination activity. The effect of H2SO4 concentration on the activity of this type catalyst was examined, and the results showed that there is an optimal loading of H2SO4 (S/Bi = 0.5 mol/mol), at which the conversion of C2H2 was enhanced to 81% under the reaction condition and coke deposition is a main reason for the deactivation of catalyst.

Unimolecular HCl elimination from 1,2-dichloroethane: A single pulse shock tube and ab initio study

Rajakumar,Reddy,Arunan

, p. 8366 - 8373 (2002)

Thermal decomposition of 1,2-dichloroethane (1,2-DCE) has been studied in the temperature range of 1050-1175 K behind reflected shock waves in a single pulse shock tube. The unimolecular elimination of HCl is found to be the major channel through which 1,2-DCE decomposes under these conditions. The rate constant for the unimolecular elimination of HCl from 1,2-dichloroethane is found to be 1013.98±0.80 exp(-57.8 ± 2.0/RT) s-1, where the activation energy is given in kcal mol-1 and is very close to that value for CH3CH2Cl (EC). Ab initio (HF and MP2) and DFT calculations have been carried out to find the activation barrier and the structure of the transition state for this reaction channel from both EC and 1,2-DCE. The preexponential factors calculated at various levels of theory (HF/6-311 ++G*, MP2/6-311 ++G*, and B3LYP/6-311 ++G*) are (≈ 1015 s-1) significantly larger than the experimental results. If the torsional mode in the ground state is treated as free internal rotation the preexponential factors reduce significantly, giving excellent agreement with experimental values. The DFT results are in excellent (fortuitous?) agreement with the experimental value for activation energy for 1,2-DCE while the MP2 and HF results seem to overestimate the barrier. However, DFT results for EC is 4.5 kcal mol-1 less than the previously reported experimental values. At all levels, theory predicts an increase in HCl elimination barrier on β-Cl substitution on EC.

Hydrochlorination of acetylene using expanded multilayered vermiculite (EML-VMT)-supported catalysts

Xin-Huang,Yu, Feng,Zhu, Ming-Yuan,Ouyang, Fei-Hong,Dai, Bin,Dan, Jian-Ming

, p. 1101 - 1104 (2015)

Catalyst supports have very important effects on catalyst performance. A novel expanded multilayered vermiculite (EML-VMT) is successfully used as the catalyst support for the acetylene hydrochlorination. By mixing carbon on the surface of EML-VMT (i.e., EML-VMT-C), the HgCl2/EML-VMT-C achieved a high acetylene conversion of 97.3%, a vinyl chloride selectivity of 100% and a turn over frequency (TOF) value 8.83*10-3s-1 a temperature of 140 8C, an acetylene gas hourly space velocity (GHSV) of 108 h-1, and a feed volume ratio V(HCl)/V(C2H2) of 1.15. Moreover, the HgCl2/EML-VMT-C shows good stability. The EML-VMT also shows potential in the preparation of other EML-VMT-supported catalysts.

Kinetics of acetylene hydrochlorination over bimetallic Au-Cu/C catalyst

Wang, Shengjie,Shen, Benxian,Song, Qinglei

, p. 102 - 109 (2010)

A kinetic model of the acetylene hydrochlorination over the bimetallic Au-Cu/C catalyst was obtained on the basis of kinetic data. DFT theoretical calculation and the kinetic model indicated the reaction probably proceeds via the Eley-Rideal mechanism in which gas phase HCl reacts with the adsorbed C 2H2 to produce vinyl chloride. Reaction conditions were optimized according to kinetics analyses. Under the optimized reaction conditions obtained, the bimetallic Au-Cu/C showed excellent performances with more than 99.5% conversion and selectivity and did not deactivate in 200 h on stream.

An Au-Cu bimetal catalyst for acetylene hydrochlorination with renewable γ-Al2O3 as the support

Zhao, Jigang,Zeng, Junjian,Cheng, Xiaoguang,Wang, Lei,Yang, Henghua,Shen, Benxian

, p. 16727 - 16734 (2015)

The bimetal catalyst gold(iii) chloride-copper(ii) chloride (AuCl3-CuCl2) was prepared with several different gamma-aluminium oxide (γ-Al2O3) supports and its catalytic properties towards acetylene hydrochlorination were assessed in a fixed-bed reactor. The comparison indicated that one of the catalysts attained the highest activity with an acetylene conversion of 97%, which was far higher than the others. Catalysts were characterized using detailed X-ray diffraction, nitrogen-Brunauer, Emmett and Teller surface area analysis (N2-BET), ammonia temperature-programmed desorption, Fourier-transform infrared spectroscopy and carbon dioxide temperature-programmed desorption analysis. It is proposed that the base site contributed to its high catalyst activity compared with the other catalysts, instead of the acid site or the textural properties on the support, therefore, the activity and the life of the catalysts can be improved significantly by treating the supports with potassium hydroxide. In addition, the results of N2-BET, thermogravimetric analysis and scanning electron microscopy indicated that the catalysts deactivated rapidly because of carbon deposition, and the actual amount of coke deposition was 18.0% after the reaction. AuCl3-CuCl2/γ-Al2O3 was easily regenerated for reuse as a catalyst by burning off in an air atmosphere for 10 min. The activity of the regenerated catalyst nearly reached the level of the fresh catalyst. This journal is

Chlorocuprate(i) ionic liquid as an efficient and stable Cu-based catalyst for hydrochlorination of acetylene

Ren, Yanfei,Wu, Botao,Wang, Fumin,Li, Hang,Lv, Guojun,Sun, Mingshuai,Zhang, Xubin

, p. 2868 - 2878 (2019)

The gas-liquid reaction process for acetylene hydrochlorination, especially using ionic liquids (ILs) as homogeneous reaction media, has gained much attention because it can effectively avoid the deactivation caused by hot spots and carbon deposition. However, the relatively low activity and high price of the currently used ILs limit their practical applications. Herein, we synthesize a series of chlorocuprate(i) ILs to explore an efficient and stable Cu-based catalyst for acetylene hydrochlorination. The N-methylpyrrolidonium hydrochloride-0.60CuCl ([Hnmpo]Cl-0.60CuCl) IL exhibits the best catalytic performance, showing an acetylene conversion of 86% over 150 h under the conditions of 180 °C and 50 h-1 GHSV. It is confirmed that the Cu(i) species is the major active component and extremely stable under the reaction conditions via characterization of TGA-DSC-FTIR, ICP-OES, XPS, UV-vis, ESI-MS, and Raman. In addition, the [Hnmpo]Cl-0.60CuCl IL has the capacity to effectively activate HCl, which is directly observed by in situ FTIR. By combining the experimental results and theoretical calculations, we propose the reaction mechanism and find that the catalytic performance of chlorocuprate(i) ILs is positively correlated with the adsorption of HCl. The strong interaction with HCl is identified as the key characteristic of the [Hnmpo]Cl-CuCl IL, which endows it with excellent catalytic performance. Briefly, this study shows that the cost-effective [Hnmpo]Cl-CuCl IL can be a viable alternative to the commercial heterogeneous HgCl2/AC catalyst for acetylene hydrochlorination.

Novel nonmetal catalyst of supported tetraphenylphosphonium bromide for acetylene hydrochlorination

Li, Xiaoyan,Nian, Yao,Shang, Shanshan,Zhang, Haiyang,Zhang, Jinli,Han, You,Li, Wei

, p. 188 - 198 (2019)

Tetraphenylphosphonium bromide (TPPB) ionic liquid-supported catalysts were synthesized and evaluated for the acetylene hydrochlorination reaction for the development of highly efficient nonmetal catalysts as substitutes for the currently used industrial mercuric catalyst in the production of vinyl chloride (VCM). The optimal 15% TPPB/SAC catalyst exhibited favorable catalytic activity and stability, with the highest acetylene conversion of 97.1% and the selectivity for VCM above 99.5% under the conditions of 220 °C, an acetylene gas hourly space velocity (GHSV) = 30 h-1 and VHCl/VC2H2 = 1.15. Characterized by TPD, FTIR, XPS, etc., TPPB exhibits strong adsorption toward HCl but very weak adsorption toward C2H2 and VCM; in particular, the adsorbed HCl can change the conformational structure of TPPB. DFT calculations suggest that over the active catalytic site of TPPB, the activation energy of acetylene hydrochlorination is 21.15 kcal mol-1, which is much lower than that without catalyst (44.29 kcal mol-1). During the reaction, the H-Cl bond is preferentially activated through accepting the electrons transferred from the anion of TPPB, and then the C2H2 is activated to complete the addition reaction of H and Cl. Such unique preferential activation toward the H-Cl bond as well as the weak adsorption to the product VCM promotes the catalytic activity and the stability of the supported TPPB catalysts. The amount of carbon deposition on the 15% TPPB/SAC catalyst is as low as 2.99%, even after 300 h of reaction. The high activity and stability of the 15% TPPB/SAC catalyst indicate great promise for its application as a nonmetal catalyst for acetylene hydrochlorination.

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