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1,1-Dichloroethylene, also known as vinylidene chloride, is a colorless gas with a sweet, pungent odor. It is an important industrial chemical, primarily used in the production of polyvinylidene chloride (PVDC) resins and copolymers. These materials are utilized in various applications, including food packaging, wire and cable insulation, and pipe lining. 1,1-Dichloroethylene is synthesized through the reaction of acetylene and hydrogen chloride, and it is considered a hazardous substance due to its potential health risks, such as irritation to the eyes, nose, and throat, as well as its classification as a probable human carcinogen. Exposure to high concentrations can lead to central nervous system depression, and it is also harmful to the environment, particularly aquatic life.

75-35-4

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75-35-4 Usage

Check Digit Verification of cas no

The CAS Registry Mumber 75-35-4 includes 5 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 2 digits, 7 and 5 respectively; the second part has 2 digits, 3 and 5 respectively.
Calculate Digit Verification of CAS Registry Number 75-35:
(4*7)+(3*5)+(2*3)+(1*5)=54
54 % 10 = 4
So 75-35-4 is a valid CAS Registry Number.

75-35-4 Well-known Company Product Price

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  • Supelco

  • (40027)  1,1-Dichloroethenesolution  certified reference material, 1000 μg/mL in methanol

  • 75-35-4

  • 000000000000040027

  • 359.19CNY

  • Detail
  • USP

  • (1601204)  ResidualSolventClass1-1,1-Dichloroethene  United States Pharmacopeia (USP) Reference Standard

  • 75-35-4

  • 1601204-3X1.2ML

  • 4,662.45CNY

  • Detail

75-35-4SDS

SAFETY DATA SHEETS

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

Version: 1.0

Creation Date: Aug 16, 2017

Revision Date: Aug 16, 2017

1.Identification

1.1 GHS Product identifier

Product name 1,1-dichloroethene

1.2 Other means of identification

Product number -
Other names 1,1-Dichloroethene

1.3 Recommended use of the chemical and restrictions on use

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

1.4 Supplier's details

1.5 Emergency phone number

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

More Details:75-35-4 SDS

75-35-4Synthetic route

1,1,2-trichloroethane
79-00-5

1,1,2-trichloroethane

1,1-Dichloroethylene
75-35-4

1,1-Dichloroethylene

Conditions
ConditionsYield
cesium chloride; silica gel at 250℃; for 5h; dehydrochlorination, catalytic activity, other temperature;100%
With sodium hydroxide; triethylbenzylammonium ethanolate at 30℃; for 1h; Product distribution; further triethylbenzylammonium alkoxide catalysts;100%
With sodium hydroxide at 20℃;98%
1,1,1-trichloroethane
71-55-6

1,1,1-trichloroethane

A

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

1,1,1,2-tetrachoroethane

B

1,1-Dichloroethylene
75-35-4

1,1-Dichloroethylene

C

pentachloroethane
76-01-7

pentachloroethane

Conditions
ConditionsYield
With chlorine at 25℃; Irradiation;A 92.5%
B 2.4%
C 5.1%
With chlorine at 25℃; Irradiation;A 89.9%
B 4.7%
C 5.3%
thiophosgene
463-71-8

thiophosgene

CH2Cl3P

CH2Cl3P

1,1-Dichloroethylene
75-35-4

1,1-Dichloroethylene

Conditions
ConditionsYield
In hexane at 0 - 20℃; Inert atmosphere; Autoclave;80%
1,1,1-trichloroethane
71-55-6

1,1,1-trichloroethane

A

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

1,1,1,2-tetrachoroethane

B

1,1-Dichloroethylene
75-35-4

1,1-Dichloroethylene

Conditions
ConditionsYield
With chlorine at 200℃; Mechanism; Irradiation; other temperature; other laser; other Cl2 flow rate; other ratio educt/Cl2;A 61.3%
B 25.9%
With chlorine at 200℃; Irradiation;A 61.3%
B 25.9%
methylene
2465-56-7

methylene

dibromodichloromethane
594-18-3

dibromodichloromethane

A

1,1-Dichloroethylene
75-35-4

1,1-Dichloroethylene

B

1,2-dibromomethane
74-95-3

1,2-dibromomethane

Conditions
ConditionsYield
Tetrabrommethan,Bromoform und Jodoform reagieren analog;
ethane
74-84-0

ethane

1,1-Dichloroethylene
75-35-4

1,1-Dichloroethylene

Conditions
ConditionsYield
With steam; chlorine at 450 - 600℃;
With hydrogenchloride; chlorine at 450 - 600℃;
1,1,1-trichloroethane
71-55-6

1,1,1-trichloroethane

A

propene
187737-37-7

propene

B

1,1-Dichloroethylene
75-35-4

1,1-Dichloroethylene

Conditions
ConditionsYield
at 360 - 435℃; Geschwindigkeit.Pyrolysis;
1,1,1-trichloroethane
71-55-6

1,1,1-trichloroethane

1,1-Dichloroethylene
75-35-4

1,1-Dichloroethylene

Conditions
ConditionsYield
With aluminum oxide at 176.9 - 326.9℃;
With 2,4,6-triphenylverdazyl radical for 0.0833333h; Product distribution; Rate constant; Irradiation; Decomposition of CH3CCl3 (triphenylverdazyl radical as monitor), influence of stabilizators, other time;;
With steel wool; chlorine at 167 - 196℃;
With iron(III) chloride at 50 - 74℃;
With aluminum oxide at 250℃;
1,1,2-trichloroethane
79-00-5

1,1,2-trichloroethane

A

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

cis-1,2-Dichloroethylene

B

trans-1,2-dichloroethylene
156-60-5

trans-1,2-dichloroethylene

C

1,1-Dichloroethylene
75-35-4

1,1-Dichloroethylene

Conditions
ConditionsYield
at 500℃; bei der thermischen Zersetzung;
at 500℃; Geschwindigkeit dieser Spaltung bei verschiedenen Temperaturen und Beschleunigung der Pyrolyse durch geringe Mengen Sauerstoff oder Chlor;
1,1,2-trichloroethane
79-00-5

1,1,2-trichloroethane

A

1,2-Dichloroethylene
540-59-0

1,2-Dichloroethylene

B

1,1-Dichloroethylene
75-35-4

1,1-Dichloroethylene

Conditions
ConditionsYield
potassium chloride at 250℃; under 26.3 Torr; Product distribution; temperatures 200 or 220 deg C, different types of silica gels, conversion and selectivity given;
With chlorine at 400℃;
With oxygen at 400℃;
1,1,2-trichloroethane
79-00-5

1,1,2-trichloroethane

A

1,1-Dichloroethylene
75-35-4

1,1-Dichloroethylene

B

Trichloroethylene
79-01-6

Trichloroethylene

Conditions
ConditionsYield
With oxygen; copper(II) oxide at 375 - 525℃;
1,1,1,2-tetrachoroethane
630-20-6

1,1,1,2-tetrachoroethane

1,1-Dichloroethylene
75-35-4

1,1-Dichloroethylene

Conditions
ConditionsYield
With zinc at 30 - 35℃;
With iron sulfide In water at 25℃; pH=8.3; Kinetics; Dehalogenation;
methylene
2465-56-7

methylene

dibromodichloromethane
594-18-3

dibromodichloromethane

chlorobenzene
108-90-7

chlorobenzene

A

1,1-Dichloroethylene
75-35-4

1,1-Dichloroethylene

B

1,2-dibromomethane
74-95-3

1,2-dibromomethane

acetylene
74-86-2

acetylene

A

1,1-Dichloroethylene
75-35-4

1,1-Dichloroethylene

B

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

1,1,2,2-tetrachloroethane

Conditions
ConditionsYield
With chlorine; iron(III) chloride; 1,1,2,2-tetrachloroethane at 135℃;
1,1,1-trichloroethane
71-55-6

1,1,1-trichloroethane

1,3,5-triphenylverdazyl
2154-65-6

1,3,5-triphenylverdazyl

A

1,1-Dichloroethylene
75-35-4

1,1-Dichloroethylene

B

1,3,5-triphenylverdazylium chloride
72024-84-1

1,3,5-triphenylverdazylium chloride

C

2,4,6-triphenylverdazyl
22459-57-0

2,4,6-triphenylverdazyl

Conditions
ConditionsYield
at 25℃; Kinetics; Thermodynamic data; Irradiation; E;
1,1,1-trichloroethane
71-55-6

1,1,1-trichloroethane

A

4-chloro-6-methyl-2H-pyran-2-one
17422-72-9

4-chloro-6-methyl-2H-pyran-2-one

B

1-Chloro-1,1-difluoroethane
75-68-3

1-Chloro-1,1-difluoroethane

C

HCFC-141b
1717-00-6

HCFC-141b

D

1,1-Dichloroethylene
75-35-4

1,1-Dichloroethylene

E

3,5-dichlorophenol
591-35-5

3,5-dichlorophenol

F

2-methyl-5,7-dichlorochromone

2-methyl-5,7-dichlorochromone

Conditions
ConditionsYield
With sulfuric acid; hydrogen fluoride; antimonypentachlorideA 1.19 g
B n/a
C n/a
D n/a
E 0.20 g
F 0.08 g
1,1,1-trichloroethane
71-55-6

1,1,1-trichloroethane

A

2,2,2-trifluoroethanol
420-46-2

2,2,2-trifluoroethanol

B

1-Chloro-1,1-difluoroethane
75-68-3

1-Chloro-1,1-difluoroethane

C

HCFC-141b
1717-00-6

HCFC-141b

D

1,1-Dichloroethylene
75-35-4

1,1-Dichloroethylene

Conditions
ConditionsYield
With fluorinated (with SF4) γ-alumina; hydrogen fluoride for 2h; Product distribution; Ambient temperature;
With hydrogen fluoride; antimonypentachloride at 60℃; under 7500.6 Torr; Mechanism; var. reaction partners and temp.;
With chromium(III) oxide; sulfur tetrafluoride; hydrogen fluoride at 20℃; for 2h; Product distribution; Further Variations:; Reagents;
1,1,2-trichloroethane
79-00-5

1,1,2-trichloroethane

A

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

cis-1,2-Dichloroethylene

B

trans-1,2-dichloroethylene
156-60-5

trans-1,2-dichloroethylene

C

chloroethylene
75-01-4

chloroethylene

D

chloroacetylene
593-63-5

chloroacetylene

E

1,1-Dichloroethylene
75-35-4

1,1-Dichloroethylene

F

acetylene
74-86-2

acetylene

Conditions
ConditionsYield
under 0.2 Torr; Product distribution; Mechanism; Irradiation; laser photolysis, var. pressure, var. pulse energy, presence of var. gases;
β,β-dichloroethylacetate
53942-53-3

β,β-dichloroethylacetate

A

chloroethylene
75-01-4

chloroethylene

B

1,1-Dichloroethylene
75-35-4

1,1-Dichloroethylene

Conditions
ConditionsYield
In toluene at 520℃; Product distribution;
2,2,2-trichloroethyl acetate
625-24-1

2,2,2-trichloroethyl acetate

1,1-Dichloroethylene
75-35-4

1,1-Dichloroethylene

Conditions
ConditionsYield
In toluene at 540℃; Product distribution;
α,α-dichloroethyl radical
19468-97-4

α,α-dichloroethyl radical

A

1,1-Dichloroethylene
75-35-4

1,1-Dichloroethylene

B

hydrogen

hydrogen

Conditions
ConditionsYield
In gas at 294℃; under 740 Torr; Rate constant;
ethyl β,β-dichlorovinyl sulfide
21985-81-9

ethyl β,β-dichlorovinyl sulfide

A

thiophene
188290-36-0

thiophene

B

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

1,1,2,2-tetrachloroethylene

C

1,1-Dichloroethylene
75-35-4

1,1-Dichloroethylene

D

Trichloroethylene
79-01-6

Trichloroethylene

E

chlorobenzene
108-90-7

chlorobenzene

F

benzene
71-43-2

benzene

Conditions
ConditionsYield
at 500℃; for 0.00444444h; Product distribution;
(2,2,2-Trichloro-ethoxy)-ethene
89585-65-9

(2,2,2-Trichloro-ethoxy)-ethene

1,1-Dichloroethylene
75-35-4

1,1-Dichloroethylene

Conditions
ConditionsYield
In toluene at 530℃; Product distribution;

75-35-4Relevant academic research and scientific papers

Catalytic Dehydrochlorination of 1,1,2-Trichloroethane (TCE) into 1,1-Dichloroethene (DCE) over Cesium Nitrate Supported on Silica Gel

Mochida, Isao,Yasumoto, Yoshinori,Fujitsu, Hiroshi,Kojima, Yasuhiro

, p. 461 - 464 (1992)

Catalytic activity of silica gel-supported cesium salts was examined for the dehydrochlorination of TCE into DCE by recovering hydrogen chloride.Among the salts, CsNO3 showed the best activity, although it was converted into CsCl during the reaction.High dispersion of CsNO3 on silica gel may be a major reason of the high activity.

HIGH CATALYTIC ACTIVITY OF CsCl SUPPORTED ON SILICA GEL FOR THE SELECTIVE DEHYDROCHLORINATION OF 1,1,2-TRICHLOROETHANE

Mochida, Isao,Miyazaki, Tatsuro,Takagi, Takeshi,Fujitsu, Hiroshi

, p. 833 - 836 (1985)

CsCl supported on a particular silica gel dryed at 120 deg C, exhibited a remarkable activity fot selective dehydrochlorination of TCE into 1,1-DCE after the calcination around 500 deg C.The proper heat-treatment before and after impregnation of CsCl on the silica gel strongly influenced the activity of the catalyst.

Interaction and Catalytic Decomposition of 1,1,1-Trichloroethane on High Surface Area Alumina. An Infrared Spectroscopic Study

Ballinger, Todd H.,Yates, John T.

, p. 1417 - 1423 (1992)

Transmission infrared spectroscopy has been used to study the catalytic decomposition of 1,1,1-trichloroethane, CH3CCl3, on high surface area alumina, Al2O3, in the temperature range 300 - 600 K.At 300K CH3CCl3 is reversibly adsorbed on the isolated surface hydroxyl groups of Al2O3 via hydrogen bonding.At T >/= 400 K an α,β-HCl elimination occurs, forming CH2=CCl2(g).A small amount of surface carboxylate was also formed by means of a minor reaction pathway.It was found that Lewis acid (Al3+) surface sites were involved in causing the primary reaction.This was shown by the observation that irreversible adsorption of pyridine on the Al3+ sites efficiently quenched the surface reaction.Conversely, surface Al-OH groups are not involved in the CH3CCl3 decomposition.

Mesoporous carbon nitride as a basic catalyst in dehydrochlorination of 1,1,2-trichloroethane into 1,1-dichloroethene

Tian, Cong,Lu, Chunshan,Wang, Bolin,Xie, Xiangzhou,Miao, Yangsen,Li, Xiaonian

, p. 103829 - 103833 (2015)

1,1-Dichloroethene has many applications in industrial production and it holds great promise in developing a vapor phase catalytic dehydrochlorination process. We synthesized a carbon nitride material by dissolving dicyandiamide in N,N-dimethylformamide (DMF) as a precursor and using SBA-15 as a template. A carbon nitride material with a mesoporous structure and textured pores has been obtained and then characterized by N2-adsorption measurements, XRD, HRTEM, EDS and FT-IR. A mesoporous carbon nitride material with a surface area of 350 m2 g-1 and pore volume of 0.72 cm3 g-1 was fabricated, which also possessed triazine N heterocycles with extra amino groups. It is an outstanding heterogeneous base catalyst in the selective catalytic dehydrochlorination of 1,1,2-trichloroethane into 1,1-dichloroethene reaction with a maximum 1,1,2-trichloroethane conversion of 23.96% and maximum 1,1-dichloroethene selectivity of 100%. A total of 110 h stability experiment of the catalyst was provided and the selectivity stayed above 99% all through the experiment and the conversion remained no less than 15% for 35 h.

Method for eliminating hydrogen chloride by catalytic cracking of chloralkane

-

Paragraph 0095-0100, (2020/08/06)

The invention discloses a method for eliminating hydrogen chloride by catalytic cracking of chloralkane, comprising the following steps of: carrying out a cracking reaction on chloralkane under the action of a biomass-based nitrogen-doped carbon catalyst to eliminate hydrogen chloride so as to prepare corresponding olefin, wherein the biomass-based nitrogen-doped carbon catalyst is prepared by carbonizing biomass or a mixture of biomass and a nitrogen source at 400-1000 DEG C, and the biomass is selected from at least one of bamboo processing leftovers, wood processing leftovers, plant straws,plant leaves, cereals, beans, cereal processing leftovers, bean processing leftovers and livestock manure. The method disclosed by the invention has the advantages of simple preparation process, easily available raw materials, low cost, strong process controllability, easiness in large-scale production, high catalytic cracking conversion rate of the chloralkane, high product selectivity, low energy consumption and the like.

Nitrogen-Doped Carbon-Assisted One-pot Tandem Reaction for Vinyl Chloride Production via Ethylene Oxychlorination

Chen, De,Chen, Qingjun,Fuglerud, Terje,Ma, Guoyan,Ma, Hongfei,Qi, Yanying,Rout, Kumar R.,Wang, Yalan

supporting information, p. 22080 - 22085 (2020/10/02)

A bifunctional catalyst comprising CuCl2/Al2O3 and nitrogen-doped carbon was developed for an efficient one-pot ethylene oxychlorination process to produce vinyl chloride monomer (VCM) up to 76 % yield at 250 °C and under ambient pressure, which is higher than the conventional industrial two-step process (≈50 %) in a single pass. In the second bed, active sites containing N-functional groups on the metal-free N-doped carbon catalyzed both ethylene oxychlorination and ethylene dichloride (EDC) dehydrochlorination under the mild conditions. Benefitting from the bifunctionality of the N-doped carbon, VCM formation was intensified by the surface Cl*-looping of EDC dehydrochlorination and ethylene oxychlorination. Both reactions were enhanced by in situ consumption of surface Cl* by oxychlorination, in which Cl* was generated by EDC dehydrochlorination. This work offers a promising alternative pathway to VCM production via ethylene oxychlorination at mild conditions through a single pass reactor.

METHOD OF PRODUCING VINYL CHLORIDE

-

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.

Efficient Electrocatalysis for the Preparation of (Hetero)aryl Chlorides and Vinyl Chloride with 1,2-Dichloroethane

Liang, Yujie,Lin, Fengguirong,Adeli, Yeerlan,Jin, Rui,Jiao, Ning

supporting information, p. 4566 - 4570 (2019/02/14)

Although the application of 1,2-dichloroethane (DCE) as a chlorinating reagent in organic synthesis with the concomitant release of vinyl chloride as a useful byproduct is a fantastic idea, it still presents a tremendous challenge and has not yet been achieved because of the harsh dehydrochlorination conditions and the sluggish C?H chlorination process. Here we report a bifunctional electrocatalysis strategy for the catalytic dehydrochlorination of DCE at the cathode simultaneously with anodic oxidative aromatic chlorination using the released HCl as the chloride source for the efficient synthesis of value-added (hetero)aryl chlorides. The mildness and practicality of the protocol was further demonstrated by the efficient late-stage chlorination of bioactive molecules.

New method for synthesizing ranitidine

-

Paragraph 0034-0036; 0047-049; 0059-0061, (2018/12/14)

The invention discloses a new method for synthesizing ranitidine. The method comprises the steps of synthesizing vinylidene chloride, synthesizing 1, 1-dichloro-2-nitroethylene, carrying out a ring-closing reaction, carrying out a ring-opening reaction in presence of a desiccant, and synthesizing the ranitidine. The method adopts an anhydrous environment in the preparation process of a ring-opening product, thus avoiding the interference with the reaction and the generation of impurities due to the presence of water, reducing the post-treatment work and increasing the utilization rate of the raw materials. The preparation method provided by the invention effectively increases the reaction yield of the ring-opening product, improves the purity of the ring-opening reaction, and reduces the reaction time; therefore, the yield and purity of the product ranitidine are improved, the production cost is lowered, and the method is more beneficial to industrial production.

Method for synthesizing ranitidine

-

Paragraph 0034; 0035; 0045; 0046; 0056; 0057; 0067; 0068, (2017/10/09)

A method for synthesizing ranitidine includes following steps: 1), dropwise adding sodium hydroxide water solution into 1, 1, 2-trichloroethane at 30-35 DEG C for reaction to obtain vinylidene chloride, wherein a mass ratio of 1, 1, 2-trichloroethan to sodium hydroxide is 1:0.3-0.33; 2), dropwise adding vinylidene chloride into mixed acid of concentrated hydrochloric acid and concentrated nitric acid at 20-25 DEG C for reaction for 2-4h, wherein a consumption ratio of vinylidene chloride to the mixed acid is 1:2-3; 3), adding cysteamine hydrochloride into sodium hydroxide and potassium hydroxide solution, and dropwise adding a product of the step 2) at 50-55 DEG C to obtain a closed-loop product; 4), enabling the closed-loop product to react with alcohol or methanol solution at room temperature for 14-18h to obtain an open-loop product; 5), adding the open-loop product and 2-[(dimethylamino)methyl]-5 chloromethyl-furan into potassium hydroxide or sodium hydroxide water solution for reaction at 40-50 DEG C for 2-4h to obtain ranitidine. The method lowers potential safety hazards and is simple and easy for industrial production.

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