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  • 67-66-3 Structure
  • Basic information

    1. Product Name: Chloroform
    2. Synonyms: Methyl trichloride;Freon 20;R 20 (refrigerant);Trichloormethaan;Methane trichloride;Cloroformio;Chloroforme;Triclorometano;NCI-C02686;Methenyl trichloride;Methane, trichloro-;Trichlormethan;Trichloroform;Trichloromethane;Methane,trichloro-;Formyl trichloride;Industrial Chloroform;Chloroform, Reagent;Chloroform, Spectrophotometric Grade;
    3. CAS NO:67-66-3
    4. Molecular Formula: CHCl3
    5. Molecular Weight: 119.37764
    6. EINECS: 200-663-8
    7. Product Categories: N/A
    8. Mol File: 67-66-3.mol
    9. Article Data: 284
  • Chemical Properties

    1. Melting Point: -63℃
    2. Boiling Point: 61.2 °C at 760 mmHg
    3. Flash Point: 60.5-61.5°C
    4. Appearance: Colorless liquid
    5. Density: 1.5 g/cm3
    6. Vapor Density: 4.12 (vs air)
    7. Vapor Pressure: 213.3 hPa at 20°C
    8. Refractive Index: 1.444-1.445
    9. Storage Temp.: N/A
    10. Solubility: N/A
    11. Water Solubility: 8 g/L (20℃)
    12. CAS DataBase Reference: Chloroform(CAS DataBase Reference)
    13. NIST Chemistry Reference: Chloroform(67-66-3)
    14. EPA Substance Registry System: Chloroform(67-66-3)
  • Safety Data

    1. Hazard Codes:  Xn:Harmful;
    2. Statements: R22:; R38:; R40:; R48/20/22:;
    3. Safety Statements: S36/37:;
    4. WGK Germany:
    5. RTECS:
    6. HazardClass: N/A
    7. PackingGroup: III
    8. Hazardous Substances Data: 67-66-3(Hazardous Substances Data)

67-66-3 Usage

Chemical Description

Chloroform is a colorless, heavy, sweet-smelling liquid used as a solvent and in medicine.

Chemical Description

Chloroform is a colorless, sweet-smelling liquid that was once used as an anesthetic.

Chemical Description

Chloroform, ethyl acetate, and petroleum ether are solvents used for extraction and purification.

Chemical Description

Chloroform is a colorless liquid used as a solvent.

Chemical Description

Chloroform is a colorless, sweet-smelling organic compound that is commonly used as a solvent.

Chemical Description

Chloroform, ethanol, and acetic acid are solvents used in the reactions.

Chemical Description

Chloroform is a colorless liquid that was once used as an anesthetic but is now primarily used as a solvent.

Chemical Description

Chloroform is a solvent used in the purification of some compounds, while methanol is a common solvent used in organic chemistry.

Chemical Description

Chloroform and n-hexane are organic solvents used in the study.

Chemical Description

Chloroform is a colorless, sweet-smelling organic compound with the formula CHCl3.

Chemical Description

Chloroform is a colorless, heavy, sweet-smelling liquid used as a solvent and in the production of refrigerants.

Chemical Description

Chloroform is a colorless liquid used as a solvent in various chemical reactions.

Chemical Description

Chloroform is a colorless, sweet-smelling organic compound used as a solvent.

Chemical Description

Chloroform and bromoform are specific examples of haloforms.

Chemical Description

Chloroform is a colorless, sweet-smelling organic compound.

Chemical Description

Chloroform and chloroform-d are solvents, while the other chemicals are aromatic amines or related compounds.

Chemical Description

Chloroform is a colorless, heavy, sweet-smelling liquid used as a solvent.

Chemical Description

Chloroform is used in the TLC solvent system, and aqueous hydrochloric acid is used to form the HC1 salt of the final product.

Chemical Description

Chloroform is a colorless, sweet-smelling organic compound that is used as a solvent.

Chemical Description

Chloroform was used to dilute the mixture, while sodium bisulfite was used as a washing solution.

Check Digit Verification of cas no

The CAS Registry Mumber 67-66-3 includes 5 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 2 digits, 6 and 7 respectively; the second part has 2 digits, 6 and 6 respectively.
Calculate Digit Verification of CAS Registry Number 67-66:
(4*6)+(3*7)+(2*6)+(1*6)=63
63 % 10 = 3
So 67-66-3 is a valid CAS Registry Number.

67-66-3SDS

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 chloroform

1.2 Other means of identification

Product number -
Other names HCC20

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:67-66-3 SDS

67-66-3Synthetic route

Bromotrichloromethane
75-62-7

Bromotrichloromethane

N,N,N',N'-Tetraisopropyl-P-methylphosphonous diamide
110838-39-6

N,N,N',N'-Tetraisopropyl-P-methylphosphonous diamide

A

chloroform
67-66-3

chloroform

B

P-(bromomethyl)-N,N,N',N'-tetraisopropylphosphonous diamide
124862-13-1

P-(bromomethyl)-N,N,N',N'-tetraisopropylphosphonous diamide

Conditions
ConditionsYield
In diethyl ether for 0.25h; Ambient temperature;A 100%
B 45%
In diethyl ether for 0.25h; Ambient temperature; or P-ethyl-N,N,N',N'-tetraisopropylphosphonous diamide;A n/a
B 45%
Bromotrichloromethane
75-62-7

Bromotrichloromethane

P-ethyl-N,N,N',N'-tetraisopropylphosphonous diamide
122691-44-5

P-ethyl-N,N,N',N'-tetraisopropylphosphonous diamide

A

chloroform
67-66-3

chloroform

B

P-(1-bromoethyl)-N,N,N',N'-tetraisopropylphosphonous diamide
124862-16-4

P-(1-bromoethyl)-N,N,N',N'-tetraisopropylphosphonous diamide

Conditions
ConditionsYield
In diethyl ether for 0.25h; Ambient temperature;A 100%
B 45%
1,1,1,3,3,3-hexachloro-propan-2-one
116-16-5

1,1,1,3,3,3-hexachloro-propan-2-one

isopropylamine
75-31-0

isopropylamine

A

chloroform
67-66-3

chloroform

B

N-Isopropyl-2,2,2-trichloroacetamide
23144-67-4

N-Isopropyl-2,2,2-trichloroacetamide

Conditions
ConditionsYield
In hexaneA n/a
B 100%
pentachloroacetone
1768-31-6

pentachloroacetone

isopropylamine
75-31-0

isopropylamine

A

chloroform
67-66-3

chloroform

B

N-Isopropyl-2,2-dichloroacetamide
39063-24-6

N-Isopropyl-2,2-dichloroacetamide

Conditions
ConditionsYield
In hexane for 0.5h;A n/a
B 100%
1,1,1,3,3,3-hexachloro-propan-2-one
116-16-5

1,1,1,3,3,3-hexachloro-propan-2-one

N-butylamine
109-73-9

N-butylamine

A

chloroform
67-66-3

chloroform

B

trichloro-acetic acid butylamide
31464-96-7

trichloro-acetic acid butylamide

Conditions
ConditionsYield
In hexaneA n/a
B 100%
pentachloroacetone
1768-31-6

pentachloroacetone

methylamine
74-89-5

methylamine

A

chloroform
67-66-3

chloroform

B

2,2-dichloro-N-methylacetamide
5345-73-3

2,2-dichloro-N-methylacetamide

Conditions
ConditionsYield
In hexane Heating;A n/a
B 100%
1,1,1,3,3-pentachlorobutanone
64697-39-8

1,1,1,3,3-pentachlorobutanone

methylamine
74-89-5

methylamine

A

chloroform
67-66-3

chloroform

B

2,2-Dichloro-N-methyl-propionamide
83703-95-1

2,2-Dichloro-N-methyl-propionamide

Conditions
ConditionsYield
In hexane Heating;A n/a
B 100%
tris(cyclopentadienyl)zirconiumhydride

tris(cyclopentadienyl)zirconiumhydride

A

(π-C5H5)3ZrCl

(π-C5H5)3ZrCl

B

chloroform
67-66-3

chloroform

Conditions
ConditionsYield
With tetrachloromethane In toluene under Ar; excess of CCl4 added to suspension of Cp3ZrH in PhMe; stirredat about 20°C for 5 h; stored overnight at 0-5°C; sepd. by pressure; dried in an Ar stream; elem. anal.;A 99%
B 89%
1,1,1,3,3,3-hexachloro-propan-2-one
116-16-5

1,1,1,3,3,3-hexachloro-propan-2-one

2,2,3,3-tetrafluoropropanol
76-37-9

2,2,3,3-tetrafluoropropanol

A

chloroform
67-66-3

chloroform

B

bis(2,2,3,3-tetrafluoropropyl) carbonate
1422-70-4

bis(2,2,3,3-tetrafluoropropyl) carbonate

Conditions
ConditionsYield
With potassium fluoride; zirconium(IV) oxide at 140℃; for 10h; Product distribution / selectivity; pressure tight reactor;A 99%
B 99%
1,1,1,3,3,3-hexachloro-propan-2-one
116-16-5

1,1,1,3,3,3-hexachloro-propan-2-one

2,2,2-trifluoroethanol
75-89-8

2,2,2-trifluoroethanol

A

chloroform
67-66-3

chloroform

B

bis(2,2,2-trifluoroethyl) carbonate
1513-87-7

bis(2,2,2-trifluoroethyl) carbonate

Conditions
ConditionsYield
With potassium fluoride; zirconium(IV) oxide at 140℃; for 10h; pressure tight reactor;A 99%
B 99%
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%
Schwartz's reagent

Schwartz's reagent

A

zirconocene dichloride
1291-32-3

zirconocene dichloride

B

chloroform
67-66-3

chloroform

Conditions
ConditionsYield
With tetrachloromethane In toluene under Ar; elem. anal.;A 98%
B 62%
Trichlormethansulfinsaeureanilid
42521-52-8

Trichlormethansulfinsaeureanilid

A

chloroform
67-66-3

chloroform

B

N-phenylsulfinylamine
222851-56-1

N-phenylsulfinylamine

Conditions
ConditionsYield
With potassium carbonate In acetonitrile Ambient temperature;A n/a
B 97.2%
1,1,1,3,3,3-hexachloro-propan-2-one
116-16-5

1,1,1,3,3,3-hexachloro-propan-2-one

1-amino-2-propene
107-11-9

1-amino-2-propene

A

chloroform
67-66-3

chloroform

B

2,2,2-trichloro-N-(2-propenyl)acetamide
39089-56-0

2,2,2-trichloro-N-(2-propenyl)acetamide

Conditions
ConditionsYield
In hexane for 0.5h;A n/a
B 97%
1,1,1,3,3,3-hexachloro-propan-2-one
116-16-5

1,1,1,3,3,3-hexachloro-propan-2-one

ethanolamine
141-43-5

ethanolamine

A

chloroform
67-66-3

chloroform

B

2,2,2-trichloro-N-(2-hydroxyethyl)acetamide
35234-31-2

2,2,2-trichloro-N-(2-hydroxyethyl)acetamide

Conditions
ConditionsYield
In hexane for 0.5h;A n/a
B 96%
tetrachloromethane
56-23-5

tetrachloromethane

di-n-propylmercury
628-85-3

di-n-propylmercury

A

mercury(I) chloride

mercury(I) chloride

B

1-Chloropropane
540-54-5

1-Chloropropane

C

chloroform
67-66-3

chloroform

D

n-propylmercury(II) chloride
2440-40-6

n-propylmercury(II) chloride

E

mercury

mercury

Conditions
ConditionsYield
In neat (no solvent) 150°C, 60 h; further products;A <1
B 96%
C >99
D 5%
E 95%
pentachloroacetone
1768-31-6

pentachloroacetone

ethanolamine
141-43-5

ethanolamine

A

chloroform
67-66-3

chloroform

B

2,2-dichloro-N-(2-hydroxyethyl)acetamide
6419-44-9

2,2-dichloro-N-(2-hydroxyethyl)acetamide

Conditions
ConditionsYield
In hexane for 0.5h;A n/a
B 95.4%
1,1,1,3,3,3-hexachloro-propan-2-one
116-16-5

1,1,1,3,3,3-hexachloro-propan-2-one

methylamine
74-89-5

methylamine

A

chloroform
67-66-3

chloroform

B

N-methyltrichloroacetamide
23170-77-6

N-methyltrichloroacetamide

Conditions
ConditionsYield
In hexane Heating;A n/a
B 95.2%
tetrachloromethane
56-23-5

tetrachloromethane

oxygen
80937-33-3

oxygen

diisopropylmercury
1071-39-2

diisopropylmercury

A

propane
74-98-6

propane

B

isopropyl chloride
75-29-6

isopropyl chloride

C

chloroform
67-66-3

chloroform

D

isopropylmercury(II) chloride
30615-19-1

isopropylmercury(II) chloride

E

mercury

mercury

Conditions
ConditionsYield
In neat (no solvent) 20°C, 96 h; further products;A 4%
B 48%
C 30%
D 95%
E 5%
pentachloroacetone
1768-31-6

pentachloroacetone

N-butylamine
109-73-9

N-butylamine

A

chloroform
67-66-3

chloroform

B

2,2-dichloro-N-butylacetamide
5345-74-4

2,2-dichloro-N-butylacetamide

Conditions
ConditionsYield
In hexaneA n/a
B 93.9%
1,1,1,3,3-pentachlorobutanone
64697-39-8

1,1,1,3,3-pentachlorobutanone

ethanolamine
141-43-5

ethanolamine

A

chloroform
67-66-3

chloroform

B

2,2-Dichloro-N-(2-hydroxy-ethyl)-propionamide
83704-00-1

2,2-Dichloro-N-(2-hydroxy-ethyl)-propionamide

Conditions
ConditionsYield
In hexane for 0.5h;A n/a
B 93.5%
1,1,1,3,3-pentachlorobutanone
64697-39-8

1,1,1,3,3-pentachlorobutanone

1-amino-2-propene
107-11-9

1-amino-2-propene

A

chloroform
67-66-3

chloroform

B

N-Allyl-2,2-dichloro-propionamide
83703-99-5

N-Allyl-2,2-dichloro-propionamide

Conditions
ConditionsYield
In hexane for 0.5h;A n/a
B 93.5%
1,1,1,3,3,3-hexachloro-propan-2-one
116-16-5

1,1,1,3,3,3-hexachloro-propan-2-one

ethanol
64-17-5

ethanol

2,2,3,3-tetrafluoropropanol
76-37-9

2,2,3,3-tetrafluoropropanol

A

chloroform
67-66-3

chloroform

B

2,2,3,3-Tetrafluor-propyl-propionat
2062-06-8

2,2,3,3-Tetrafluor-propyl-propionat

Conditions
ConditionsYield
Stage #1: 1,1,1,3,3,3-hexachloro-propan-2-one; ethanol With potassium fluoride at 30℃; for 1h; pressure tight reactor;
Stage #2: 2,2,3,3-tetrafluoropropanol at 100℃;
A 93%
B 74%
pentachloroacetone
1768-31-6

pentachloroacetone

1-pentanamine
110-58-7

1-pentanamine

A

chloroform
67-66-3

chloroform

B

N-Pentyl-2,2-dichloroacetamide
83703-97-3

N-Pentyl-2,2-dichloroacetamide

Conditions
ConditionsYield
In hexane for 0.5h;A n/a
B 92%
1,1,1,3,3-pentachlorobutanone
64697-39-8

1,1,1,3,3-pentachlorobutanone

1-pentanamine
110-58-7

1-pentanamine

A

chloroform
67-66-3

chloroform

B

2,2-Dichloro-N-pentyl-propionamide
83703-98-4

2,2-Dichloro-N-pentyl-propionamide

Conditions
ConditionsYield
In hexane for 0.5h;A n/a
B 92%
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%
1-Decanol
112-30-1

1-Decanol

pentachloroacetone
1768-31-6

pentachloroacetone

A

chloroform
67-66-3

chloroform

B

decyl 2,2-dichloroacetate
83005-00-9

decyl 2,2-dichloroacetate

Conditions
ConditionsYield
With triethylamine Heating;A n/a
B 91.4%
tetrachloromethane
56-23-5

tetrachloromethane

diisopropylmercury
1071-39-2

diisopropylmercury

A

mercury(I) chloride

mercury(I) chloride

B

isopropyl chloride
75-29-6

isopropyl chloride

C

chloroform
67-66-3

chloroform

D

isopropylmercury(II) chloride
30615-19-1

isopropylmercury(II) chloride

E

mercury

mercury

Conditions
ConditionsYield
In neat (no solvent) 130°C, 10 h; further products;A 3%
B 51%
C 50%
D 91%
E 3%
styrene
292638-84-7

styrene

chloroform
67-66-3

chloroform

1,1-dichloro-2-phenylcyclopropane
2415-80-7

1,1-dichloro-2-phenylcyclopropane

Conditions
ConditionsYield
With potassium hydroxide; tetrabutylammomium bromide; 1,3,5-trimethyl-benzene In dichloromethane at 40℃; for 6h;100%
With PEG-supported tetrakis ammonium salt In dichloromethane at 25℃; for 0.5h;98%
With tetrabutylammomium bromide; sodium hydroxide In dichloromethane at 20℃; for 0.0833333h;96%
chloroform
67-66-3

chloroform

cyclohexene
110-83-8

cyclohexene

7,7-dichloro-bicyclo[4.1.0]heptane
823-69-8

7,7-dichloro-bicyclo[4.1.0]heptane

Conditions
ConditionsYield
With sodium hydroxide; Sucrose-ethyleneoxide adducts In chloroform at 20℃; for 2h; Product distribution; further catalysts: PEG, DB18K6; further objects of study: phase-transfer catalysis;;100%
With sodium hydroxide; Sucrose-ethyleneoxide adducts In chloroform at 20℃; for 2h; Product distribution; further catalysts: PEG, DB18K6;100%
With potassium hydroxide; 18-crown-6 ether In dichloromethane at 40℃; for 6h;98%
styrene
292638-84-7

styrene

chloroform
67-66-3

chloroform

1,1,3-trichloro-3-phenylpropane
42956-39-8

1,1,3-trichloro-3-phenylpropane

Conditions
ConditionsYield
With Grubbs catalyst first generation at 65℃; for 2h;100%
Grubbs catalyst first generation at 65 - 80℃; Kharasch addition;99%
With N2[(RuCl2)2(1,3,5-iPr3C6H3)(tricyclohexylphosphine]2 In toluene at 40℃; for 48h;93%
chloroform
67-66-3

chloroform

Bis(2,4,6-tri-tert-butylphenyl)diphosphen
83466-54-0, 93602-74-5, 79073-99-7

Bis(2,4,6-tri-tert-butylphenyl)diphosphen

1,2-bis(2,4,6-tri-tert-butylphenyl)3,3-dichloro diphosphirane
111888-01-8, 126976-48-5

1,2-bis(2,4,6-tri-tert-butylphenyl)3,3-dichloro diphosphirane

Conditions
ConditionsYield
With potassium hydroxide In hexane at 15℃; for 2h; sonication;100%
With potassium tert-butylate
chloroform
67-66-3

chloroform

3,3-Diethyl-6,7-dimethoxy-1-phenyl-3,4-dihydro-isoquinoline
132067-80-2

3,3-Diethyl-6,7-dimethoxy-1-phenyl-3,4-dihydro-isoquinoline

6,7-Dimethoxy-8bphenyl-1,1-dichloro-3,3-diethyl-1,3,4,8b-tetrahydroazirino<2,1-a>isoquinoline
132067-87-9

6,7-Dimethoxy-8bphenyl-1,1-dichloro-3,3-diethyl-1,3,4,8b-tetrahydroazirino<2,1-a>isoquinoline

Conditions
ConditionsYield
With sodium hydroxide; N-benzyl-N,N,N-triethylammonium chloride In hexane 1) 3 h, 12 deg C 2) 1 h, 20 deg C;100%
chloroform
67-66-3

chloroform

N,N-dimethyl-formamide
68-12-2, 33513-42-7

N,N-dimethyl-formamide

Vilsmeier-Haack reagent

Vilsmeier-Haack reagent

Conditions
ConditionsYield
With trichlorophosphate at 20℃; for 0.5h;100%
chloroform
67-66-3

chloroform

4-Ethoxyaniline
156-43-4

4-Ethoxyaniline

acetone
67-64-1

acetone

α-p-phenetidino-isobutyric acid p-phenetidide
74262-33-2

α-p-phenetidino-isobutyric acid p-phenetidide

Conditions
ConditionsYield
With sodium hydroxide; N-benzyl-N,N,N-triethylammonium chloride In dichloromethane at 5℃;100%
chloroform
67-66-3

chloroform

(3aR,6aR)-4-Dichloromethylene-2,2-dimethyl-tetrahydro-furo[3,4-d][1,3]dioxole

(3aR,6aR)-4-Dichloromethylene-2,2-dimethyl-tetrahydro-furo[3,4-d][1,3]dioxole

(3'aR)-2,2,3,3-tetrachloro-2',2'-dimethyl-(3'ar,6'ac)-tetrahydrospiro(cyclopropane-1,4'-furo[3,4-d][1,3]dioxolane)

(3'aR)-2,2,3,3-tetrachloro-2',2'-dimethyl-(3'ar,6'ac)-tetrahydrospiro(cyclopropane-1,4'-furo[3,4-d][1,3]dioxolane)

Conditions
ConditionsYield
With sodium hydroxide; N-benzyl-N,N,N-triethylammonium chloride 0 deg C, 30 min; RT, 2.5 h;100%
chloroform
67-66-3

chloroform

palmatine chloride
10605-02-4

palmatine chloride

8-trichloromethyl-7,8-dihydropalmatine
50932-23-5

8-trichloromethyl-7,8-dihydropalmatine

Conditions
ConditionsYield
With ammonium hydroxide for 24h;100%
With ammonium hydroxide at 20℃; for 24h;74.9%
chloroform
67-66-3

chloroform

(Z)-2,3-Diphenyl-acrylic acid 2-[(E)-phenyliminomethyl]-phenyl ester

(Z)-2,3-Diphenyl-acrylic acid 2-[(E)-phenyliminomethyl]-phenyl ester

2-(1,2-diphenylvinyl)-2,5-epoxy-4-phenyl-2,3,4,5-tetrahydro-1,4-benzoxazepin-3-one

2-(1,2-diphenylvinyl)-2,5-epoxy-4-phenyl-2,3,4,5-tetrahydro-1,4-benzoxazepin-3-one

Conditions
ConditionsYield
With potassium hydroxide; N-benzyl-N,N,N-triethylammonium chloride at 20℃;100%
C20H29NO3
618103-13-2

C20H29NO3

chloroform
67-66-3

chloroform

C21H29Cl2NO3
618103-14-3

C21H29Cl2NO3

Conditions
ConditionsYield
With sodium hydroxide; tetrabutylammomium bromide In water for 16h;100%
4-(3-acetoxy-4-methylanilino)-7-benzyloxy-6-methoxyquinazoline

4-(3-acetoxy-4-methylanilino)-7-benzyloxy-6-methoxyquinazoline

chloroform
67-66-3

chloroform

4-(3-acetoxy-4-methylanilino)-7-hydroxy-6-methoxyquinazoline

4-(3-acetoxy-4-methylanilino)-7-hydroxy-6-methoxyquinazoline

Conditions
ConditionsYield
palladium In methanol; N,N-dimethyl-formamide100%
palladium In methanol; N,N-dimethyl-formamide100%
4-(3-acetoxy-4-methylanilino)-7-benzyloxy-6-methoxyquinazoline hydrochloride

4-(3-acetoxy-4-methylanilino)-7-benzyloxy-6-methoxyquinazoline hydrochloride

chloroform
67-66-3

chloroform

4-(3-acetoxy-4-methylanilino)-7-hydroxy-6-methoxyquinazoline hydrochloride

4-(3-acetoxy-4-methylanilino)-7-hydroxy-6-methoxyquinazoline hydrochloride

Conditions
ConditionsYield
palladium In methanol; N,N-dimethyl-formamide100%
1-hydroxytetraphenylcyclopentadienyl(tetraphenyl-2,4-cyclopentadien-1-one)-μ-hydrotetracarbonyldiruthenium(II)

1-hydroxytetraphenylcyclopentadienyl(tetraphenyl-2,4-cyclopentadien-1-one)-μ-hydrotetracarbonyldiruthenium(II)

chloroform
67-66-3

chloroform

dicarbonylchloro(η5-1-hydroxy-2,3,4,5-tetraphenylcyclopentadienyl)ruthenium(II)

dicarbonylchloro(η5-1-hydroxy-2,3,4,5-tetraphenylcyclopentadienyl)ruthenium(II)

Conditions
ConditionsYield
In ethanol; chloroform byproducts: CH2Cl2, CH3CHO; (Ar); using Schlenk techniques; dissolving of ((Ph4C4CO)2H)Ru2(CO)4(H) in degassed CHCl3 and C2H5OH; closing of flask, stirring at 90°C for 7 h; removal of solvent under high vac., elem .anal.;100%
chloroform
67-66-3

chloroform

bis[tris-(3,5-dimethyl-2-oxidobenzyl-κO)ammonium]zirconium(IV)

bis[tris-(3,5-dimethyl-2-oxidobenzyl-κO)ammonium]zirconium(IV)

bis[tris-(3,5-dimethyl-2-oxidobenzyl-κO)ammonium]zirconium(IV) chloroform disolvate

bis[tris-(3,5-dimethyl-2-oxidobenzyl-κO)ammonium]zirconium(IV) chloroform disolvate

Conditions
ConditionsYield
In chloroform Zr((CH3)2C6H2(O)CH2)3NH) dissolved in dry CHCl3 in air; recrystd.; elem. anal.; detd. by XRD;100%
chloroform
67-66-3

chloroform

bis(η2-ethene)[η5-(8-quinolyl)cyclopentadienyl]iridium(I)
866488-88-2

bis(η2-ethene)[η5-(8-quinolyl)cyclopentadienyl]iridium(I)

[η5-(8-quinolyl)cyclopentadienyl]dichloridoiridium(III)
1184999-49-2

[η5-(8-quinolyl)cyclopentadienyl]dichloridoiridium(III)

Conditions
ConditionsYield
In chloroform Irradiation (UV/VIS); under Ar atm.soln. Ir complex in CHCl3 was irradiated for 3 days with light 150-W Hg high-pressure lamp; solvent was evapd.;100%
chloroform
67-66-3

chloroform

(OC-6-54-C) μ-chlorido, μ-hydroxo, bis(cis-dicarbonyl, [2,2'-phenylene-4,5-(R,R)-pinenopyridine-κC,N]ruthenium(II))

(OC-6-54-C) μ-chlorido, μ-hydroxo, bis(cis-dicarbonyl, [2,2'-phenylene-4,5-(R,R)-pinenopyridine-κC,N]ruthenium(II))

bis(cis-dicarbonyl, μ-chlorido, [2,2'-phenylene-4,5-(R,R)-pinenopyridine-κC,N]ruthenium(II))*CH2Cl2

bis(cis-dicarbonyl, μ-chlorido, [2,2'-phenylene-4,5-(R,R)-pinenopyridine-κC,N]ruthenium(II))*CH2Cl2

Conditions
ConditionsYield
In chloroform 80°C, 48 h;100%
1,4,7-trithiacyclononane
6573-11-1

1,4,7-trithiacyclononane

di-μ-chlorobis(azobenzene-2C,N)dipalladium(II)

di-μ-chlorobis(azobenzene-2C,N)dipalladium(II)

chloroform
67-66-3

chloroform

acetone
67-64-1

acetone

[Pd(C6H4N=NC6H5)(1,4,7-trithiacyclononane)][Pd(C6H4N=NC6H5)(Cl2)]*CHCl3

[Pd(C6H4N=NC6H5)(1,4,7-trithiacyclononane)][Pd(C6H4N=NC6H5)(Cl2)]*CHCl3

Conditions
ConditionsYield
In dichloromethane byproducts: AgCl; under N2 or Ar using Schlenk app.; CH2Cl2 added to solid mixt. of (Pd(C6H4NNC6H5)Cl)2 (0.20 mol) and 1,4,7-trithiacyclononane (0.40 mol); stirred for 18 h; filtered; evapd. to dryness; extd. (MeOH); ext. filtered and evapd. to dryness; crystd. (CHCl3 and hexane) at room temp. for 3 d;100%
(tetrahydrothiophene)gold(I) chloride
39929-21-0

(tetrahydrothiophene)gold(I) chloride

chloroform
67-66-3

chloroform

(C5H5O2(OCH3)2CH2OCH3)5(PC6H5(CH2C5H5O2(OCH3)2)2)

(C5H5O2(OCH3)2CH2OCH3)5(PC6H5(CH2C5H5O2(OCH3)2)2)

P-chlorido-[6(A),6(B)-dideoxy-6(A),6(B)-[(R)-phenylphosphinidene]-2(A),2(B),2(C),2(D),2(E),2(F),2(G),3(A),3(B),3(C),3(D),3(E),3(G),6(C),6(D),6(E),6(F),6(G)-nonadeca-O-methyl-β-cyclodextrin]gold(I)*0.5CHCl3

P-chlorido-[6(A),6(B)-dideoxy-6(A),6(B)-[(R)-phenylphosphinidene]-2(A),2(B),2(C),2(D),2(E),2(F),2(G),3(A),3(B),3(C),3(D),3(E),3(G),6(C),6(D),6(E),6(F),6(G)-nonadeca-O-methyl-β-cyclodextrin]gold(I)*0.5CHCl3

Conditions
ConditionsYield
In dichloromethane (Schlenk, N2) to stirred soln. of phosphane in CH2Cl2 was added to a soln. of Au-complex in CH2Cl2, 30 min; evapd. to dryness, column chromy. (silica gel, CH2Cl2-CH3OH, 96:4, v/v);elem. anal.;100%
chloroform
67-66-3

chloroform

2,4,6-trimethylaniline
88-05-1

2,4,6-trimethylaniline

2-mesityl isocyanide
57116-96-8

2-mesityl isocyanide

Conditions
ConditionsYield
Stage #1: 2,4,6-trimethylaniline With 15-crown-5; sodium hydride In benzene at 40 - 50℃; for 0.25h;
Stage #2: chloroform In benzene at 40℃; for 1h;
100%
With benzyltriethylammonium chloride; sodium hydroxide In dichloromethane; water for 22h;53%
chloroform
67-66-3

chloroform

C81H64N4O4

C81H64N4O4

C85H64Cl8N4O4

C85H64Cl8N4O4

Conditions
ConditionsYield
With N-benzyl-N,N,N-triethylammonium chloride; sodium hydroxide In chloroform; water at 40 - 45℃; for 1h;100%
chloroform
67-66-3

chloroform

C63H53N3O3

C63H53N3O3

C66H53Cl6N3O3

C66H53Cl6N3O3

Conditions
ConditionsYield
With N-benzyl-N,N,N-triethylammonium chloride; sodium hydroxide In water at 40 - 45℃; for 1h;100%
chloroform
67-66-3

chloroform

C45H42N2O3

C45H42N2O3

C47H42Cl4N2O3

C47H42Cl4N2O3

Conditions
ConditionsYield
With N-benzyl-N,N,N-triethylammonium chloride; sodium hydroxide In water at 40 - 45℃;100%

67-66-3Relevant articles and documents

-

Teeple

, p. 536 (1904)

-

Gas-phase photooxidation of trichloroethylene on TiO2 and ZnO: Influence of trichloroethylene pressure, oxygen pressure, and the photocatalyst surface on the product distribution

Driessen,Goodman,Miller,Zaharias,Grassian

, p. 549 - 556 (1998)

Transmission Fourier transform infrared spectroscopy has been used to identify gas-phase and surface-bound products and intermediates formed during the gas-phase photooxidation of trichloroethylene (TCE) on TiO2 and ZnO. Several factors are found to influence the gas-phase product distribution for this reaction. On clean TiO2 and ZnO surfaces and at high TCE and O2 pressures, gas-phase CO, CO2, COCl2, CCl2HCOCl, CHCl3, C2HCl5, and HCl are produced, whereas at low TCE and O2 pressures, TCE is converted to gas-phase CO and CO2 only. In addition to TCE and O2 pressure, the product distribution of the photooxidation of TCE is strongly dependent upon the coverage of adsorbed species on the surface of the photocatalyst. It is shown here that the complete oxidation of adsorbed TCE can occur on clean photocatalytic surfaces whereas only partial oxidation of adsorbed TCE occurs on adsorbate-covered surfaces. The role of adsorbed surface products in TCE photooxidation is discussed.

KINETICS OF THE GAS-PHASE PHOTOCHLORINATION OF DICHLOROMETHANE IN A TUBULAR PHOTOREACTOR.

Sugawara,Suzuki,Ohashi

, p. 854 - 859 (1980)

The kinetics were studied with due consideration taken of the radial variation in light intensity across the reactor and with the proper selection of kinetic equations, including the recombination of dichloromethyl radicals as the dominant termination step. The dependence of the absorbed radiant energy on the chlorine concentration was well simulated by the use of the radial-light and line-source model. The predominance of the observed production rate of hydrogen chloride over that of chloroform was also reproduced well by the appropriately selected kinetic expressions, without any use of the long-chain approximation. This work is pertinent to photochemical reactor design.

Patinkin,Lieber

, p. 2778 (1950)

Mechanistic studies of the photocatalytic oxidation of trichloroethylene with visible-light-driven N-doped TiO2 photocatalysts

Joung, Soon-Kil,Amemiya, Takashi,Murabayashi, Masayuki,Itoh, Kiminori

, p. 5526 - 5534 (2006)

Visible-light-driven TiO2 photocatalysts doped with nitrogen have been prepared as powders and thin films in a cylindrical tubular furnace under a stream of ammonia gas. The photocatalysts thus obtained were found to have a band-gap energy of 2.95 eV. Electron spin resonance (ESR) under irradiation with visible light (λ ≥ 430 nm) afforded the increase in intensity in the visible-light region. The concentration of trapped holes was about fourfold higher than that of trapped electrons. Nitrogendoped TiO 2 has been used to investigate mechanistically the photocatalytic oxidation of trichloroethylene (TCE) under irradiation with visible light (λ ≥ 420 nm). Cl and O radicals, which contribute significantly to the generation of dichloroacetyl chloride (DCAC) in the photocatalytic oxidation of TCE under UV irradiation, were found to be deactivated under irradiation with visible light. As the main by-product. only phosgene was detected in the photocatalytic oxidation of TCE under irradiation with visible light. Thus, the reaction mechanism of TCE photooxidation under irradiation with visible light clearly differs markedly from that under UV irradiation. Based on the results of the present study, we propose a new reaction mechanism and adsorbed species for the photocatalytic oxidation of TCE under irradiation with visible light. The energy band for TiO2 by doping with nitrogen may involve an isolated band above the valence band.

Electrochemical investigation of the rate-limiting mechanisms for trichlomethylene and carbon tetrachloride reduction at iron surfaces

Li, Tie,Farrell, James

, p. 3560 - 3565 (2001)

The mechanisms involved in reductive dechlorination of carbon tetrachloride (CT) and trichloroethylene (TCE) at iron surfaces were studied to determine if their reaction rates were limited by rates of electron transfer. Chronoamperometry and chronopotentiometry analyses were used to determine the kinetics of CT and TCE reduction by a rotating disk electrode in solutions of constant halocarbon concentration. Rate constants for CT and TCE dechlorination were measured as a function of the electrode potential over a temperature range from 2 to 42 °C. Changes in dechlorination rate constants with electrode potential were used to determine the apparent electron-transfer coefficients at each temperature. The transfer coefficient for CT dechlorination was 0.22 ± 0.02 and was independent of temperature. The temperature independence of the CT transfer coefficient is consistent with a rate-limiting mechanism involving an outer-sphere electron-transfer step. Conversely, the transfer coefficient for TCE was temperature dependent and ranged from 0.06 ± 0.01 at 2 °C to 0.21 ± 0.02 at 42 °C. The temperature-dependent TCE transfer coefficient indicated that its reduction rate was limited by chemical dependent factors and not exclusively by the rate of electron transfer. In accord with a rate-limiting mechanism involving an electron-transfer step, the apparent activation energy (Ea) for CT reduction decreased with decreasing electrode potential and ranged from 33.0 ± 1.6 to 47.8 ± 2.0 kJ/mol. In contrast, the E, for TCE reduction did not decline with decreasing electrode potential and ranged from 29.4 ± 3.4 to 40.3 ± 3.9. The absence of a potential dependence for the TCE Ea supports the conclusion that its reaction rate was not limited by an electron-transfer step. The small potential dependence of TCE reaction rates can be explained by a reaction mechanism in which TCE reacts with atomic hydrogen produced from reduction of water.

Stimulatory effect of anesthetics on dechlorination of carbon tetrachloride in guinea-pig liver microsomes

Fujii, Kohyu

, p. 147 - 153 (1996)

Effects of the anesthetics isoflurane, enflurane, halothane and sevoflurane on the dechlorination of carbon tetrachloride to produce chloroform were investigated using guinea pig liver microsomes. Under anaerobic conditions, chloroform is produced from carbon tetrachloride by the microsomes in the presence of NADPH, and chloroform production from 86 μM carbon tetrachloride was enhanced to 146%, 133%, 123% and 115% by the addition of isoflurane, enflurane, halothane and sevoflurane, respectively. The half-life of oxidized cytochrome P450 which remained during the reduction by the addition of NADPH was shortened to 51%, 54%, 60% and 80% by isoflurane, enflurane, halothane and sevoflurane, respectively, without alteration of NADPH-cytochrome c reductase activity. These anesthetics hastened the onset of the 445 nm absorption band formation which was shown by microsomes with carbon tetrachloride in the presence of NADPH under anaerobic conditions. These results indicate that the anesthetics isoflurane, enflurane, sevoflurane and halothane stimulate the reduction of cytochrome P450 results in the acceleration of the carbon tetrachloride dechlorination. These results may have implications for other type II drugs that are administered during anesthesia.

Carbon tetrachloride transformation in a model iron-reducing culture: Relative kinetics of biotic and abiotic reactions

Adriaens,Bouwer,McCormick

, p. 403 - 410 (2002)

CCl4 (CT) is one of the most frequently encountered chlorinated solvent pollutants in groundwater. Contributions of biotic (cell-mediated) and abiotic (mineral-mediated) reactions CT transformation were investigated in a model iron-reducing system that utilized hydrous ferric oxide (HFO) as the electron acceptor, acetate as the substrate, and Geobacter metallireducens as a representative dissimilative iron-reducing bacteria. The mineral-mediated (abiotic) reaction was estimated to be 60-260-fold faster than the biotic reaction throughout the incubation period. A second member of the dissimilative iron-reducing bacteria, G. metallireducens, could biotically transform CT. However, in the presence of HFO, G. metallireducens drove CT transformation primarily through the formation of reactive mineral surfaces. This did not diminish the role that DIRB play even though it suggested that biologically mineral surfaces may be the principal agents of reductive transformation in iron-reducing environments. The results indicated that an alternative approach to stimulate reductive transformation of pollutants in iron-reducing environments might be to improve the formation of reactive biogenic minerals in situ. Other FeII species have been identified in iron-reducing environments that are also reactive with chlorinated solvents including the ferrous sulfides, green rusts, and sorbed FeII. It could also be possible to couple microbial iron reduction to reactive barrier design to exploit the ability of such bacteria to reactivate passivated metal surfaces.

Micellar Effects on the Base-Catalyzed Oxidative Cleavage of a Carbon-Carbon Bond in 1,1-Bis(p-chlorophenyl)-2,2,2-trichloroethanol

Nome, Faruk,Schwingel, Erineu W.,Ionescu, Lavinel G.

, p. 705 - 710 (1980)

The base-catalyzed oxidative cleavage of 1,1-bis(p-chlorophenyl)-2,2,2-trichloroethanol (Dicofol) results in the formation of chloroform and 4,4'-dichlorobenzophenone.The reaction was studied in the presence of hexadecyltrimethylammonium bromide (CTAB) and hexadecyldimethyl(2-hydroxyethyl)ammonium bromide (CHEDAB), and catalytic factors of 200- and 345-fold, respectively, were obtained.The experimental results are rationalized in terms of an increase of the concentration of the reagents in the micellar phase.Sodium dodecyl sulfate (NaLS) inhibits the reaction, and dodecylcarnitine chloride (LCC) essentially does not alter the rate.The catalysis by cationic surfactants (CTAB, CHEDAB) is inhibited by added salts.The effectiveness of the salts in decreasing the rate constant is NaCl (excit.) = 27.7 kcal/mol, ΔG(excit.) = 19.8 kcal/mol, ΔS(excit.) = 25.9 eu) and for 1.0E-1 M CTAB (ΔH(excit.) = 26.7 kcal/mol, ΔG(excit.) = 20.8 kcal/mol, ΔS(excit.) = 19.6 eu) indicate that the rate decrease observed at high surfactant concentration is due to an entropic contribution to the free-energy term.

Formation of halocarbons in the methane-alkaline halide crystal system under UV radiation

Prilepsky,Povarov,Bredelev,Isidorov

, p. 1910 - 1913 (1998)

The possibility of formation of halomethanes upon the photostimulated reaction of halogen-containing minerals with methane was shown. The dynamics of accumulation of chloromethane, dichloromethane, and chloroform in model systems CH4-NaCl, CH4-sylvinite, and CH4-halite was studied experimentally. The kinetic parameters for the formation of methyl chloride were determined.

Mechanisms and Products of Surface-Mediated Reductive Dehalogenation of Carbon Tetrachloride by Fe(II) on Goethite

Elsner, Martin,Haderlein, Stefan B.,Kellerhals, Thomas,Luzi, Samuel,Zwank, Luc,Angst, Werner,Schwarzenbach, Rene P.

, p. 2058 - 2066 (2004)

Aliphatic chlorinated hydrocarbons, including CCl4, are widespread groundwater contaminants. Mechanisms and product formation of CCl4 reduction by Fe(II) sorbed to goethite, which may lead to completely dehalogenated products or to form chloroform, a toxic product that is fairly persistent under anoxic conditions, were studied. A simultaneous transfer of two electrons and cleavage of two C-Cl bonds of CCl4 would completely circumvent chloroform production. Product formation pathways did not primarily depend on the competition between an initial one- and two-electron transfer, but on the presence of different radical scavengers and the properties of the mineral surface with respect to stabilization of reaction intermediates. Specific adsorption of major anions or pH effects could modify the capability of the goethite surface to stabilize short-lived radical intermediates.

Effects of polydiallyldimethyl ammonium chloride coagulant on formation of chlorinated by products in drinking water

Chang,Chiang,Chao,Liang

, p. 1333 - 1346 (1999)

The objectives of this research work was to evaluate the reduction of THM precursors by cationic p-DADMAC and determine the correlations between the chlorine demand and trihalomethane formation in the presence of electrolyte solutions and ambient light. The chlorine demand was found to be significantly reduced provided that the H2SO4 electrolyte was fed to the sample solutions. The amount of CHCl3 formation was also decreased when the Na2SO4 electrolyte was introduced in spite of the levels of light intensity. The p-DADMAC can not only effectively remove the turbidity but also reduce the formation of CHCl3. The optimum dosage of p-DADMAC for reducing the turbidity, TOC and CHCl3 in the humic acid and source water samples was determined and depended upon the nature of organics. The objectives of this research work was to evaluate the reduction of THM precursors by cationic p-DADMAC and determine the correlations between the chlorine demand and trihalomethane formation in the presence of electrolyte solutions and ambient light. The chlorine demand was found to be significantly reduced provided that the H2SO4 electrolyte was fed to the sample solutions. The amount of CHCl3 formation was also decreased when the Na2SO4 electrolyte was introduced in spite of the levels of light intensity. The p-DADMAC can not only effectively remove the turbidity but also reduce the formation of CHCl3. The optimum dosage of p-DADMAC for reducing the turbidity, TOC and CHCl3 in the humic acid and source water samples was determined and depended upon the nature of organics.

PROTON-TRANSFER MECHANISM IN THE DECARBOXYLATION OF AMMONIUM TRICHLOROACETATE IN ACETONITRILE

Pawlak, Zenon,Fox, Malcolm F.,Tusk, Maria,Kuna, Stevan

, p. 1987 - 1994 (1983)

The rate constants, k, for the decomposition of ammonium trichloroacetate in acetonitrile were determined at 298 K where B is an N-base.The first-order decarboxylation of trichloroacetic acid in the presence of N-bases is strongly deopendent upon proton transfer in complexes.Discussion of the rate constants, k, obtained shows 3 types of complexes in the proton-transfer mechanism, i.e. a symmetrically positioned proton, and without proton transfer for 2 cases: .The sigmoidal curve of rate constants, -log k, plotted against (pKa)AN describes the location of the proton in the hydrogen bridge.The behaviour of (CCl3COOHR)(1-) complexes has many similarities to the molecular complexes, CCl3COOHB, discussed above.Implications of these results for carboxylate additives in overbased lubricating oils are discussed.

The role of hydrogen atoms in CIDNP effects in the reaction of diisobutylaluminum hydride with CCl4

Sadykov,Teregulov

, p. 2040 - 2042 (1998)

Integral polarization of chloroform, methylene dichloride, and pentachloroethane was observed in the 1H NMR spectra during the exothermal reaction of a 1 M solution of Bui2AlH in 1,4-dioxane with CCl4. CIDNP was shown to appear in the diffusion radical pair of the hydrogen atom and trichloromethyl radical.

Fachinetti, G.,Floriani, G.

, (1972)

A study of the Atherton-Todd reaction mechanism

Troev,Kirilov,Roundhill

, p. 1284 - 1285 (1990)

-

Chlorination of phenols: Kinetics and formation of chloroform

Gallard, Herve,von Gunten, Urs

, p. 884 - 890 (2002)

The kinetics of chlorination of several phenolic compounds and the corresponding formation of chloroform were investigated at room temperature. For the chlorination of phenolic compounds, second-order in the phenolic compound. The rate constants of the reactions of HOCl with phenol and phenolate anion and the rate constant of the acid-catalyzed reaction were determined in the pH range 1-11. The second-order rate constants for the reaction HOCl + phenol varied between 0.02 and 0.52 M-1 s-1, for the reaction HOCl and phenolate between 8.46 × 101 and 2.71 × 104 M-1 s-1. The rate constant for the acid-catalyzed reaction varied between 0.37 M-2 s-1 to 6.4 × 103 M-2 s-1. Hammett-type correlations were obtained for the reaction for the reaction of HOCl with phenolate (log(k) = 4.15-3.00 × ∑σ). The formation of chloroform could be interpreted with a second-order model, first-order in chlorine, and first-order in chloroform precursors. The corresponding rate constants varied between k > 100 M-1 s-1 for resorcinol to 0.026 M-1 s-1 to p-nitrophenol at pH 8.0. It was found that the rate-limiting step of chloroform formation is the chlorination of the chlorinated ketones. Yields of chloroform formation depend on the type and position of the substituents and varied between 2 and 95% based on the concentration of the phenol.

Anschuetz

, p. 3512 (1892)

Chang et al.

, p. 2070 (1971)

Reductive dehalogenation of chlorinated methanes by iron metal

Matheson,Tratnyek

, p. 2045 - 2053 (1994)

Reduction of chlorinated solvents by fine-grained iron metal was studied in well-mixed anaerobic batch systems in order to help assess the utility of this reaction in remediation of contaminated groundwater. Iron sequentially dehalogenates carbon tetrachloride via chloroform to methylene chloride. The initial rate of each reaction step was pseudo-first-order in substrate and became substantially slower with each dehalogenation step. Thus, carbon tetrachloride degradation typically occurred in several hours, but no significant reduction of methylene chloride was observed over 1 month. Trichloroethene (TCE) was also dechlorinated by iron, although more slowly than carbon tetrachloride. Increasing the clean surface area of iron greatly increased the rate of carbon tetrachloride dehalogenation, whereas increasing pH decreased the reduction rate slightly. The reduction of chlorinated methanes in batch model systems appears to be coupled with oxidative dissolution (corrosion) of the iron through a largely diffusion-limited surface reaction.

Kinetics of Radiation-Induced Hydrogen Abstraction by CCl3 Radicals in the Liquid Phase. Secondary Alcohols

Feilman, Liviu,Alfassi, Zeev B.

, p. 3060 - 3063 (1981)

The dependence of the yield of products in the γ-radiation-induced free-radical reactions in carbon tetrachloride solutions of secondary alcohols on the alcohol concentration and the temperature was studied in the range of 0.05-0.6 M and 30-150 deg C.The rate constant for the reaction CCl3 + R1R2COH -> CHCl3 + R1R2COH (k1) was found as logk1 (M-1 s-1) = 8.63-9.1, where Τ = 2.303RT kcal mol-1.The activation energy is 1.8 +/- 0.3 kcal mol-1 lower than for secondary hydrogens in alkanes and about the same as for the tertiary hydrogens in 2,3-dimethylbutane.

Synthesis of Decorated Carbon Structures with Encapsulated Components by Low-Voltage Electric Discharge Treatment

Bodrikov, I. V.,Pryakhina, V. I.,Titov, D. Yu.,Titov, E. Yu.,Vorotyntsev, A. V.

, p. 60 - 69 (2022/03/17)

Abstract: Polycondensation of complexes of chloromethanes with triphenylphosphine by the action of low-voltage electric discharges in the liquid phase gives nanosized solid products. The elemental composition involving the generation of element distribution maps (scanning electron microscopy–energy dispersive X?ray spectroscopy mapping) and the component composition (by direct evolved gas analysis–mass spectrometry) of the solid products have been studied. The elemental and component compositions of the result-ing structures vary widely depending on the chlorine content in the substrate and on the amount of triphenylphosphine taken. Thermal desorption analysis revealed abnormal behavior of HCl and benzene present in the solid products. In thermal desorption spectra, these components appear at an uncharacteristically high temperature. The observed anomaly in the behavior of HCl is due to HCl binding into a complex of the solid anion HCI-2 with triphenyl(chloromethyl)phosphonium chloride, which requires a relatively high temperature (up to 800 K) to decompose. The abnormal behavior of benzene is associated with its encapsulated state in nanostructures. The appearance of benzene begins at 650 K and continues up to temperatures above 1300?K.

A process of preparing methyl chloride using multistage reaction

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Paragraph 0092-0100; 0112; 0120, (2020/06/10)

The present invention relates to a method of producing methyl chloride by multistage reactions. The method of the present invention comprises: a) a chlorination step for sufficiently increasing the conversion rate of methane, which is an initial reactant; and b) a subsequent reaction step for actively utilizing hydrogen chloride (HCl), which is a hazardous byproduct of chlorination, efficiently treating harmful hydrogen chloride, and at the same time, improving the overall production of methyl chloride.COPYRIGHT KIPO 2020

Control of methane chlorination with molecular chlorine gas using zeolite catalysts: Effects of Si/Al ratio and framework type

Kwon, Seungdon,Chae, Ho-Jeong,Na, Kyungsu

, p. 111 - 117 (2020/01/31)

CH4 chlorination with Cl2 gas is used for the production of chlorinated products via C–H bond activation in CH4. Due to the high reactivity of Cl2, this reaction can occur spontaneously under UV irradiation or with mild thermal energy even in the absence of a catalyst via a free radical-mediated chain reaction mechanism that undesirably causes excessive chlorination of the CH4 and is thus non-selective. In this work, CH4 chlorination is investigated using HY and MFI zeolites with various Si/Al ratios, by which the reaction is catalytically controlled for selective production of the mono-chlorinated product (CH3Cl). Depending on the framework type, Si/Al ratio of the zeolites, and reaction conditions, different degrees of CH4 conversion, CH3Cl selectivity, and hence CH3Cl yield were achieved, by which systematic relationships between the catalyst properties and performance were discovered. A high aluminum content facilitated the production of CH3Cl with up to ~20 % yield at a high gas hourly space velocity of 2400 cm3gcat?1 h?1 with a CH4/Cl2 ratio of 1 at 350 °C. HY zeolites generally furnished a slightly higher CH3Cl yield than MFI zeolites, which can be attributed to the larger micropores of the HY zeolites that support facile molecular diffusion. With various flow rates and ratios of CH4 and Cl2, the CH4 conversion and CH3Cl selectivity changed simultaneously, with a trade-off relationship. Unfortunately, all zeolite catalysts suffered from framework dealumination due to the HCl produced during the reaction, but it was less pronounced for the zeolites having a low aluminum content. The results shed light on the detailed roles of zeolites as solid-acid catalysts in enhancing CH3Cl production during electrophilic CH4 chlorination.