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107-31-3

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107-31-3 Usage

Description

Methyl formate is the methyl ester form of formic acid.It has a rather pleasant odor. It is an aromatic compound found in apples (Neubeller and Buchloh, 1986), and was identified as a volatile constituent in brewed, roasted, and dried coffee (Lovell et al., 1980); it has also been detected in the volatiles of chicken, beef, and pork flavor (Shahidi et al., 1986). Methyl formate is used primarily to manufacture formamide, dimethylformamide, and formic acid. It is also used as a solvent for quick-drying finishes such as lacquers and in organic synthesis. Other uses include use as a larvicide for tobacco and food crops, in the manufacture of certain pharmaceuticals, and as a blowing agent for foam insulation. It was formerly used as a refrigerant for house appliances.

Chemical Properties

Different sources of media describe the Chemical Properties of 107-31-3 differently. You can refer to the following data:
1. Methyl formate is a colorless liquid with a pleasant odor. Its solubility in water is 230 g/l at 25 °C (Riddick et al., 1985), but it reacts slowly with water to form formic acid and methyl alcohol (DOT, 1984). It is soluble in ether, chloroform, and is miscible with ethanol (Lide, 2000).
2. Methyl formate , also called methyl methanoate, is the methyl ester of formic acid. The simplest example of an ester, it is a clear liquid with an ethereal odour, high vapor pressure, and low surface tension.

Physical properties

Clear, colorless, mobile liquid with a pleasant, etheral odor. An odor threshold concentration of 130 ppmv was reported by Nagata and Takeuchi (1990).

Uses

Different sources of media describe the Uses of 107-31-3 differently. You can refer to the following data:
1. Methyl formate is used as a fumigant, as alarvicide for food crops, and as a solvent forcellulose acetate.
2. Methyl formate is used primarily to manufacture formamide, dimethyl formamide, and formic acid. Because of its high vapor pressure, it is used for quick - drying finishes. It is also used as an insecticide and to manufacture certain pharmaceuticals. Foam Supplies, Inc. has trademarked Ecomate, which is used as a blowing agent for foam insulation, as a replacement for CFC, HCFC, or HFCs, with zero ozone depletion potential and < 25 global warming potential. A historical use of methyl formate, which sometimes brings it attention, was in refrigeration. Before the introduction of less-toxic refrigerants, methyl formate was used as an alternative to sulfur dioxide in domestic refrigerators, such as some models of the famous GE Monitor Top. Owners of methyl formate refrigerators should keep in mind that, even though they operate below atmospheric pressure, if evidence of a leak develops, they should take measures to avoid exposure to the ether-smelling liquid and vapor.
3. Fumigant and larvicide for tobacco and food crops. Fire hazard is avoided by use with CO2.

Production Methods

In the laboratory, methyl formate can be produced by the condensation reaction of methanol and formic acid, as follows: HCOOH + CH3OH → HCOOCH3 + H2O Industrial methyl formate, however, is usually produced by the combination of methanol and carbon monoxide (carbonylation) in the presence of a strong base, such as sodium methoxide : CH3OH + CO → HCOOCH3 This process, practiced commercially by BASF among other companies gives 96 % selectivity toward methyl formate, although it can suffer from catalyst sensitivity to water, which can be present in the carbon monoxide feedstock, commonly derived from synthesis gas. Very dry carbon monoxide is, therefore, an essential requirement.

General Description

A clear colorless liquid with an agreeable odor. Flash point -27°F. Less dense than water Vapors heavier than air.

Air & Water Reactions

Highly flammable. Water soluble. Reacts slowly with water to give formic acid, a corrosive material, and methanol, a flammable liquid. Both products are dissolved in the water.

Reactivity Profile

Methyl formate reacts with acids to liberate heat along with alcohols and acids. Strong oxidizing acids may cause a vigorous reaction that is sufficiently exothermic to ignite the reaction products. Heat is also generated with caustic solutions. Flammable hydrogen is generated by mixing with alkali metals and hydrides.

Hazard

Flammable, dangerous fire and explosionrisk, explosive limits in air 5.9–20%. Eye, upperand lower respiratory tract irritant.

Health Hazard

Different sources of media describe the Health Hazard of 107-31-3 differently. You can refer to the following data:
1. Methyl formate is a moderately toxic com pound affecting eyes, respiratory tract, andcentral nervous system. It is an irritant tothe eyes, nose, and lungs. Exposure to highconcentrations of its vapors in air may pro duce visual disturbances, irritations, narcoticeffects, and respiratory distress in humans.Such effects may be manifested at a 1-hourexposure to about 10,000-ppm concentration.Cats died of pulmonary edema from 2-hourexposure to this concentrationThe acute oral toxicity of methyl formatewas low in test subjects. The symptoms werenarcosis, visual disturbances, and dyspnea.An oral LD50 value in rabbit is in the range1600 mg/kg..
2. Inhalation causes irritation of mucous membranes. Prolonged inhalation can produce narcosis and central nervous symptoms, including some temporary visual disturbance. Contact with liquid irritates eyes and may irritate skin if allowed to remain. Ingestion causes irritation of mouth and stomach and central nervous system depression, including visual disturbances.

Fire Hazard

Behavior in Fire: Vapor is heavier than air and may travel considerable distance to a source of ignition and flash back.

Flammability and Explosibility

Flammable

Chemical Reactivity

Reactivity with Water Slow reaction to form formic acid and methyl alcohol; reaction is not hazardous; Reactivity with Common Materials: No reaction; Stability During Transport: Stable; Neutralizing Agents for Acids and Caustics: Not pertinent; Polymerization: Not pertinent; Inhibitor of Polymerization: Not pertinent.

Safety Profile

Moderately toxic by ingestion. Inhalation of vapor can cause irritation to nasal passages and conjunctiva, optic neuritis, narcosis, retching, and death from pulmonary irritation. Industrial fatalities have occurred only with exposure to high concentrations. Flammable liquid. Very dangerous fire hazard when exposed to heat or flame; can react vigorously with oxidizing materials. Explosive in the form of vapor when exposed to heat or flame. Reacts with methanol + sodium methoxide to form an explosive product. To fight fire, use alcohol foam, CO2, dry chemical. When heated to decomposition it emits acrid smoke and irritating fumes.

Potential Exposure

Methyl formate is used as a solvent; as an intermediate in pharmaceutical manufacture; and as a fumigant

Environmental fate

Photolytic. Methyl formate, formed from the irradiation of dimethyl ether in the presence of chlorine, degraded to carbon dioxide, water, and small amounts of formic acid. Continued irradiation degraded formic acid to carbon dioxide, water, and hydrogen chloride (Kallos and Tou, 1977; Good et al., 1999). A rate constant of 2.27 x 10-12 cm3/molecule?sec was reported for the reaction of methyl formate and OH radicals in the atmosphere (Atkinson, 1989). Chemical/Physical. Hydrolyzes slowly in water forming methanol and formic acid (NIOSH, 1997). Hydrolysis half-lives reported at 25 °C: 0.91 h at pH 9, 9.1 h at pH 8, 2.19 d at pH 7, and 21.9 d at pH 6 (Mabey and Mill, 1978).

Shipping

Color code—Red: Flammability Hazard: Store in a flammable liquid storage area or approved cabinet away from ignition sources and corrosive and reactive materials. Prior to working with this chemical, personnel should be trained on its proper handling and storage. Before entering confined space where this chemical may be present, check to make sure that an explosive concentration does not exist. Methyl formate must be stored to avoid contact with strong oxidizers, such as chlorine, bromine, chlorine dioxide; nitrates, and permanganates; since violent reactions occur. Store in tightly closed containers in a cool, well-ventilated area away from heat. Sources of ignition, such as smoking and open flames are prohibited where methyl formate is handled, used, or stored. Metal containers involving the transfer of 5 gal or more of methyl formate should be grounded and bonded. Drums must be equipped with selfclosing valves, pressure vacuum bungs; and flame arresters. Use only nonsparking tools and equipment, especially when opening and closing containers of methyl formate. Wherever methyl formate is used, handled, manufactured, or stored, use explosion-proof electrical equipment and fittings.

Purification Methods

Wash the formate with strong aqueous Na2CO3, dry it with solid Na2CO3 and distil it from P2O5. (Procedure removes free alcohol or acid.) [Beilstein 2 IV 20.]

Incompatibilities

May form explosive mixture with air. Incompatible with oxidizers (chlorates, nitrates, peroxides, permanganates, perchlorates, chlorine, bromine, fluorine, etc.); contact may cause fires or explosions. Keep away from alkaline materials, strong bases, strong acids, oxoacids, epoxides. Reacts slowly with water to form methanol and formic acid. Contact with water, steam releases formic acid. Compounds of the carboxyl group react with all bases, both inorganic and organic (i.e., amines) releasing substantial heat, water and a salt that may be harmful. Incompatible with arsenic compounds (releases hydrogen cyanide gas), diazo compounds, dithiocarbamates isocyanates, mercaptans, nitrides, and sulfides (releasing heat, toxic, and possibly flammable gases), thiosulfates and dithionites (releasing hydrogen sulfate and oxides of sulfur)

Waste Disposal

Incineration; atomizing in a suitable combustion chamber.

References

Lee, Jae S., J. C. Kim, and Y. G. Kim. "Methyl formate as a new building block in C1 chemistry." Applied Catalysis 57.1 (1990): 1-30. Handa, Yash Paul, et al. "Insulating Thermoplastic Foams Made With Methyl Formate-Based Blowing Agents." (2006).

Check Digit Verification of cas no

The CAS Registry Mumber 107-31-3 includes 6 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 3 digits, 1,0 and 7 respectively; the second part has 2 digits, 3 and 1 respectively.
Calculate Digit Verification of CAS Registry Number 107-31:
(5*1)+(4*0)+(3*7)+(2*3)+(1*1)=33
33 % 10 = 3
So 107-31-3 is a valid CAS Registry Number.
InChI:InChI=1/C2H4O2/c1-4-2-3/h2H,1H3

107-31-3 Well-known Company Product Price

  • Brand
  • (Code)Product description
  • CAS number
  • Packaging
  • Price
  • Detail
  • Alfa Aesar

  • (A15850)  Methyl formate, 97%, may cont. up to ca 3% methanol   

  • 107-31-3

  • 500ml

  • 193.0CNY

  • Detail
  • Alfa Aesar

  • (A15850)  Methyl formate, 97%, may cont. up to ca 3% methanol   

  • 107-31-3

  • 2500ml

  • 440.0CNY

  • Detail
  • Alfa Aesar

  • (A15850)  Methyl formate, 97%, may cont. up to ca 3% methanol   

  • 107-31-3

  • 10000ml

  • 1009.0CNY

  • Detail
  • Sigma-Aldrich

  • (291056)  Methylformate  anhydrous, 99%

  • 107-31-3

  • 291056-100ML

  • 624.78CNY

  • Detail
  • Sigma-Aldrich

  • (291056)  Methylformate  anhydrous, 99%

  • 107-31-3

  • 291056-1L

  • 1,333.80CNY

  • Detail
  • Sigma-Aldrich

  • (259705)  Methylformate  spectrophotometric grade, 99%

  • 107-31-3

  • 259705-1L

  • 2,127.06CNY

  • Detail
  • Sigma-Aldrich

  • (M46837)  Methylformate  reagent grade, 97%

  • 107-31-3

  • M46837-1L

  • 427.05CNY

  • Detail
  • Sigma-Aldrich

  • (M46837)  Methylformate  reagent grade, 97%

  • 107-31-3

  • M46837-4X1L

  • 1,257.75CNY

  • Detail
  • Sigma-Aldrich

  • (06547)  Methylformate  analytical standard

  • 107-31-3

  • 06547-5ML

  • 576.81CNY

  • Detail

107-31-3SDS

SAFETY DATA SHEETS

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

Version: 1.0

Creation Date: Aug 10, 2017

Revision Date: Aug 10, 2017

1.Identification

1.1 GHS Product identifier

Product name methyl formate

1.2 Other means of identification

Product number -
Other names methyl-formate

1.3 Recommended use of the chemical and restrictions on use

Identified uses For industry use only. Food additives -> Flavoring Agents
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:107-31-3 SDS

107-31-3Synthetic route

Dimethoxymethane
109-87-5

Dimethoxymethane

A

Dimethyl ether
115-10-6

Dimethyl ether

B

Methyl formate
107-31-3

Methyl formate

Conditions
ConditionsYield
With titanium(IV) fluoride In chloroform-d1; dichloromethane at 24.84℃; for 48h;
With calcined hydrogen type ferrierite base having a silica-alumina ratio is 10: 1 at 150℃; under 15001.5 Torr; Reagent/catalyst; Temperature; Pressure; Inert atmosphere;
With MCC-22 at 90℃; under 750.075 Torr; Temperature; Pressure; Reagent/catalyst; Autoclave; Industrial scale;
With H-type MCM-22 In water at 90℃; under 750.075 Torr; Reagent/catalyst; Temperature; Pressure;
carbon monoxide
201230-82-2

carbon monoxide

A

methanol
67-56-1

methanol

B

ethanol
64-17-5

ethanol

C

Methyl formate
107-31-3

Methyl formate

D

ethylene glycol
107-21-1

ethylene glycol

Conditions
ConditionsYield
With hydrogen In various solvent(s) at 300℃; under 1471020 Torr; Further byproducts given;
With hydrogen; dicobalt octacarbonyl; dodecacarbonyl-triangulo-triruthenium; tris(1-methylethyl)phosphine In toluene at 270℃; under 1520000 Torr; for 1h; Yield given. Yields of byproduct given;
With 2-hydroxypyridin; hydrogen; acetylacetonatodicarbonylrhodium(l) In various solvent(s) at 230℃; under 1499480 Torr; for 4.5h; Further byproducts given. Title compound not separated from byproducts;A 284 mmol
B 191 mmol
C 52 mmol
D 1000 mmol
With 1-(pyridine-2-yl)ethanol; hydrogen; acetylacetonatodicarbonylrhodium(l) In various solvent(s) at 230℃; under 1499480 Torr; for 4.5h; Further byproducts given. Title compound not separated from byproducts;A 284 mmol
B 191 mmol
C 52 mmol
D 1000 mmol
With hydrogen; dodecacarbonyltetrarhodium(0) In tetrahydrofuran at 230℃; under 1800 Torr; for 1h; Yield given. Further byproducts given. Yields of byproduct given;
methanol
67-56-1

methanol

dihydroxyacetone
96-26-4

dihydroxyacetone

Methyl formate
107-31-3

Methyl formate

Conditions
ConditionsYield
With Cu/Al2O3; dihydrogen peroxide In chloroform at 50℃; for 24h; Reagent/catalyst; Solvent;84%
methanol
67-56-1

methanol

formic acid
64-18-6

formic acid

Methyl formate
107-31-3

Methyl formate

Conditions
ConditionsYield
With sulfuric acid In water for 4h; Reflux;80%
With (triphenylphosphine)gold(I) chloride; oxygen; silver(I) triflimide In dichloromethane-d2 at 25℃; for 12h;55%
methanol
67-56-1

methanol

carbon monoxide
201230-82-2

carbon monoxide

A

formaldehyd
50-00-0

formaldehyd

B

ethanol
64-17-5

ethanol

C

Methyl formate
107-31-3

Methyl formate

Conditions
ConditionsYield
With hydrogen In N,N-dimethyl-formamide at 160℃; under 30003 Torr; for 8h; Inert atmosphere; Autoclave;
methanol
67-56-1

methanol

carbon monoxide
201230-82-2

carbon monoxide

A

formaldehyd
50-00-0

formaldehyd

B

Methyl formate
107-31-3

Methyl formate

C

carbon dioxide
124-38-9

carbon dioxide

Conditions
ConditionsYield
With hydrogen In N,N-dimethyl-formamide at 160℃; under 30003 Torr; for 8h; Inert atmosphere; Autoclave;
methanol
67-56-1

methanol

carbon dioxide
124-38-9

carbon dioxide

Methyl formate
107-31-3

Methyl formate

Conditions
ConditionsYield
Stage #1: carbon dioxide With phenylsilane In N,N-dimethyl acetamide at 50℃; under 22502.3 Torr; for 4h; pH=Ca. 1.2; Autoclave;
Stage #2: methanol In N,N-dimethyl acetamide Pressure; Temperature; Reagent/catalyst;
100%
With hydrogen; HCO2Ru3(CO)10 at 125℃; under 12928.7 Torr; for 24h; Product distribution; other catalysts, various reaction conditions;
With hydrogen; HCO2Ru3(CO)10 at 125℃; under 12928.7 Torr; for 24h; Yield given;
methyl chloroformate
79-22-1

methyl chloroformate

Methyl formate
107-31-3

Methyl formate

Conditions
ConditionsYield
With ammonium chloride; lithium hexamethyldisilazane In tetrahydrofuran; ethyl acetate91%
Dimethyl ether
115-10-6

Dimethyl ether

carbon monoxide
201230-82-2

carbon monoxide

A

methanol
67-56-1

methanol

B

Methyl formate
107-31-3

Methyl formate

C

acetic acid methyl ester
79-20-9

acetic acid methyl ester

D

acetic acid
64-19-7

acetic acid

Conditions
ConditionsYield
With 25 wt.percent Heteropoly acids supported on SBA-15 In ethanol at 200℃; under 11251.1 Torr; for 1.5h;
methanol
67-56-1

methanol

formaldehyd
50-00-0

formaldehyd

Methyl formate
107-31-3

Methyl formate

Conditions
ConditionsYield
With oxygen In water at 20℃; Reagent/catalyst; Irradiation;16%
Dimethyl ether
115-10-6

Dimethyl ether

A

methanol
67-56-1

methanol

B

formaldehyd
50-00-0

formaldehyd

C

Dimethoxymethane
109-87-5

Dimethoxymethane

D

Methyl formate
107-31-3

Methyl formate

Conditions
ConditionsYield
With nitrogen; oxygen at 239.84℃; Conversion of starting material;A 19.4%
B 79%
C 0.1%
D 1.6%
With nitrogen; oxygen at 199.84 - 259.84℃; Rate constant;A 17.3%
B 69.2%
C 0%
D 1.6%
With nitrogen; oxygen at 239.84℃; Conversion of starting material;A 22.4%
B 60.1%
C 0%
D 5%
(formoxymethyl)dimethylmethoxysilane
1324010-88-9

(formoxymethyl)dimethylmethoxysilane

A

Methyl formate
107-31-3

Methyl formate

B

2,2,5,5-tetramethyl-1,4-dioxa-2,5-disilacyclohexane
5895-82-9

2,2,5,5-tetramethyl-1,4-dioxa-2,5-disilacyclohexane

Conditions
ConditionsYield
With tetrabutoxytitanium at 120℃; under 270.027 Torr; for 7h; Inert atmosphere;A 55 mmol
B 42%
methanol
67-56-1

methanol

formaldehyd
50-00-0

formaldehyd

A

Methyl formate
107-31-3

Methyl formate

B

hydrogen
1333-74-0

hydrogen

Conditions
ConditionsYield
With (PdO)n loaded on TiO2 In water at 20℃; Irradiation; Inert atmosphere;A 6.1%
B 6.7%
methanol
67-56-1

methanol

carbon monoxide
201230-82-2

carbon monoxide

Methyl formate
107-31-3

Methyl formate

Conditions
ConditionsYield
With sodium sulfide In benzene at 80℃; under 75006 Torr; for 1h; Product distribution; Further Variations:; Reagents; Solvents; Temperatures; Pressures;85%
sodium methylate at 84 - 160℃; under 71257.1 - 112511 Torr; Product distribution / selectivity;52%
potassium methanolate at 72 - 100℃; under 71257.1 - 94509.5 Torr; Product distribution / selectivity;47.6%
methanol
67-56-1

methanol

A

formaldehyd
50-00-0

formaldehyd

B

Methyl formate
107-31-3

Methyl formate

Conditions
ConditionsYield
Cu(II)-TSM at 400℃; Product distribution; investigation of activities of various catalysts for the dehydrogenation; various temperatures;A 80%
B 6.7%
With hydrogen at 230℃; under 760.051 Torr;A n/a
B 3.5%
at 350℃; Leiten ueber MgO+CdO+Cr2O3;
carbon monoxide
201230-82-2

carbon monoxide

A

propan-1-ol
71-23-8

propan-1-ol

B

ethanol
64-17-5

ethanol

C

Methyl formate
107-31-3

Methyl formate

D

ethylene glycol
107-21-1

ethylene glycol

Conditions
ConditionsYield
With 2-hydroxypyridin; hydrogen; acetylacetonatodicarbonylrhodium(l) In various solvent(s) at 230℃; under 1499480 Torr; for 4.5h; Further byproducts given. Title compound not separated from byproducts;A 121 mmol
B 191 mmol
C 52 mmol
D 1000 mmol
carbon monoxide
201230-82-2

carbon monoxide

A

ethanol
64-17-5

ethanol

B

Methyl formate
107-31-3

Methyl formate

C

propyl methanoate
110-74-7

propyl methanoate

D

ethylene glycol
107-21-1

ethylene glycol

Conditions
ConditionsYield
With 2-hydroxypyridin; hydrogen; acetylacetonatodicarbonylrhodium(l) In various solvent(s) at 230℃; under 1499480 Torr; for 4.5h; Further byproducts given. Title compound not separated from byproducts;A 191 mmol
B 52 mmol
C 29 mmol
D 1000 mmol
methanol
67-56-1

methanol

glycolic acid ; magnesium glycolate

glycolic acid ; magnesium glycolate

ethylene glycol
107-21-1

ethylene glycol

A

Dimethyl oxalate
553-90-2

Dimethyl oxalate

B

glycolide
502-97-6

glycolide

C

glycolic acid methyl ester
96-35-5

glycolic acid methyl ester

D

ethylene glycol monoformate
628-35-3

ethylene glycol monoformate

E

Methyl formate
107-31-3

Methyl formate

F

ethylene glycol glycolate
14396-72-6

ethylene glycol glycolate

G

oxalic acid
144-62-7

oxalic acid

Conditions
ConditionsYield
Stage #1: methanol; ethylene glycol With oxygen at 90℃; under 3750.38 Torr; for 5h; Autoclave;
Stage #2: glycolic acid ; magnesium glycolate In methanol at 80℃; for 2h; Autoclave;
Dimethoxymethane
109-87-5

Dimethoxymethane

Methyl formate
107-31-3

Methyl formate

Conditions
ConditionsYield
With hydrogen-type ferrierite (Si/Al = 10) at 150℃; under 15001.5 Torr; Reagent/catalyst; Temperature; Pressure;
With oxygen In water at 30 - 150℃; Reagent/catalyst; Irradiation;
methanol
67-56-1

methanol

formaldehyd
50-00-0

formaldehyd

A

Dimethoxymethane
109-87-5

Dimethoxymethane

B

Dimethyl ether
115-10-6

Dimethyl ether

C

Methyl formate
107-31-3

Methyl formate

Conditions
ConditionsYield
With amberlyst-15; MCM-22 In water at 90℃; under 750.075 Torr; Reagent/catalyst; Temperature; Pressure;
methanol
67-56-1

methanol

Methyl formate
107-31-3

Methyl formate

Conditions
ConditionsYield
With lithium tetrafluoroborate; carbonyl hydridoformate bis[2-(diisopropylphosphino)ethyl]amine iron(II) In ethyl acetate for 4.41667h; Catalytic behavior; Reagent/catalyst; Solvent; Inert atmosphere; Schlenk technique; Sealed tube; Reflux;99%
With oxygen at 249.84℃; for 2h; Reagent/catalyst; Temperature; Flow reactor;74%
With oxygen at 80℃; Catalytic behavior; Temperature; Reagent/catalyst; Gas phase;62%
Dimethyl ether
115-10-6

Dimethyl ether

A

methanol
67-56-1

methanol

B

formaldehyd
50-00-0

formaldehyd

C

Methyl formate
107-31-3

Methyl formate

Conditions
ConditionsYield
With nitrogen; oxygen at 240℃; Conversion of starting material;A 14.72%
B 84.96%
C 0.26%
With nitrogen; oxygen at 239.84℃; Conversion of starting material;A 19.5%
B 79.9%
C 1.6%
With nitrogen; oxygen at 239.84℃; Conversion of starting material;A 22.1%
B 76.3%
C 1.5%
Dimethoxymethane
109-87-5

Dimethoxymethane

A

methanol
67-56-1

methanol

B

Methyl formate
107-31-3

Methyl formate

C

methoxymethyl formate
4382-75-6

methoxymethyl formate

D

carbonic acid dimethyl ester
616-38-6

carbonic acid dimethyl ester

Conditions
ConditionsYield
With N-hydroxyphthalimide; oxygen; chlorobenzene; silica gel In acetonitrile under 60006 Torr; for 2h; Product distribution / selectivity;
With N-hydroxyphthalimide; oxygen; chlorobenzene; 2 molepercent solid CuO In acetonitrile under 60006 Torr; for 2h; Product distribution / selectivity;
With N-hydroxyphthalimide; oxygen; chlorobenzene; 2percentCuNi-org/SiO2 In acetonitrile at 100℃; under 30003 Torr; for 3h; Product distribution / selectivity;
methanol
67-56-1

methanol

carbon monoxide
201230-82-2

carbon monoxide

A

Methyl formate
107-31-3

Methyl formate

B

carbon dioxide
124-38-9

carbon dioxide

C

carbonic acid dimethyl ester
616-38-6

carbonic acid dimethyl ester

Conditions
ConditionsYield
With oxygen at 119.84℃; under 760.051 Torr; Reagent/catalyst; Flow reactor;
formic acid
64-18-6

formic acid

Methyl formate
107-31-3

Methyl formate

Conditions
ConditionsYield
With oxygen In water Reagent/catalyst; Irradiation;13.2%
methanol
67-56-1

methanol

A

Dimethoxymethane
109-87-5

Dimethoxymethane

B

Methyl formate
107-31-3

Methyl formate

Conditions
ConditionsYield
With PHTHALIMAX S4 vanadia-titania catalyst; oxygen at 139.84℃; under 760.051 Torr; Inert atmosphere;A 38%
B n/a
at 150℃; for 18h; Product distribution;A 0.72 mmol
B 2.24 mmol
chloro(cyclopentadienyl)bis(triphenylphosphine)ruthenium (II) at 20℃; Product distribution; Further Variations:; Catalysts; Electrolysis;
Dimethoxymethane
109-87-5

Dimethoxymethane

A

Methyl formate
107-31-3

Methyl formate

B

hydrogen
1333-74-0

hydrogen

Conditions
ConditionsYield
With (PdO)n loaded on TiO2 In water Irradiation; Inert atmosphere;A 6%
B 6.4%

107-31-3Relevant articles and documents

Effects of the MoO3 structure of Mo-Sn catalysts on dimethyl ether oxidation to methyl formate under mild conditions

Liu, Guangbo,Zhang, Qingde,Han, Yizhuo,Tsubaki, Noritatsu,Tan, Yisheng

, p. 1057 - 1064 (2015)

The selective oxidation of dimethyl ether (DME) to methyl formate (MF) was conducted in a fixed-bed reactor over the MoO3-SnO2 catalysts with different Mo/Sn ratios. The MF selectivity reached 94.1% and the DME conversion was 33.9% without the formation of COx over the MoSn catalyst at 433 K. The catalysts were deeply characterized by NH3-TPD, CO2-TPD, BET, XPS and H2-TPR. The characterization results showed that different compositions of catalysts obviously affected the surface properties of the catalysts, but the valence of the metal hardly changed with the Mo/Sn ratios. Raman spectroscopy, XRD and XAFS were further used to characterize the structure of the catalysts. The results indicated that the catalyst composition exerted a significant influence on the structure of MoO3. The formation of oligomeric MoO3 and the appropriate coordination numbers of Mo-O at 1.94 ? are the main reasons for the distinct high catalytic activity of the MoSn catalyst. This journal is

Cu Sub-Nanoparticles on Cu/CeO2 as an Effective Catalyst for Methanol Synthesis from Organic Carbonate by Hydrogenation

Tamura, Masazumi,Kitanaka, Takahisa,Nakagawa, Yoshinao,Tomishige, Keiichi

, p. 376 - 380 (2016)

Cu/CeO2 works as an effective heterogeneous catalyst for hydrogenation of dimethyl carbonate to methanol at 433 K and even at low H2 pressure of 2.5 MPa, and it provided 94% and 98% methanol yield based on the carbonyl and total produced methanol, respectively. This is the first report of high yield synthesis of methanol from DMC by hydrogenation with H2 over heterogeneous catalysts. Characterization of the Cu/CeO2 catalyst demonstrated that reduction of Cu/CeO2 produced Cu metal with 2 surface, which is responsible for the high catalytic performance.

Synergetic Behavior of TiO2-Supported Pd(z)Pt(1-z) Catalysts in the Green Synthesis of Methyl Formate

Baldovino-Medrano, Víctor G.,Pollefeyt, Glenn,Bliznuk, Vitaliy,Van Driessche, Isabel,Gaigneaux, Eric M.,Ruiz, Patricio,Wojcieszak, Robert

, p. 1157 - 1166 (2016)

Methyl formate (MF) is a valuable platform molecule, the industrial production of which is far from being green. In this contribution, TiO2-supported Pd(z)Pt(1-z) catalysts were found to be effective in the green synthesis of methyl formate (MF) - at T=323 K and ambient pressure - through methanol (MeOH) oxidation. Two series of catalysts with similar bulk Pd/(Pd+Pt) molar ratios, z, were prepared; one by a water-in-oil microemulsion (MicE) method and the other by an incipient wetness impregnation (IWI). The MicE method led to more efficient catalysts owing to a weak influence of z on particle size distributions and nanoparticles composition. Pd(z)Pt(1-z)-MicE catalysts exhibited strong synergistic effects for MF production but weak synergistic effects for MeOH conversion. The catalytic performance of Pd(z)Pt(1-z)-MicE was superior to that of Pd(z)Pt(1-z)-IWI catalysts despite the latter displaying synergetic effects during the reaction. The catalytic behavior of TiO2-supported Pd(z)Pt(1-z) catalysts was explained from correlations between XRD, TEM, and X-ray photoelectron spectroscopy characterizations.

The mechanism of dimethyl carbonate synthesis on Cu-exchanged zeolite Y

Zhang, Yihua,Bell, Alexis T.

, p. 153 - 161 (2008)

The mechanism of dimethyl carbonate (DMC) synthesis from oxidative carbonylation of methanol over Cu-exchanged Y zeolite has been investigated using in situ infrared spectroscopy and mass spectrometry under transient-response conditions. The formation of DMC is initiated by reaction of molecularly adsorbed methanol with oxygen to form either mono- or di-methoxide species bound to Cu+ cations. Reaction of the mono-methoxide species with CO produces monomethyl carbonate (MMC) species. DMC is formed via two distinct reaction pathways-CO addition to di-methoxide species or by reaction of methanol with MMC. The rate-limiting step in DMC synthesis is found to be the reaction of CO with mono-methoxide or di-methoxide species. The first of these reactions produces MMC, which then reacts rapidly with methanol to produce DMC, whereas the second of these reactions produces DMC directly. Formaldehyde was identified as an intermediate in the formation of dimethoxy methane (DMM) and methyl formate (MF). Both byproducts are thought to form via a hemiacetal intermediate produced by the reaction of methanol with adsorbed formaldehyde at a Cu+ site.

Study of thermolysis of peroxyacetals and peroxycetals

Helgorsky,Saux,Degueil-Castaing,Maillard

, p. 8263 - 8274 (1996)

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Structural and reactive relevance of V + Nb coverage on alumina of V{single bond}Nb{single bond}O/Al2O3 catalytic systems

Lewandowska, Anna E.,Banares, Miguel A.,Ziolek, Maria,Khabibulin, Dzhalil F.,Lapina, Olga B.

, p. 94 - 103 (2008)

Vanadium and niobium species (together and separately) were loaded on gamma alumina, and the resulting catalysts were run in the methanol conversion. This reaction was studied by both GC analysis and FTIR study in the flow system. The catalytic properties are discussed based on the combined FTIR and 27Al, 51V and 1H MAS NMR studies. The NMR studies revealed a different mechanism of interaction between Nb and Al2O3 than that between V and Al2O3. This predetermines the structure of vanadium sites in bimetallic VNb/Al samples. The effect of coverage was considered for various metal loadings ranging from below to above monolayer. One of our most interesting findings is that the surface Nb oxide species exhibited a redox character below monolayer but were acidic above monolayer. 27Al MAS NMR revealed a strong alumina-Nb interaction that may account for its redox performance. Moreover, the role of sulfate from vanadium precursor is evidenced.

The new catalytic property of supported rhenium oxides for selective oxidation of methanol to methylal

Yuan, Youzhu,Shido, Takafumi,Iwasawa, Yasuhiro

, p. 1421 - 1422 (2000)

A new catalytic property of supported rhenium oxides has been found for selective methanol oxidation to methylal; high performances for the selective catalytic oxidation are observed with V2O5-, ZrO2-, Fe2O3- and TiO2-supported Reoxide catalysts, which are characterized by pulse experiments, XRD and XPS.

Novel anion exchange resin-based catalyst for liquid-phase methanol synthesis at 373-393 K

Aika, Ken-Ichi,Kobayashi, Hidenobu,Harada, Kenji,Inazu, Koji

, p. 1252 - 1253 (2004)

A thermo-stable anion exchange resin-Raney Cu system was found as the most effective solid catalyst for low-temperature liquid-phase methanol synthesis at 373 to 393 K under 5.0 MPa of syngas (2H2/CO). With the catalyst (20 mL of the resin and 2.0 g of Cu) suspended in methanol solution 72% of CO was converted to methanol (70%) and methyl formate (HCOOCH3) (30%) in 4 h.

Vapor-phase dehydrogenation of methanol to methyl formate in catalytic membrane reactor with Pd/SiO2/ceramic composite membrane

Guo, Yanglong,Lu, Guanzhong,Mo, Xunhua,Wang, Yunsong

, p. 1628 - 1629 (2004)

Vapor-phase dehydrogenation of methanol to methyl formate was investigated in the catalytic membrane reactor (CMR) with the Pd/SiO2/ceramic composite membrane prepared by an impregnation method. The studies show that the CMR has much better performance than the fixed-bed reactor, in which no methyl formate is detected under the similar reaction conditions. Copyright

Zirconia-supported MoOx catalysts for the selective oxidation of dimethyl ether to formaldehyde: Structure, redox properties, and reaction pathways

Liu, Haichao,Cheung, Patricia,Iglesia, Enrique

, p. 4118 - 4127 (2003)

Dimethyl ether (DME) reacts to form formaldehyde with high selectivity at 500-600 K on MoOx-ZrO2 catalysts with a wide range of MoOx surface density (0.5-50.1 Mo/nm2) and local structure (monomers, oligomers, MoO3 crystallites, and ZrMo2O8). Reaction rates (per Mo-atom) increased markedly as MoOx surface density increased from 2.2 to 6.4 Mo/nm2 and two-dimensional polymolybdates and MoO3 clusters became the prevalent active species. The rate of incipient stoichiometric reduction of MoOx-ZrO2 samples in H2 also increased with increasing MoOx surface density, suggesting that catalytic turnovers involve redox cycles that become faster as the size and dimensionality of MoOx domains increase. DME reaction rates (per Mo-atom) decreased as MoOx surface densities increased above 6.4 Mo/nm2, as MoO3 and ZrMo2O8 clusters with increasingly inaccessible MoOx species form. On MoOx and ZrMo2O8, areal reaction rates reach a constant value at MoOx surface densities above 10 Mo/nm2, as the exposed surfaces become covered with the respective active species. ZrMo2O8 surfaces were more reducible in H2 than MoOx surfaces and showed higher areal reaction rates. Reaction rates were nearly independent of O2 pressure, but the reaction order in DME decreased from one at low pressures (60 kPa). DME reacts via primary pathways leading to HCHO, methyl formate, and COx, with rate constants k1, k2, and k3, respectively, and via secondary HCHO conversion to methylformate (k4) and COx (k5). Primary HCHO selectivities (and k1/(k2 + k3) ratios) increased with increasing MoOx surface density on MoOx-containing samples and reached values of 80-90% above 10 Mo/nm2. Kinetic ratios relevant to secondary HCHO reactions (k1/[(k4 + k5)CAO]; CAO inlet DME concentration) also increased with increasing MoOx surface density to values of a??0.1 and 0.8 on MoOx and ZrMo2O8 structures (at the constant inlet DME concentration CAO), respectively. Thus, increasing the coverage of ZrO2 surfaces with MoOx or ZrMo2O8 leads to more selective structures for HCHO synthesis from DME.

Ozone-activated nanoporous gold: A stable and storable material for catalytic oxidation

Personick, Michelle L.,Zugic, Branko,Biener, Monika M.,Biener, Juergen,Madix, Robert J.,Friend, Cynthia M.

, p. 4237 - 4241 (2015)

We report a new method for facile and reproducible activation of nanoporous gold (npAu) materials of different forms for the catalytic selective partial oxidation of alcohols under ambient pressure, steady flow conditions. This method, based on the surface cleaning of npAu ingots with ozone to remove carbon documented in ultrahigh vacuum conditions, produces active npAu catalysts from ingots, foils, and shells by flowing an ozone/dioxygen mixture over the catalyst at 150 °C, followed by a temperature ramp from 50 to 150 °C in a flowing stream of 10% methanol and 20% oxygen. With this treatment, all three materials (ingots, foils, and shells) can be reproducibly activated, despite potential carbonaceous poisons resulting from their synthesis, and are highly active for the selective oxidation of primary alcohols over prolonged periods of time. The npAu materials activated in this manner exhibit catalytic behavior substantially different from those activated under different conditions previously reported. Once activated in this manner, they can be stored and easily reactivated by flow of reactant gases at 150 °C for a few hours. They possess improved selectivity for the coupling of higher alcohols, such as 1-butanol, and are not active for carbon monoxide oxidation. This ozone-treated npAu is a functionally new catalytic material.

Levulinic esters from the acid-catalysed reactions of sugars and alcohols as part of a bio-refinery

Hu, Xun,Li, Chun-Zhu

, p. 1676 - 1679 (2011)

Polymeric humin formation greatly diminishes levulinic acid yields in acid treatment of C6 sugars in aqueous medium. Protecting reactive functional groups of sugars and reaction intermediates via acetalisation and etherification in methanol medium effectively suppresses humin formation and remarkably enhances the production of levulinic esters.

ANIONIC GROUP 6B METAL CARBONYLS AS HOMOGENEOUS CATALYSTS FOR CARBON DIOXIDE/HYDROGEN ACTIVATION. THE PRODUCTION OF ALKYL FORMATES.

Darensbourg,Ovalles

, p. 3750 - 3754 (1984)

The production of alkyl formates from the hydrocondensation of carbon dioxide in alcohols utilizing anionic group 6B carbonyl hydrides as catalysts is reported. HM(CO)//5** minus (M equals Cr, W; derived from mu -H left bracket M//2(CO)//1//0 right bracket ** minus ) and their products of carbon dioxide insertion, HCO//2M(CO)//5** minus , have been found to be effective catalysts for the hydrogenation of CO//2 in alcohols under rather mild conditions (loading pressures of CO//2 and H//2, 250 psi each, and 125 degree C) to provide alkyl formates. The only metal carbonyl species detected in solution via infrared spectroscopy, both at the end of a catalytic period and during catalysis, were M(CO)//6 and HCO//2M(CO)//5** minus .

Photocatalytic cross-coupling of methanol and formaldehyde on a rutile TiO2(110) surface

Yuan, Qing,Wu, Zongfang,Jin, Yuekang,Xu, Lingshun,Xiong, Feng,Ma, Yunsheng,Huang, Weixin

, p. 5212 - 5219 (2013)

The photocatalytic oxidation of methanol on a rutile TiO2(110) surface was studied by means of thermal desorption spectroscopy (TDS) and X-ray photoelectron spectroscopy (XPS). The combined TDS and XPS results unambiguously identify methyl formate as the product in addition to formaldehyde. By monitoring the evolution of various surface species during the photocatalytic oxidation of methanol on TiO2(110), XPS results give direct spectroscopic evidence for the formation of methyl formate as the product of photocatalytic cross-coupling of chemisorbed formaldehyde with chemisorbed methoxy species and clearly demonstrate that the photocatalytic dissociation of chemisorbed methanol to methoxy species occurs and contributes to the photocatalytic oxidation of methanol. These results not only greatly broaden and deepen the fundamental understanding of photochemistry of methanol on the TiO2 surface but also demonstrate a novel green and benign photocatalytic route for the synthesis of esters directly from alcohols or from alcohols and aldehydes.

A comparative study on the effect of Zn addition to Cu/Ce and Cu/Ce-Al catalysts in the steam reforming of methanol

Mrad, Mary,Hammoud, Dima,Gennequin, Cédric,Abouka?s, Antoine,Abi-Aad, Edmond

, p. 84 - 90 (2014)

The performances of different catalysts xCu10Ce and xCu10Ce10Al (with x = 1, 3 and 5) in the steam reforming of methanol reaction were studied with and without the presence of zinc. The reaction was investigated at 350°C with a Gas Hourly Space Velocity o

The direct synthesis of dimethyl carbonate by the oxicarbonylation of methanol over Cu supported on carbon nanotube

Merza,László,Oszkó,Pótári,Baán,Erdohelyi

, p. 117 - 124 (2014)

The activity of Cu/MWCNT and Cu-Ni/MWCNT catalysts was investigated in the synthesis of dimethyl carbonate (DMC) by oxidative carbonylation of methanol. The catalysts were prepared via conventional incipient wetness impregnation technique. The samples were characterized by X-ray photoelectron spectroscopy (XPS), and DRIFT. The reaction was carried out in a continuous flow system at atmospheric pressure at 393 K. The main products were methyl formate (MF), DMC and CO2. The methanol conversion on Cu/MWCNT achieved a steady state value after 2 h, but on Cu-Ni/MWCNT the conversion decreased continuously. The DMC selectivity was more than 30% and the yield was 1.2% on Cu/MWCNT. Based on the XPS data we can establish that copper reduced to its metallic form during reduction but oxidized in the reaction mixture, and is mostly in the Cu + state, with some Cu2+ also present on the surface at the beginning of the reaction though its ratio decreased in time. We assume that the DMC formation rate depends on the surface concentration of oxidized Cu. Based upon the FTIR data adsorbed DMC is present on the surface of the Cu/MWCNT catalyst during the catalytic reaction but on Cu-Ni/MWCNT sample only methyl formate was detected in the gas phase.

Low-temperature CO2 hydrogenation to liquid products via a heterogeneous cascade catalytic system

Chen, Yuan,Choi, Saemin,Thompson, Levi T.

, p. 1717 - 1725 (2015)

Research described in this paper targeted a cascade system for the hydrogenation of CO2 to methanol via formic acid and/or formate intermediates, a reaction sequence that has been accomplished previously using homogeneous catalysts. On the basis of results for the hydrogenation of CO2, formic acid, and ethyl formate over a series of Cu- and Mo2C-based catalysts, we selected a Cu chromite catalyst for CO2 hydrogenation to the formate and a Cu/Mo2C catalyst to convert the formate to methanol. These catalysts worked cooperatively in the presence of ethanol, yielding a methanol turnover frequency of 4.7 × 10-4 s-1 at 135 °C, 10 bar of CO2, and 30 bar of H2 in 1,4-dioxane. The performance for this Cu chromite:Cu/Mo2C cascade system surpassed the additive production of the individual catalysts by 60%. The results also allowed an investigation of the reaction pathways. The hydrogenation of CO2 to formic acid appeared to be the rate-limiting step for most of the catalysts. This is not surprising given the thermodynamics for this reaction. Finally, the hydrogenation of CO2 to dimethyl ether was also demonstrated using a system consisting of the Cu/Mo2C catalyst to produce methanol from CO2 and HZSM-5 to produce dimethyl ether from methanol. The systems described in this paper are, to our knowledge, the first demonstrating cascade CO2 hydrogenation via heterogeneous catalysts.

Hydrogenation of carbon dioxide in the presence of rhodium catalysts

Kolesnichenko,Ezhova,Kremleva,Slivinskii

, p. 2542 - 2545 (2004)

The results of CO2 hydrogenation in the presence of the Wilkinson complexes, viz., RhCl3 and acacRh(CO)2, at room temperature and excess PPh3 are presented. The influence of different ions on the catalytic properties of the Rh complexes was studied. Methanol and methyl formate are formed along with formic acid in the presence of an inorganic salt. Ions that are the most active in the formation of formic acid are the least active in methanol formation.

Promotional effect of potassium salt in low-temperature formate and methanol synthesis from CO/CO2/H2 on copper catalyst

Zhao, Tian-Sheng,Yoneyama, Yoshiharu,Fujimoto, Kaoru,Yamane, Nodyuki,Fujimoto, Kenichiro,Tsubaki, Noritatsu

, p. 734 - 735 (2007)

Alkyl formates can be formed from CO2-containing syngas with C1-C4 alkyl alcohol solvents in the presence of potassium carbonate, which changed to potassium formate as catalyst. The formates can be in situ hydrogenolysized further to produce methanol effectively over manganese oxide or magnesia-supported copper catalysts. These homogeneous and heterogeneous catalysts constitute a novel system for methanol synthesis from CO/CO2/H2 even at 443 K. Copyright

Catalytic oxidation of alcohol via nickel phosphine complexes with pendant amines

Weiss, Charles J.,Das, Parthapratim,Miller, Deanna L.,Helm, Monte L.,Appel, Aaron M.

, p. 2951 - 2958 (2014)

Nickel complexes were prepared with diphosphine ligands that contain pendant amines, and these complexes catalytically oxidize primary and secondary alcohols to their respective aldehydes and ketones. Kinetic and mechanistic studies of these prospective electrocatalysts were performed to understand what influences the catalytic activity. For the oxidation of diphenylmethanol, the catalytic rates were determined to be dependent on the concentration of both the catalyst and the alcohol and independent of the concentration of base and oxidant. The incorporation of pendant amines to the phosphine ligand results in substantial increases in the rate of alcohol oxidation with more electron-donating substituents on the pendant amine exhibiting the fastest rates. (Chemical Equation Presented).

Oxidation of methanol to methyl formate over supported Pd nanoparticles: Insights into the reaction mechanism at low temperature

Wojcieszak,Karelovic,Gaigneaux,Ruiz

, p. 3298 - 3305 (2014)

Pd nanoparticles supported on TiO2 and SiO2 (2 wt.%) were synthesized by the water-in-oil microemulsion method. The materials were characterized by standard physico-chemical methods (XRD, ICP, TEM, BET, XPS) and DRIFT in operando mode and tested in the gas-phase reaction of methanol oxidation. The direct formation of methyl formate (MF) from methanol was observed. Supported palladium catalysts produced methyl formate at low temperature (2 occurred. The DRIFT-operando study confirmed that methanol is adsorbed mainly in two forms, the undissociated gaseous methanol (via H bond) and dissociatively adsorbed methoxy species (CH3O-) on the surface. Methyl formate is formed already at RT with the maximum at about 80 °C. The mechanism of the formation of methyl formate from methanol at low temperature is discussed. the Partner Organisations 2014.

Simplified DEMS set up for electrocatalytic studies of porous PtRu alloys

Ianniello,Schmidt

, p. 83 - 86 (1995)

A simplified experimental apparatus for Differential Electrochemical Mass Spectrometry (DEMS) was constructed having only one turbomolecular pump and a modified gas inlet system. The setup allows the determination of the activity of porous PtRu electrodes for the electro-oxidation of small organic molecules. Various PtRu alloys with defined composition can be electrodeposited onto porous gold substrates. First results on the electrooxidation of methanol in acid solution were presented.

CuO - Activated carbon catalysts for methanol decomposition to hydrogen and carbon monoxide

Tsoncheva, Tanya,Nickolov, Radostin,Vankova, Svetoslava,Mehandjiev, Dimitar

, p. 1096 - 1100 (2003)

A comparison of the abilities of CuO - activated carbon catalysts, prepared by different copper precursors and preparation techniques, in the methanol decomposition reaction to carbon monoxide and hydrogen, was undertaken. Higher catalytic activity and stability are found for the catalysts obtained from an ammonia solution of copper carbonate. The nature of the catalytic active complex in the samples is also discussed.

Selective oxidation of methanol to methyl formate on catalysts of Au-Ag alloy nanoparticles supported on titania under UV irradiation

Han, Chenhui,Yang, Xuzhuang,Gao, Guanjun,Wang, Jie,Lu, Huailiang,Liu, Jie,Tong, Min,Liang, Xiaoyuan

, p. 3603 - 3615 (2014)

We find that the Au-Ag alloy nanoparticles supported on titania exhibit superior methanol conversion and methyl formate selectivity for selective oxidation of methanol by low partial pressure oxygen in air under UV irradiation in the 15°C-45°C temperature range, with the highest methanol conversion above 90% and the highest selectivity towards methyl formate above 85%. The only by-product definitely detected is CO2. The superior photocatalytic performance of the catalyst is closely related to the special structure of the catalyst and the electronic properties of the alloy, which reduce the recombination of the photo-excited electron-hole pairs by transferring the photo-excited electrons in time from the conduction band of titania to the alloy on the one hand, and elevate the negative charge level of the alloy surface by the spd hybridization, the formation of Schottky barriers, the electron transfer from the conduction band of titania to the metal as well as the interband and intraband electron transitions under UV irradiation on the other hand. The photo-generated holes are responsible for the oxidation from methanol to coordinated methoxy, from coordinated methoxy to coordinated formaldehyde and finally to carbon dioxide. The methyl formate selectivity is dependent on the density of the surface methoxy. To enhance the efficiency of electron-hole separation is beneficial to the formation of the coordinated methoxy and coordinated formaldehyde and thus the selectivity to methyl formate. The negative charges on the surface of the metal are responsible for the dissociation of oxygen, which is the rate-determining step in the reaction. The dissociative oxygen repels the water molecules formed from the surface hydroxyls and refills the oxygen vacancies on the surface of titania. The surface oxygen is the acceptor of the hydrogen dissociated from methanol and/or methoxy and thus is beneficial for the formation of the coordinated methoxy and coordinated formaldehyde. The oxygen partial pressure remarkably influences the methanol conversion and the methyl formate selectivity. The light intensity has a remarkable impact on the methanol conversion but not on the methyl formate selectivity. These findings provide useful insight into the design of catalysts for selective oxidation of methanol to methyl formate in a more green way. This journal is the Partner Organisations 2014.

RuO2 clusters within LTA zeolite cages: Consequences of encapsulation on catalytic reactivity and selectivity

Zhan, Bi-Zeng,Iglesia, Enrique

, p. 3697 - 3700 (2007)

(Figure Presented) Trapped! The title system (ca. 1 nm diameter; left) catalyzes methanol oxidation with higher turnover rates than clusters on SiO2 supports. Spatial constraints lead to the preferential oxidation of methanol over larger alcohols. Restricted access to active sites also protects encapsulated Ru clusters (right) against inhibition of ethene hydrogenation by organosulfur compounds.

Method for preparing formate by using nitromethane process byproduct formic acid

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Paragraph 0039-0046, (2021/07/08)

The invention belongs to the technical field of organic synthesis, and particularly relates to a method for preparing formate by using a nitromethane process byproduct formic acid. The method comprises the following steps: adding alcohol into a nitromethane hydrolysis reaction solution to carry out esterification reaction, distilling and rectifying to obtain the formate, wherein the nitromethane hydrolysis reaction liquid contains formic acid and hydrochloric acid. The method solves the problems that in the prior art, formic acid is not easy to remove, and the added value of the byproduct calcium formate is low, and the byproduct formic acid can be fully recycled by adopting the esterification reaction of the low-carbon alcohol and the byproduct formic acid; the used low-carbon alcohol is ethanol or methanol, and the esterification product is low in boiling point and easy to separate; and the produced methyl formate and ethyl formate are high in added value and wide in application.

The facet effect of ceria nanoparticles on platinum dispersion and catalytic activity of methanol partial oxidation

Choi, Hanseul,Choi, Minkee,Kim, Daeho,Park, Jeong Young,Reddy, Kasala Prabhakar,Ryoo, Ryong

supporting information, p. 7382 - 7385 (2021/08/03)

The effect of platinum-supported nano-shaped ceria catalysts on methanol partial oxidation and methyl formate product selectivity has been investigated. A Pt-supported CeO2nanocube catalyst had a higher turnover frequency than nanosphere catalysts; however, nanosphere catalysts showed higher selectivity towards methyl formate. The observed ceria shape effect in catalysis was associated with the shape-dependent Pt dispersion and its oxidation states. Furthermore,in situstudies revealed that the reduced platinum and mono-dentate methoxy group were responsible for the higher turnover frequency.

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