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127-18-4

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127-18-4 Usage

General Description

1,1,2,2-Tetrachloroethylene, also known as perchloroethylene, is a colorless liquid with a sweet odor that is widely used as a solvent in dry cleaning and metal degreasing. It is also used in the production of other chemicals and as an intermediate in the synthesis of fluorocarbons. However, 1,1,2,2-Tetrachloroethylene is considered a hazardous chemical due to its potential for causing harm to human health and the environment. It is a known carcinogen and can cause damage to the liver, kidneys, and central nervous system with prolonged exposure. It is also toxic to aquatic organisms and can persist in the environment for long periods of time, making it a potential threat to ecosystems. Therefore, proper handling and disposal of 1,1,2,2-Tetrachloroethylene is necessary to minimize its impact on human health and the environment.

Check Digit Verification of cas no

The CAS Registry Mumber 127-18-4 includes 6 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 3 digits, 1,2 and 7 respectively; the second part has 2 digits, 1 and 8 respectively.
Calculate Digit Verification of CAS Registry Number 127-18:
(5*1)+(4*2)+(3*7)+(2*1)+(1*8)=44
44 % 10 = 4
So 127-18-4 is a valid CAS Registry Number.

127-18-4 Well-known Company Product Price

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  • Alfa Aesar

  • (32437)  Tetrachloroethylene, Ultrapure, Spectrophotometric Grade, 99+%   

  • 127-18-4

  • 1L

  • 926.0CNY

  • Detail
  • Alfa Aesar

  • (32437)  Tetrachloroethylene, Ultrapure, Spectrophotometric Grade, 99+%   

  • 127-18-4

  • 4L

  • 2732.0CNY

  • Detail
  • Alfa Aesar

  • (32437)  Tetrachloroethylene, Ultrapure, Spectrophotometric Grade, 99+%   

  • 127-18-4

  • *4x1L

  • 3288.0CNY

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  • Alfa Aesar

  • (B20089)  Tetrachloroethylene, 99%   

  • 127-18-4

  • 100ml

  • 142.0CNY

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  • Alfa Aesar

  • (B20089)  Tetrachloroethylene, 99%   

  • 127-18-4

  • 500ml

  • 310.0CNY

  • Detail
  • Alfa Aesar

  • (B20089)  Tetrachloroethylene, 99%   

  • 127-18-4

  • 2500ml

  • 456.0CNY

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  • Supelco

  • (48609)  Tetrachloroethylenesolution  certified reference material, 200 μg/mL in methanol

  • 127-18-4

  • 000000000000048609

  • 207.09CNY

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  • Supelco

  • (40083)  Tetrachloroethylenesolution  certified reference material, 5000 μg/mL in methanol

  • 127-18-4

  • 000000000000040083

  • 400.14CNY

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  • Sigma-Aldrich

  • (15889)  DensityStandard1623kg/m3  H&D Fitzgerald Ltd. Quality

  • 127-18-4

  • 15889-10ML-F

  • 2,341.17CNY

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127-18-4SDS

SAFETY DATA SHEETS

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

Version: 1.0

Creation Date: Aug 12, 2017

Revision Date: Aug 12, 2017

1.Identification

1.1 GHS Product identifier

Product name tetrachloroethene

1.2 Other means of identification

Product number -
Other names TETRACHLORO ETHYLENE

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:127-18-4 SDS

127-18-4Synthetic route

N-(2,2,2-trichloroethylidene)benzenesulfonamide
55596-11-7

N-(2,2,2-trichloroethylidene)benzenesulfonamide

complex of sulfur dioxide with dimethylamine
21326-49-8

complex of sulfur dioxide with dimethylamine

A

1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

B

chloroform
67-66-3

chloroform

C

N,N-dimethyl-N′-(phenylsulfonyl)formimidamide
13707-43-2

N,N-dimethyl-N′-(phenylsulfonyl)formimidamide

Conditions
ConditionsYield
In dichloromethane at 20℃; for 24h;A n/a
B n/a
C 98%
N-(2,2,2-trichloroethylidene)benzenesulfonamide
55596-11-7

N-(2,2,2-trichloroethylidene)benzenesulfonamide

diethylamine
109-89-7

diethylamine

A

1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

B

chloroform
67-66-3

chloroform

C

N1,N1-diethyl-N2-phenylsulfonylformamidine
29665-24-5

N1,N1-diethyl-N2-phenylsulfonylformamidine

Conditions
ConditionsYield
In dichloromethane at 0℃; for 24h;A n/a
B n/a
C 98%
hexachloroethane
67-72-1

hexachloroethane

1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

Conditions
ConditionsYield
In tetrachloromethane at 300℃; for 0.000555556h; Temperature; Flow reactor; Pyrolysis;97%
at 600℃;
With pyrographite at 700℃;
Hexachlorobutadiene
87-68-3

Hexachlorobutadiene

1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

Conditions
ConditionsYield
With aluminum (III) chloride; chlorine at 280 - 750℃; Temperature;95%
N-(2,2,2-trichloroethylidene)benzenesulfonamide
55596-11-7

N-(2,2,2-trichloroethylidene)benzenesulfonamide

dimethyl amine
124-40-3

dimethyl amine

A

1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

B

chloroform
67-66-3

chloroform

C

N,N-dimethyl-N′-(phenylsulfonyl)formimidamide
13707-43-2

N,N-dimethyl-N′-(phenylsulfonyl)formimidamide

Conditions
ConditionsYield
In dichloromethane at 20℃; for 24h;A n/a
B n/a
C 92%
N-(2,2,2-trichloroethylidene)benzenesulfonamide
55596-11-7

N-(2,2,2-trichloroethylidene)benzenesulfonamide

complex of sulfur dioxide with dimethylamine
21326-49-8

complex of sulfur dioxide with dimethylamine

A

1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

B

chloroform
67-66-3

chloroform

C

N-Phenylsulfonyl-N,N'-dimethylformamidine hydrochloride

N-Phenylsulfonyl-N,N'-dimethylformamidine hydrochloride

Conditions
ConditionsYield
In Trichloroethylene at 20℃; for 24h;A n/a
B n/a
C 89%
octachloro-cyclobutane
7294-43-1

octachloro-cyclobutane

A

1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

B

Hexachlorobutadiene
87-68-3

Hexachlorobutadiene

C

hexachlorocyclobutene
6130-82-1

hexachlorocyclobutene

Conditions
ConditionsYield
at 506℃; Product distribution;A 0.3%
B 86%
C 1.2%
tetrachloromethane
56-23-5

tetrachloromethane

A

1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

B

methane
34557-54-5

methane

C

chloroform
67-66-3

chloroform

D

carbon monoxide
201230-82-2

carbon monoxide

Conditions
ConditionsYield
With iron(II,III) oxide; sodium chloride at 25℃; pH=8.9; Kinetics;A 0.01%
B 1%
C 5.2%
D 82%
With hydroxysulfate green rust In water at 20℃; for 575h; pH=7.6; Product distribution;
pentachloroethane
76-01-7

pentachloroethane

1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

Conditions
ConditionsYield
With methyl diethylphosphinate at 150℃; for 10h;75%
With chlorine at 379.84℃; Gas phase; chemoselective reaction;33.8%
With nickel dichloride at 330℃;
1,1,2,2-tetrachloroethane
79-34-5

1,1,2,2-tetrachloroethane

A

1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

B

Trichloroethylene
79-01-6

Trichloroethylene

Conditions
ConditionsYield
With hydrogenchloride; oxygen at 379.84℃; for 18h;A 20.8%
B 64.3%
With CuCl2/KCl/attapulgite; chlorine at 379.84℃; Gas phase; chemoselective reaction;A 16.6%
B 45%
1,1,2,2-tetrachloroethane
79-34-5

1,1,2,2-tetrachloroethane

A

1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

B

Trichloroethylene
79-01-6

Trichloroethylene

C

pentachloroethane
76-01-7

pentachloroethane

Conditions
ConditionsYield
With hydrogenchloride; oxygen at 379.84℃;A 20.8%
B 64.3%
C 6.1%
N,N-Dichlorobenzenesulfonamide
473-29-0

N,N-Dichlorobenzenesulfonamide

1,2-Dichloroethylene
540-59-0

1,2-Dichloroethylene

A

benzenesulfonamide
98-10-2

benzenesulfonamide

B

1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

C

Trichloroethylene
79-01-6

Trichloroethylene

D

N-(2,2,2-trichloroethylidene)benzenesulfonamide
55596-11-7

N-(2,2,2-trichloroethylidene)benzenesulfonamide

E

N-(2,2-dichloroethylidene)benzenesulfonamide
113791-97-2

N-(2,2-dichloroethylidene)benzenesulfonamide

F

N-{2,2-dichloro-1-[(phenylsulfonyl)amino]ethyl}benzenesulfonamide
79054-58-3

N-{2,2-dichloro-1-[(phenylsulfonyl)amino]ethyl}benzenesulfonamide

Conditions
ConditionsYield
at 55℃; for 22h; Product distribution; other time, other temperature, other initiator;A n/a
B n/a
C n/a
D n/a
E n/a
F 54.1%
N,N-Dichlorobenzenesulfonamide
473-29-0

N,N-Dichlorobenzenesulfonamide

1,2-Dichloroethylene
540-59-0

1,2-Dichloroethylene

A

1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

B

Trichloroethylene
79-01-6

Trichloroethylene

C

N-(2,2,2-trichloroethylidene)benzenesulfonamide
55596-11-7

N-(2,2,2-trichloroethylidene)benzenesulfonamide

D

N-(2,2-dichloroethylidene)benzenesulfonamide
113791-97-2

N-(2,2-dichloroethylidene)benzenesulfonamide

E

N-{2,2-dichloro-1-[(phenylsulfonyl)amino]ethyl}benzenesulfonamide
79054-58-3

N-{2,2-dichloro-1-[(phenylsulfonyl)amino]ethyl}benzenesulfonamide

F

1,1,2,2-tetrachloroethane
79-34-5

1,1,2,2-tetrachloroethane

Conditions
ConditionsYield
at 55℃; for 22h; Product distribution; other time, other temperature, other initiator;A n/a
B n/a
C n/a
D n/a
E 54.1%
F n/a
hexachloroethane
67-72-1

hexachloroethane

Ce(3+)*3C4H14NSi2(1-)*2C4H8O

Ce(3+)*3C4H14NSi2(1-)*2C4H8O

A

1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

B

tetramethyldisilazane

tetramethyldisilazane

Conditions
ConditionsYield
In toluene for 18h; Reagent/catalyst; Solvent; Time; Inert atmosphere;A n/a
B 45%
1,2-Dichloroethylene
540-59-0

1,2-Dichloroethylene

N,N-dichloro-4-chlorobenzenesulfonamide
17260-65-0

N,N-dichloro-4-chlorobenzenesulfonamide

A

1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

B

4-Chlorobenzenesulfonamide
98-64-6

4-Chlorobenzenesulfonamide

C

N-(2,2,2-trichloroethylidene)-4-chlorobenzenesulfonamide
81924-15-4

N-(2,2,2-trichloroethylidene)-4-chlorobenzenesulfonamide

D

N-(2,2-dichloroethylidene)-p-chlorobenzenesulfonamide
113791-98-3

N-(2,2-dichloroethylidene)-p-chlorobenzenesulfonamide

E

N-<2,2-dichloro-1-(N-p-chlorobenzenesulfonamido)ethyl>-p-chlorobenzenesulfonamide
113792-01-1

N-<2,2-dichloro-1-(N-p-chlorobenzenesulfonamido)ethyl>-p-chlorobenzenesulfonamide

F

1,1,2,2-tetrachloroethane
79-34-5

1,1,2,2-tetrachloroethane

Conditions
ConditionsYield
at 55℃; for 22h; Product distribution; other time, other temperature, other initiator;A n/a
B n/a
C n/a
D n/a
E 40.4%
F n/a
(2,2-dichloro-vinyl)-trimethyl-silane
18163-67-2

(2,2-dichloro-vinyl)-trimethyl-silane

A

1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

B

Trichloroethylene
79-01-6

Trichloroethylene

C

Trimethyl-(1,2,2,2-tetrachloro-ethyl)-silane

Trimethyl-(1,2,2,2-tetrachloro-ethyl)-silane

D

Chloromethyl-dimethyl-(1,2,2,2-tetrachloro-ethyl)-silane

Chloromethyl-dimethyl-(1,2,2,2-tetrachloro-ethyl)-silane

Conditions
ConditionsYield
With chlorine for 3h; Further byproducts given;A 1%
B 5%
C 30%
D 33%
With chlorine for 3h; Further byproducts given;A 1%
B 7%
C 30%
D 33%
Trichloroethylene
79-01-6

Trichloroethylene

A

1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

B

pentachloroethane
76-01-7

pentachloroethane

Conditions
ConditionsYield
With chlorine at 379.84℃; Reagent/catalyst; Temperature;A 8.1%
B 11.2%
tetrachloromethane
56-23-5

tetrachloromethane

A

1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

B

hexachloroethane
67-72-1

hexachloroethane

Conditions
ConditionsYield
at 580℃; for 0.00433333h; Rate constant; Mechanism; several condition investigated;A 10.18%
B 2.51%
at 394.5 - 445.3℃; under 83.3 - 161.6 Torr; Kinetics; Equilibrium constant; Thermodynamic data; eq. const. at 696.6 K; ΔH at 298 K;
at 600 - 1500℃;
pentacarbonyl(methoxyphenylmethylene)tungsten(0)
37823-96-4

pentacarbonyl(methoxyphenylmethylene)tungsten(0)

A

1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

B

methylene chloride
74-87-3

methylene chloride

C

dichloromethane
75-09-2

dichloromethane

D

chloroform
67-66-3

chloroform

Conditions
ConditionsYield
In tetrachloromethane byproducts: HCl, Cl2; further products; N2; stirred; gas-chromy., MAS; elem. anal.;A 6.8%
B 2%
C 0.2%
D 3.6%
piperidine
110-89-4

piperidine

tetrachloromethane
56-23-5

tetrachloromethane

pentachloroethane
76-01-7

pentachloroethane

1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

Conditions
ConditionsYield
at 20℃;
tetrachloromethane
56-23-5

tetrachloromethane

Isobutane
75-28-5

Isobutane

hexachloroethane
67-72-1

hexachloroethane

A

1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

B

tertiary butyl chloride
507-20-0

tertiary butyl chloride

Conditions
ConditionsYield
at 140℃;
tetrachloromethane
56-23-5

tetrachloromethane

1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

Conditions
ConditionsYield
Beim Durchleiten durch ein rotgluehendes Rohr;
at 1300 - 1400℃;
With hydrogen
tetrachloromethane
56-23-5

tetrachloromethane

A

1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

B

hexachlorobenzene
118-74-1

hexachlorobenzene

Conditions
ConditionsYield
at 700℃;
propene
187737-37-7

propene

1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

Conditions
ConditionsYield
With tetrachloromethane; chlorine at 800℃;
diethyl ether
60-29-7

diethyl ether

hexachloroethane
67-72-1

hexachloroethane

ethylmagnesium bromide
925-90-6

ethylmagnesium bromide

A

1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

B

1,1,1,2-tetrachoroethane
630-20-6

1,1,1,2-tetrachoroethane

C

pentachloroethane
76-01-7

pentachloroethane

D

1,1,2,2-tetrachloroethane
79-34-5

1,1,2,2-tetrachloroethane

diethyl ether
60-29-7

diethyl ether

hexachloroethane
67-72-1

hexachloroethane

sodium ethanolate
141-52-6

sodium ethanolate

1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

Conditions
ConditionsYield
at 140℃;
diethyl ether
60-29-7

diethyl ether

hexachloroethane
67-72-1

hexachloroethane

phenylmagnesium bromide

phenylmagnesium bromide

A

1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

B

1,1,1,2-tetrachoroethane
630-20-6

1,1,1,2-tetrachoroethane

C

pentachloroethane
76-01-7

pentachloroethane

D

1,1,2,2-tetrachloroethane
79-34-5

1,1,2,2-tetrachloroethane

1,1-dichloroethane
75-34-3

1,1-dichloroethane

1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

Conditions
ConditionsYield
With chlorine; pyrographite at 450℃;
pentachloropropionyl chloride
812-25-9

pentachloropropionyl chloride

A

1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

B

hexachloroethane
67-72-1

hexachloroethane

Conditions
ConditionsYield
With aluminium trichloride at 60℃;
1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

hypofluorous acid trifluoromethyl ester
373-91-1

hypofluorous acid trifluoromethyl ester

1,1,2,2-tetrachloro-1-fluoro-2-trifluoromethoxyethane
136649-69-9

1,1,2,2-tetrachloro-1-fluoro-2-trifluoromethoxyethane

Conditions
ConditionsYield
at 40.6℃;99.5%
at 160 - 195℃; under 750.075 Torr; for 31h;84.3%
1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

5-methyl-1H-2-benzothiopyran-1-one
681141-90-2

5-methyl-1H-2-benzothiopyran-1-one

2aα,8bα-1,1,2,2-tetrachloro-2,2a-dihydro-8-methyl-1H-cyclobuta[c][2]benzothiopyran-4-one

2aα,8bα-1,1,2,2-tetrachloro-2,2a-dihydro-8-methyl-1H-cyclobuta[c][2]benzothiopyran-4-one

Conditions
ConditionsYield
In acetonitrile for 12h; Irradiation;97%
1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

Pd(CN(2,6-(2,6-(i-Pr)2C6H3)2C6H3))2
1182649-23-5

Pd(CN(2,6-(2,6-(i-Pr)2C6H3)2C6H3))2

Pd(η2-C2Cl4)(CN(2,6-(2,6-(i-Pr)2C6H3)2C6H3))2

Pd(η2-C2Cl4)(CN(2,6-(2,6-(i-Pr)2C6H3)2C6H3))2

Conditions
ConditionsYield
In toluene; pentane for 0.25h; Inert atmosphere; Schlenk technique; Glovebox;97%
1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

A

1,1,1-trifluoro-2,2-dichloroethane
306-83-2

1,1,1-trifluoro-2,2-dichloroethane

B

1,1,2-trichloro-2,2-difluoroethane
354-21-2

1,1,2-trichloro-2,2-difluoroethane

C

freon-121
354-14-3

freon-121

D

1,1,1,2-tetrafluoro-2-chloroethane
2837-89-0

1,1,1,2-tetrafluoro-2-chloroethane

Conditions
ConditionsYield
With hydrogen fluoride; antimony(III) fluoride; antimony pentafluoride at 125 - 139℃; under 16351.6 - 18376.8 Torr; for 3.7h;A 92.4%
B 0.9%
C 0.01%
D 0.4%
With hydrogen fluoride; antimony(III) fluoride; antimony pentafluoride at 122 - 140℃; under 17926.8 - 20252 Torr; for 3.6h;A 89.8%
B 0.3%
C 0.08%
D 3.1%
With hydrogen fluoride; antimony(III) fluoride; antimony pentafluoride at 124 - 140℃; under 18001.8 - 19201.9 Torr; for 3.1h;A 87.2%
B 1.1%
C 0.01%
D 0.5%
1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

copper hydroxide
20427-59-2

copper hydroxide

Trimethylenediamine
109-76-2

Trimethylenediamine

Cu2(C10H16N4Cl4)(H2O)4(4+)*4Cl(1-)*8H2O = [Cu2(C10H16N4Cl4)(H2O)4]Cl4*8H2O

Cu2(C10H16N4Cl4)(H2O)4(4+)*4Cl(1-)*8H2O = [Cu2(C10H16N4Cl4)(H2O)4]Cl4*8H2O

Conditions
ConditionsYield
In water; butan-1-ol refluxing in butanol (10 h), extraction (water); pptn. from aq. phase (concn., cooling); elem. anal.;92%
1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

(E)-tert-butyldimethyl[3-(tributylstannyl)prop-2-enyloxy]silane
90838-72-5, 110410-38-3, 134435-95-3, 86633-16-1, 81925-28-2, 86646-19-7

(E)-tert-butyldimethyl[3-(tributylstannyl)prop-2-enyloxy]silane

(6E,10E)-8,9-Bis((E)-3-((tert-butyldimethylsilyl)oxy)prop-1-en-1-yl)-2,2,3,3,14,14,15,15-octamethyl-4,13-dioxa-3,14-disilahexadeca-6,8,10-triene
1638292-74-6

(6E,10E)-8,9-Bis((E)-3-((tert-butyldimethylsilyl)oxy)prop-1-en-1-yl)-2,2,3,3,14,14,15,15-octamethyl-4,13-dioxa-3,14-disilahexadeca-6,8,10-triene

Conditions
ConditionsYield
With palladium diacetate; XPhos at 60℃; Stille Cross Coupling; Inert atmosphere;90%
With palladium diacetate; XPhos at 60℃; Stille Cross Coupling; Inert atmosphere;90%
1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

tributyl[(E)-2-trimethylsilylethenyl]stannane
58207-97-9

tributyl[(E)-2-trimethylsilylethenyl]stannane

((1E,5E)-3,4-bis((E)-2-(trimethylsilyl)vinyl)hexa-1,3,5-triene-1,6-diyl)bis(trimethylsilane)
1638178-58-1

((1E,5E)-3,4-bis((E)-2-(trimethylsilyl)vinyl)hexa-1,3,5-triene-1,6-diyl)bis(trimethylsilane)

Conditions
ConditionsYield
With palladium diacetate; XPhos at 60℃; Stille Cross Coupling; Inert atmosphere;89%
With palladium diacetate; XPhos at 60℃; Stille Cross Coupling; Inert atmosphere;89%
1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

sodium isopropanethiolate
20607-43-6

sodium isopropanethiolate

tetrakis-isopropylsulfanyl-ethene
39137-72-9

tetrakis-isopropylsulfanyl-ethene

Conditions
ConditionsYield
In N,N,N,N,N,N-hexamethylphosphoric triamide for 1h; Ambient temperature;85%
1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

hypofluorous acid trifluoromethyl ester
373-91-1

hypofluorous acid trifluoromethyl ester

A

CFC-112a
76-12-0

CFC-112a

B

dichloro-fluoro-acetyl chloride
354-17-6

dichloro-fluoro-acetyl chloride

C

1,1,2,2-tetrachloro-1-fluoro-2-trifluoromethoxyethane
136649-69-9

1,1,2,2-tetrachloro-1-fluoro-2-trifluoromethoxyethane

D

Trichloroacetyl chloride
76-02-8

Trichloroacetyl chloride

E

Dichloro-trifluoromethoxy-acetyl chloride

Dichloro-trifluoromethoxy-acetyl chloride

F

COCl2

COCl2

Conditions
ConditionsYield
With oxygen at 40.9℃; under 420.8 Torr; for 1.97833h; Product distribution; Mechanism; Rate constant; var. of partial pressure, temp.;A n/a
B n/a
C n/a
D 85%
E n/a
F n/a
1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

fac-tricarbonyl(bis(diphenylphosphino)ethane)(η1-methyldithiobenzoate)tungsten
118050-71-8, 118050-81-0

fac-tricarbonyl(bis(diphenylphosphino)ethane)(η1-methyldithiobenzoate)tungsten

mer-tricarbonyl(bis(diphenylphosphino)ethane)(η2-methyldithiobenzoate)tungsten * tetrachloroethene

mer-tricarbonyl(bis(diphenylphosphino)ethane)(η2-methyldithiobenzoate)tungsten * tetrachloroethene

Conditions
ConditionsYield
In tetrahydrofuran isomerization in THF within about 48 h;; concn.; pptn. with tetrachloroethene; elem. anal.;;85%
1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

tetrabutyl-ammonium chloride
1112-67-0

tetrabutyl-ammonium chloride

C2Cl12Si4(2-)*2C16H36N(1+)

C2Cl12Si4(2-)*2C16H36N(1+)

Conditions
ConditionsYield
With hexachlorodisilane In dichloromethane at -10 - 20℃; for 12h; Inert atmosphere;85%
1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

Octanethiol
111-88-6

Octanethiol

A

Octyl-<1.2.2-trichlor-vinyl>-sulfid
36061-42-4

Octyl-<1.2.2-trichlor-vinyl>-sulfid

B

1-((E)-1,2-Dichloro-2-octylsulfanyl-vinylsulfanyl)-octane
130920-00-2

1-((E)-1,2-Dichloro-2-octylsulfanyl-vinylsulfanyl)-octane

Conditions
ConditionsYield
With potassium hydroxide In ethanol; N,N-dimethyl-formamide at 60 - 70℃;A n/a
B 83%
1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

diamantane-3-spiro-3'-diazirine
105522-49-4

diamantane-3-spiro-3'-diazirine

3-chlorodiamantane
30651-01-5

3-chlorodiamantane

Conditions
ConditionsYield
Irradiation;83%
1,1,2,2-tetrachloroethylene
127-18-4

1,1,2,2-tetrachloroethylene

A

1,1,1-trifluoro-2,2-dichloroethane
306-83-2

1,1,1-trifluoro-2,2-dichloroethane

B

1,1,2-trichloro-2,2-difluoroethane
354-21-2

1,1,2-trichloro-2,2-difluoroethane

C

1,1,1,2-tetrafluoro-2-chloroethane
2837-89-0

1,1,1,2-tetrafluoro-2-chloroethane

Conditions
ConditionsYield
With hydrogen fluoride; antimony(III) fluoride; antimony pentafluoride at 129 - 143℃; under 17626.8 - 19502 Torr; for 4.1h;A 80.5%
B 0.3%
C 5.1%
With hydrogen fluoride; antimony pentafluoride at 135 - 143℃; under 18751.9 Torr; for 2.7h;A 26%
B 0.6%
C 25.8%

127-18-4Relevant articles and documents

A novel method of CCl4 disposal by disproportionation with CH4 over Pt on various supports

Bae, Jong Wook,Lee, Jae Sung,Lee, Kyung Hee,Lee, Byeongno,Yang, Duck Joo

, p. 264 - 265 (2001)

In disproportionation of CCl4 with CH4 into CH3Cl and CHCl3, platinum supported on SrCO3, SiO2, MgO and MgAl2O4 showed stable activity and high selectivities around 700 K, providing a novel disposal method of ozone-depleting CCl4.

Influence of amine buffers on carbon tetrachloride reductive dechlorination by the iron oxide magnetite

Danielsen, Karlin M.,Gland, John L.,Hayes, Kim F.

, p. 756 - 763 (2005)

The influence of amine buffers on carbon tetrachloride (CCI4) reductive dechlorination by the iron oxide magnetite (FeIIFe II2O4) was examined in batch reactors. A baseline was provided by monitoring the reaction in a magnetite suspension containing NaCl as a background electrolyte at pH 8.9. The baseline reaction rate constant was measured at 7.1 × 10-5 ± 6.3 × 10-6 L m-2 h-1. Carbon monoxide (CO) was the dominant reaction product at 82% followed by chloroform (CHCI3) at 5.2%. In the presence of 0.01 M tris-(deuteroxymethyl) aminomethane (TRIS d), the reaction rate constant nearly tripled to 2.1 × 10 -4 ± 6.5 × 10-6 L m-2 h -1 but only increased the CHCI3 yield to 11% and did not cause any statistically significant changes to the CO yield. Reactions in the presence of triethylammonium (TEAd) (0.01 M) increased the rate constant by 17% to 8.6 × 10-5 ± 8.1 × 10 -6 L m-2 h-1 but only increased the CHCI 3 yield to 8.8% while leaving the CO yield unchanged. The same concentration of N,N,N′,N′-tetraethylethylenediamine (TEEN) increased the reaction rate constant by 18% to 8.7 × 10-5 ± 4.8 × 10-6 L m-2 h-1 but enhanced the CHCI3 yield to 34% at the expense of the CO yield that dropped to 35%. Previous work has shown that CHCI3 can be generated either through hydrogen abstraction by a trichloromethyl radical ( .CCI3), or through proton abstraction by the trichlorocarbanion (-:CCI3). These two possible hydrogenolysis pathways were examined in the presence of deuterated buffers. Deuterium tracking experiments revealed that proton abstraction by the trichlorocarbanion was the dominant hydrogenolysis mechanism in the magnetite-buffered TRISd and TEAd systems. The only buffer that had minimal influence on both the reaction rate and product distribution was TEAd. These results indicate that buffers should be prescreened and demonstrated to have minimal impact on reaction rates and product distributions prior to use. Alternatively, it may be preferable, to utilize the buffer capacity of the solids to avoid organic buffer interactions entirely.

Dynamic behaviour of chlorofluoroethanes at fluorinated chromia aerogels and fluorinated zinc(II) or magnesium(II) doped chromia aerogels

Bozorgzadeh, Hamid,Kemnitz, Erhard,Nickkho-Amiry, Mahmood,Skapin, Toma?,Winfield, John M.

, p. 83 - 92 (2003)

The preparation and characterisation of two series of fluorinated chromia aerogel materials, lightly doped with zinc(II) or magnesium(II), are described. They behave as heterogeneous catalysts for transformations of 1,1,2-trichlorotrifluoroethane under HF

Chlorination and dehydrochlorination reactions relevant to the manufacture of trichloroethene and tetrachloroethene: Part 1. Reaction pathways

Sutherland, Iain W.,Hamilton, Neil G.,Dudman, Christopher C.,Jones, Peter,Lennon, David,Winfield, John M.

, p. 1 - 11 (2011)

Factors which affect the selectivity of the chlorination of 1,2-dichloroethane and the associated dehydrochlorination reactions have been examined using approximate thermodynamic calculations, equilibrium measurements, and a continuous flow micro-reactor. There is a balance between surface and gas-phase chemistry within the system. Heterogeneous catalysis is not necessary to effect dehydrochlorination of 1,1,2,2-tetrachloroethane to trichloroethene but an attapulgite-supported copper(II) chloride catalyst favours formation of pentachloroethane and its dehydrochlorination product, tetrachloroethene. The latter is the thermodynamic minimum of the system. Below 473 K and with long reaction times (2 h, batch reactor), radical chlorination to form pentachloroethane is dominant. Above 573 K and under flow conditions, free radical dehydrochlorination to form trichloroethene becomes dominant. Heterogeneous chlorination under flow conditions provides a route to pentachloroethane and thence tetrachloroethene. High conversions favour the formation of oligomeric products.

Bidinosti, D. R.,Porter, R. F.

, p. 3737 - 3743 (1961)

A homoleptic tetravalent cerium silylamide

Crozier, Alan R.,Bienfait, Andre M.,Maichle-Moessmer, Caecilia,Toernroos, Karl W.,Anwander, Reiner

, p. 87 - 89 (2013)

Treatment of Ce[N(SiHMe2)2]3(thf) 2 with the chlorinating agents PhICl2, Ph3CCl or C2Cl6 gave the homoleptic Ce(iv) silylamide Ce[N(SiHMe2)2]4. When performed in the absence of donating (solvent) molecules, the trivalent cluster Ce 5[N(SiHMe2)2]8Cl7 was isolated.

Sidebottom, H. W.,Tedder, J. M.,Walton, J. C.

, p. 755 - 762 (1969)

-

Boeeseken,Schimmel

, p. 112,125 (1913)

-

Effects of AgI, AuIII, and CuII on the reductive dechlorination of carbon tetrachloride by green rust

O'Loughlin, Edward J.,Kemner, Kenneth M.,Burris, David R.

, p. 2905 - 2912 (2003)

Green rusts (GRs), mixed iron(II)/iron(III) hydroxide minerals found in many suboxic environments, have been shown to reduce a range of organic and inorganic contaminants, including several chlorinated hydrocarbons. Many studies have demonstrated the catalytic activity of transition metal species in the reduction of chlorinated hydrocarbons, suggesting the potential for enhanced reduction by GR in the presence of an appropriate transition metal catalyst. Reductive dechlorination of carbon tetrachloride (CT) was examined in aqueous suspensions of GR amended with AgI, AuIII, or CuII. The CT reduction rates were greatly increased for systems amended with CuII, AuIII, and AgI (listed in order of increasing rates) relative to GR alone. Observed intermediates and products included chloroform, dichloromethane, chloromethane, methane, acetylene, ethene, ethane, carbon monoxide, tetrachloroethene, and various nonchlorinated C3 and C4 compounds. Product distributions for the reductive dechlorination of CT were highly dependent on the transition metal used. A reaction pathway scheme is proposed in which CT is reduced primarily to methane and other nonchlorinated end products, largely through a series of one-electron reductions forming radicals and carbenes/carbenoids. Recently, X-ray absorption fine structure analysis of aqueous GR suspensions amended with AgI, AuIII, or CuII showed that the metals were reduced to their zerovalent forms. A possible mechanism for CT reduction is the formation of a galvanic couple involving the zerovalent metal and GR, with reduction of CT occurring on the surface of the metal and GR serving as the bulk electron source. The enhanced reduction of CT by GR suspensions amended with AgI, AuIII, or CuII may prove useful in the development of improved materials for remediation of chlorinated organic contaminants.

MULTIPHOTON IONIZATION OF CHLOROMETHANES WITH 193-NM EXCIMER LASER RADIATION IN ARGON MATRICES

Machara, Nicholas P.,Ault, Bruce S.

, p. 1908 - 1913 (1989)

The 193-nm output of an excimer laser has been coupled with the matrix isolation technique to demonstrate the feasibility of multiphoton ionization of matrix-isolated species.CCl4, CHCl3, and CH2Cl2 were, in turn, deposited in argon and (in some cases) nitrogen matrices and irradiated for between 5 min and 3 h.For CCl4 and CH2Cl2, the major product was the parent cation or species derived directly thereform, while more varied species, including the CHCL3(-) anion, were observed in the CHCl3 studies.In addition, neutral fragments were observed in a manner similar to previous resonance radiation and proton-beam radiolysis studies.Irradiation of the sample mixture during the deposition process led to increased product yield, as well as additional products for some of the systems.The laser irradiation time, power, and repetition rate were varied over a wide range, and a relative insensitivity to these parameters was noted.

Maynard

, p. 112 (1963)

Experimental study on the thermal oxidation of 1,3-hexachlorobutadiene at 500-1100°C

Baillet,Fadli,Sawerysyn

, p. 1261 - 1273 (1996)

Thermal degradation processes of 1,3-hexachlorobutadiene (C4Cl6) have been studied using a tubular flow reactor at 1 atm over the temperature range 500-1100°C for residence times of 2 seconds. Kinetic studies were performed with mixtures of 1000 ppmV of C4Cl6 in air. Overall Arrhenius parameters for the destruction of C4Cl6 were determined between 700 and 850°C. About 30 molecular halogenated products from C1 to C8 formed by pyrolysis or oxidation of 1,3-hexachlorobutadiene over the investigated temperature range were identified. Concentration profiles of major products (CO2, Cl2, CO, COCl2, C2Cl4, CCl4) and some minor products (C3Cl4O, C4Cl4O, C6Cl6, C3Cl4 and C3Cl6) have been measured as a function of temperature. Phosgene is the major chlorinated intermediate product. Detection of some aromatics such as hexachlorobenzene and octachlorostyrene show the importance of the molecular growth pathways in the chemical mechanism. Reaction pathways of main products are proposed and corresponding reaction enthalpies are estimated.

-

West,Schmerling

, p. 3525 (1950)

-

Transformation of chlorinated aliphatic compounds by ferruginous smectite

Cervini-Silva,Larson,Wu,Stucki

, p. 805 - 809 (2001)

A series of chlorinated aliphatic compounds (RCI, including carbon tetrachloride (PCM), 1,1,1-trichloroethane (TCA), 1,1,2,2-tetrachloroethane (TeCA), pentachloroethane (PCA), hexachloroethane (HCA), trichloroethene (TCE), tetrachloroethene (PCE), trichloronitromethane (chloropicrin, CP), and trichloroacetonitrile (TCAN)) was reacted with ferruginuous smectite (sample SWa-1 from The Source Clays Repository), SWa, in aqueous suspension under anoxic conditions. Compounds highly polarizable or sharing substituents that facilitate charge delocalization adsorbed faster by reduced (SWa-R) than by unaltered (SWa-U) clay, indicating stronger dipole-dipole interactions between the substituents and the clay surface and/or hydrating water molecules. The reduction of the clay accelerated RCI adsorption up to 100-fold. Incubations with SWa-R promoted RCI reduction (CP, TCAN) or dehydrochlorination (TeCA and PCA). The reduction of structural Fe catalyzes the transformation of RCI via Bronsted and Lewis-basic promoted pathways. This study indicates that oxidation state of the structural Fe in SWa greatly alters surface chemistry and has a large impact on clay-organic interactions.

-

Weiser,Wightman

, p. 415 (1919)

-

Kinetics and mechanism of the sonolytic degradation of CCL4: Intermediates and byproducts

Hua, Inez,Hoffmann, Michael R.

, p. 864 - 871 (1996)

The sonolytic degradation of aqueous carbon tetrachloride is investigated at a sound frequency of 20 kHz and 135 W (112.5 W cm-2) of power. The observed first-order degradation rate constant in an Ar-saturated solution is 3.3 x 10-3 s-1 when the initial CCh concentration, [CCl4](i), is 1.95 x 10-4 mol L-1 and increases slightly to 3.9 x 10-3 s-1 when [CCl4](i) = 1.95 x 10-5 mol L-1. Low concentrations (10-8-10-7 mol L-1) of the organic byproducts, hexachloroethane and tetrachloroethylene, are detected, as well as the inorganic products chloride ion and hypochlorous acid. The chlorine mass balance after sonolysis is determined to be >70%. The reactive intermediate, dichlorocarbene, is identified and quantified by means of trapping with 2,3-dimethyl-2-butene. The presence of ozone in the sonicated solution does not significantly effect the rate of degradation of carbon tetrachloride; however, O3 inhibits the accumulation of hexachloroethane and tetrachloroethylene. Ultrasonic irradiation of an aqueous mixture of p-nitrophenol (p-NP) and carbon tetrachloride results in the acceleration of the sonochemical degradation of p-NP. The sonolytic rate of degradation of p-NP appears to be enhanced by the presence of hypochlorous acid, which results from the sonolysis of CCl4.

-

Carpenter,W.

, p. 3082 - 3084 (1965)

-

-

McBee,Hass,Pierson

, p. 181,185 (1941)

-

Skell, P. S.,Harris, R. F.

, p. 5807 - 5808 (1965)

Kinetics and Thermochemistry of the Cl(2PJ) + C2Cl4 Association Reaction

Nicovich, J. M.,Wang, S.,McKee, M. L.,Wine, P. H.

, p. 680 - 688 (1996)

A laser flash photolysis-resonance fluorescence technique has been employed to study the kinetics of the Cl(2PJ) + C2Cl4 association reaction as a function of temperature (231-390 K) and pressure (3-700 Torr) in nitrogen buffer gas.The reaction is found to be in the falloff regime between third and second order over the range of conditions investigated, although the second-order limit is approached at the highest pressures and lowest temperatures.At temperatures below 300 K, the association reaction is found to be irreversible on the experimental time scale of ca. 20 ms.The kinetic data at T 0298 = -18.1 +/- 1.3 kcal mol-1, ΔH00 = -17.6 +/- 1.3 kcal mol-1, and ΔS0298 = -27.7 +/- 3.0 cal mol-1 K-1.In conjunction with the well-known heats of formation of Cl(2PJ) and C2Cl4, the above ΔH values lead to the following heats of formation for C2Cl5 at 298 and 0 K: ΔH0f,298 = 8.0 +/- 1.3 kcal mol-1 and ΔH0f,0 = 8.1 +/- 1.5 kcal mol-1.The kinetic and thermochemical parameters reported above are compared with other reported values, and the significance of reported association rate coefficients for understanding tropospheric chlorine chemistry is discussed.

Natural organic matter as reductant for chlorinated aliphatic pollutants

Kappler, Andreas,Haderlein, Stefan B.

, p. 2714 - 2719 (2003)

Humic acids (HA) are ubiquitous redox-active compounds of natural aquatic and soil systems. Here we studied the potential of HA as reductants for chlorinated aliphatic pollutants. To avoid artifacts potentially involved when studying chemically reduced HA, we prepared electrochemically reduced soil, aquatic and synthetic HA, and anthrahydroquinone-2,6-disulfonic acid (AHQDS), a model compound for hydroquinone moieties in HA. Both reduced HA and AHQDS reduced hexachloroethane (HCE) at appreciable rates. Some reduction of HCE by HA, however, occurred even before electrochemical reduction of the humic acids. This indicates that a small fraction of reduced moieties in HA persists at oxic conditions for some time. The initial reaction followed pseudo-first-order reaction kinetics, and tetrachloroethylene was the only halogenated product. The relatively small variations in carbonnormalized rate constants, kDOC, found indicate that despite inherent variations in concentration, accessibility, and reactivity of redox-active groups in HA of various origins their overall dechlorination activity is fairly constant. However, HCE transformation rate constants and reducing capacities of different HA did not correlate. Rate constants normalized to both carbon content and reducing capacity of HA clearly indicate that reduced functional groups in different HA exhibit different reactivities. Our results together with the factthat reduced HA can be formed by a variety of microbiological and chemical processes suggest that HA could play a significant role as reductants in the reductive transformation of subsurface contaminants and that such a process could potentially be enhanced at contaminated sites by addition of reducible natural organic matter.

Role of copper species in chlorination and condensation reactions of acetylene

Wehrmeier, Andreas,Lenoir, Dieter,Sidhu, Sukh S.,Taylor, Philip H.,Rubey, Wayne A.,Kettrup, Antonious,Dellinger, Barry

, p. 2741 - 2748 (1998)

We examined the thermally induced acetylene chlorination and condensation reactions on different types of copper salt impregnated surfaces. The System for Thermal Diagnostic Studies provided a powerful tool to study these reactions under defined reaction conditions, which were related to typical conditions in postcombustion incineration processes. Experiments were conducted with acetylene or acetylene/HCl mixtures in a quarts reactor filled with a borosilicate foam of known pore size at temperatures between 150 and 500 °C. Borosilicate was also used as the catalytic support for gas-solid reactions of acetylene and acetylene/HCl mixtures with CuCl2 and CuO. Reaction products were trapped in-line and analyzed by GC/MS. It was shown that borosilicate is not able to catalyze acetylene condensation reactions. CuCl2-impregnated borosilicate was a highly effective catalyst for acetylene chlorination/condensation reactions at temperatures above 150 °C. The same behavior was found for CuO- impregnated borosilicate in the presence of HCl. However, temperatures above 300 °C were required for this catalytic system. Mainly perchlorinated C-2 to C-8 hydrocarbons were trapped as reaction products in the gas phase. Maximum yields for acetylene chlorination/condensation reactions in each related catalytic system were found at temperatures between 300 and 400 °C. Results of the surface-catalyzed acetylene chlorination and condensation reactions were summarized in a global mechanism. A ligand transfer oxidative chlorination of acetylene with CuCl2 was proposed to be the initiation of acetylene with CuCl2 was proposed to be the initiating step. Chlorinated acetylene then condenses to higher molecular weight compounds, catalyzed by CuCl in metallacyclization reactions. We examined the thermally induced acetylene chlorination and condensation reactions on different types of copper salt impregnated surfaces. The System for Thermal Diagnostic Studies provided a powerful tool to study these reactions under defined reaction conditions, which were related to typical conditions in postcombustion incineration processes. Experiments were conducted with acetylene or acetylene/HCl mixtures in a quartz reactor filled with a borosilicate foam of known pore size at temperatures between 150 and 500 °C. Borosilicate was also used as the catalytic support for gas-solid reactions of acetylene and acetylene/HCl mixtures with CuCl2 and CuO. Reaction products were trapped in-line and analyzed by GC/MS. It was shown that borosilicate is not able to catalyze acetylene condensation reactions. CuCl2-impregnated borosilicate was a highly effective catalyst for acetylene chlorination/condensation reactions at temperatures above 150 °C. The same behavior was found for CuO-impregnated borosilicate in the presence of HCl. However, temperatures above 300 °C were required for this catalytic system. Mainly perchlorinated C-2 to C-8 hydrocarbons were trapped as reaction products in the gas phase. Maximum yields for acetylene chlorination/condensation reactions in each related catalytic system were found at temperatures between 300 and 400 °C. Results of the surface-catalyzed acetylene chlorination and condensation reactions were summarized in a global mechanism. A ligand transfer oxidative chlorination of acetylene with CuCl2 was proposed to be the initiating step. Chlorinated acetylene then condenses to higher molecular weight compounds, catalyzed by CuCl in metallacyclization reactions.

Kinetics of the transformation of halogenated aliphatic compounds by iron sulfide

Hayes,Butler

, p. 422 - 429 (2000)

The transformation of nine halogenated aliphatic compounds, i.e., pentachloroethane (PCA), 1,1,2,2- and 1,1,1,2-tetrachloroethanes (1122-TeCA and 1112-TeCA), 1,1,1- and 1,1,2-trichloroethanes (111-TCA and 112-TCA), 1,1- and 1,2-dichloroethanes (11-DCA and 12-DCA), carbon tetrachloride (CT), and tribromomethane (TBM), by 10 g/L FeS at pH 8.3 was investigated in batch experiments. 11-DCA, 12-DCA, and 112-TCA showed no significant transformation by FeS over ~ 120 days, but the other compounds were transformed with half-lives of hours to days. PCA and 1122-TeCA underwent dehydrohalogenation faster than FeS-mediated reductive dehalogenation reactions. The remaining compounds for which considerable transformation was observed underwent FeS-mediated reactions more rapidly than hydrolysis or dehydrohalogenation. For 1112-TeCA, the dihaloelimination product, i.e., 1,1-dichlroethylene, was the only reaction product observed. For 111-TCA, CT, and TBM, hydrogenolysis products were the only products detected, even though their mass recoveries were significantly 100%. Two simple log-linear correlations between rate constants and either one-electron reduction potentials or homolytic bond dissociation enthalpies were developed, with determination coefficients of 0.48 and 0.82, respectively. These results were consistent with a rate-limiting step involving homolytic bond dissociation. However, neither correlation precisely characterized the reactivity of all the compounds, indicating distinctions among the mechanisms for reductive dehalogenation of the compounds by FeS or the influence of additional molecular or thermodynamic parameters on rate constants.

Pyrolysis of hexachloroethane in the gas phase: computer aided kinetic study

Huybrechts,Theys,Van Mele

, p. 755 - 761 (1996)

The pyrolysis of C2Cl6 has been studied between 652 and 735 K at pressures ranging from 19 to 50 torr. The observed total pressure- and Cl2 pressure-time curves show S-shapes with an induction period depending on temperature and pressure. Further, the total pressure goes through a maximum to finally reach a lower constant value. These curves are explained in terms of a recently proposed reaction model using a parameter optimization computer program.

-

Benkeser,R.A.,Smith,W.E.

, p. 5307 - 5309 (1968)

-

Three-dimensionally ordered macroporous Cr2O3?CeO2: High-performance catalysts for the oxidative removal of trichloroethylene

Zhang, Xing,Liu, Yuxi,Deng, Jiguang,Zhao, Xingtian,Zhang, Kunfeng,Yang, Jun,Han, Zhuo,Jiang, Xiyun,Dai, Hongxing

, p. 200 - 209 (2019/02/14)

Three-dimensionally ordered macroporous (3DOM) CeO2, 3DOM Cr2O3, 3DOM xCr2O3?CeO2 (x (the weight percentage of Cr2O3) = 3.5, 5.5, and 8.0 wt%), and 5.5 wt% Cr2O3/3DOM CeO2 samples were prepared using the polymethyl methacrylate (PMMA)-templating and incipient wetness impregnation methods, respectively. A number of techniques were used to characterize physicochemical properties of the materials, and their catalytic activities were evaluated for the oxidation of trichloroethylene (TCE). These samples possessed a good-quality 3DOM structure and a surface area of 35?47 m2/g. The 3DOM 5.5Cr2O3?CeO2 sample performed the best (the temperature at TCE conversion = 90% = 255 °C at a space velocity of 20,000 mL/(g h)). Effects of water vapor and carbon dioxide on activity of the 5.5Cr2O3?CeO2 sample were also examined. It is observed that partial deactivation induced by H2O introduction of the 5.5Cr2O3?CeO2 sample was reversible, while that induced by CO2 addition was irreversible. Based on the activity data and characterization results, it is concluded that the good catalytic activity and thermal stability of 3DOM 5.5Cr2O3?CeO2 was associated with its high adsorbed oxygen species concentration, good low-temperature reducibility, and strong interaction between Cr2O3 and CeO2. We believe that the 3DOM 5.5Cr2O3?CeO2 catalyst is promising in the application for oxidative removal of chlorinated volatile organic compounds.

METHOD OF PRODUCING VINYL CHLORIDE

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Paragraph 0031; 0038; 0039, (2020/01/27)

A method of producing vinyl chloride is provided in the present invention. The method includes the following steps. First, 1,2-dichloroethane (EDC) is introduced into a reactor, and a residence time of the EDC in an ionic liquid catalyst is 5 seconds to 100 seconds, so as to perform a catalytic cleavage reaction. The ionic liquid catalyst is in a liquid phase. The ionic liquid catalyst includes tributylalkyl phosphonium halide, and the alkyl includes an alkyl group having 3 to 16 carbon atoms.

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