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Glyceric acid, also known as glycollic acid or hydroxyacetic acid, is a natural three-carbon sugar acid. It is a colorless, odorless, and hygroscopic liquid that is soluble in water. Salts and esters of glyceric acid are known as glycerates.

473-81-4

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473-81-4 Usage

Uses

Used in Food Industry:
Glyceric acid is used as a flavor enhancer and acidity regulator in the food industry. It helps to improve the taste and texture of various food products, such as beverages, confectionery, and baked goods.
Used in Pharmaceutical Industry:
Glyceric acid is used as a pharmaceutical intermediate for the synthesis of various drugs, such as antibiotics, anti-inflammatory agents, and anti-cancer drugs. It also serves as a buffering agent in the formulation of pharmaceutical products.
Used in Cosmetics Industry:
Glyceric acid is used as a humectant and skin conditioning agent in cosmetics and personal care products. It helps to maintain the moisture balance of the skin and improve its overall appearance.
Used in Agriculture:
Glyceric acid is used as a plant growth regulator and fertilizer additive in agriculture. It promotes plant growth and enhances the nutritional value of crops.
Used in Chemical Industry:
Glyceric acid is used as a raw material in the synthesis of various chemicals, such as glycerol, glycerol esters, and polyglycerols. It also serves as a chelating agent and sequestrant in various chemical processes.
Used in Textile Industry:
Glyceric acid is used as a dye fixative and fabric softener in the textile industry. It helps to improve the colorfastness of dyed fabrics and provides a soft, smooth finish to textiles.
Used in Paper Industry:
Glyceric acid is used as a sizing agent and wet-end additive in the paper industry. It enhances the strength and durability of paper products and improves their resistance to water and ink.
Used in Detergent and Cleaning Industry:
Glyceric acid is used as a builder and chelating agent in detergents and cleaning products. It helps to remove stains and dirt effectively and prevents the formation of scale and deposits.
Used in Biotechnology:
Glyceric acid is used as a substrate for the production of various biotechnological products, such as enzymes, proteins, and biofuels. It also serves as a carbon source for the growth of microorganisms in fermentation processes.

Check Digit Verification of cas no

The CAS Registry Mumber 473-81-4 includes 6 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 3 digits, 4,7 and 3 respectively; the second part has 2 digits, 8 and 1 respectively.
Calculate Digit Verification of CAS Registry Number 473-81:
(5*4)+(4*7)+(3*3)+(2*8)+(1*1)=74
74 % 10 = 4
So 473-81-4 is a valid CAS Registry Number.
InChI:InChI=1/C3H6O4/c4-1-2(5)3(6)7/h2,4-5H,1H2,(H,6,7)/t2-/m1/s1

473-81-4SDS

SAFETY DATA SHEETS

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

Version: 1.0

Creation Date: Aug 18, 2017

Revision Date: Aug 18, 2017

1.Identification

1.1 GHS Product identifier

Product name glyceric acid

1.2 Other means of identification

Product number -
Other names DL-2,3-Dihydroxypropionic Acid

1.3 Recommended use of the chemical and restrictions on use

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

1.4 Supplier's details

1.5 Emergency phone number

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

More Details:473-81-4 SDS

473-81-4Synthetic route

Glyceraldehyde
56-82-6

Glyceraldehyde

glyceric acid
473-81-4

glyceric acid

Conditions
ConditionsYield
With 1 wt% Au/TiO2; oxygen In water at 75℃; under 39547.2 Torr; for 3022h; Time; Flow reactor;100%
With sodium chlorite; dimethyl sulfoxide In aq. phosphate buffer at 0 - 20℃; pH=4;93%
With iodine; sodium carbonate
glycerol
56-81-5

glycerol

glyceric acid
473-81-4

glyceric acid

Conditions
ConditionsYield
Stage #1: glycerol With Rh(OTf)(trop2NH)(PPh3); water; cyclohexanone; sodium hydroxide at 20℃; for 8h; Inert atmosphere;
Stage #2: With hydrogenchloride In water Inert atmosphere; chemoselective reaction;
98%
With oxygen In water at 60℃; under 7500.75 Torr; Reagent/catalyst;75%
With water; oxygen In water at 24.84℃; under 760.051 Torr; for 6h; Catalytic behavior; Schlenk technique;42%
oxiranyl-methanol
556-52-5

oxiranyl-methanol

glyceric acid
473-81-4

glyceric acid

Conditions
ConditionsYield
Stage #1: oxiranyl-methanol With Rh(OTf)(trop2NH)(PPh3); water; cyclohexanone; sodium hydroxide at 20℃; for 8h; Inert atmosphere;
Stage #2: With hydrogenchloride In water Inert atmosphere;
95%
2-Acetylamino-2,3-dibromo-propionic acid

2-Acetylamino-2,3-dibromo-propionic acid

A

acetamide
60-35-5

acetamide

B

glyceric acid
473-81-4

glyceric acid

Conditions
ConditionsYield
With sodium hydroxide; sodium tetrahydroborate In water for 4h; Product distribution; pH=10.8-11.0;A n/a
B 90%
glycerol
56-81-5

glycerol

A

glycolic Acid
79-14-1

glycolic Acid

B

glyceric acid
473-81-4

glyceric acid

C

dihydroxyacetone
96-26-4

dihydroxyacetone

Conditions
ConditionsYield
With oxygen In water at 60℃; Catalytic behavior; Reagent/catalyst; Autoclave; chemoselective reaction;A 8.9%
B 89.9%
C 6.8%
With oxygen In water at 80℃; under 7500.75 Torr; for 2h; pH=6.7; Reagent/catalyst; Autoclave;
With oxygen In water at 60℃; under 3750.38 Torr; for 24h; Catalytic behavior; Kinetics; Reagent/catalyst; Time; High pressure;A 7.8 %Chromat.
B 55.4 %Chromat.
C 7.7 %Chromat.
glycerol
56-81-5

glycerol

A

formaldehyd
50-00-0

formaldehyd

B

tartronic acid

tartronic acid

C

glyceric acid
473-81-4

glyceric acid

D

dihydroxyacetone
96-26-4

dihydroxyacetone

Conditions
ConditionsYield
With oxygen In water at 60℃; Catalytic behavior; Reagent/catalyst; Autoclave; chemoselective reaction;A n/a
B n/a
C 84.9%
D 6.5%
glycerol
56-81-5

glycerol

A

glyceric acid
473-81-4

glyceric acid

B

dihydroxyacetone
96-26-4

dihydroxyacetone

C

Glyceraldehyde
56-82-6

Glyceraldehyde

Conditions
ConditionsYield
With oxygen In water at 60℃; Catalytic behavior; Reagent/catalyst; Autoclave; chemoselective reaction;A 84.2%
B 9.5%
C 6.3%
With oxygen In water at 60℃; under 760.051 Torr; for 4h; Catalytic behavior;
With Pt-MCM-41 catalyst; oxygen In water at 69.84℃; under 760.051 Torr; pH=Ca. 7; Kinetics; Catalytic behavior; Reagent/catalyst; Temperature;
glycerol
56-81-5

glycerol

A

glyceric acid
473-81-4

glyceric acid

B

Glyceraldehyde
56-82-6

Glyceraldehyde

Conditions
ConditionsYield
With perchloric acid In ethanol at 20℃; pH=1; Concentration; Reagent/catalyst; Electrochemical reaction;A 9%
B 70.6%
With Pseudomonas putida HK-5 pyrroloquinoline quinone-dependent alcohol dehydrogenase; 4,4'-azobis(1-methylpyridinium) bis(methyl sulfate); NADH In aq. buffer for 6h; pH=7.1; Catalytic behavior; Time; Electrolysis; Enzymatic reaction;A 53%
B 15%
With silica-supported platinum; oxygen In water at 89.84℃; for 24h;
glycerol
56-81-5

glycerol

A

tartronic acid
80-69-3

tartronic acid

B

glyceric acid
473-81-4

glyceric acid

C

oxalic acid
144-62-7

oxalic acid

Conditions
ConditionsYield
With water; oxygen In water at 24.84℃; under 760.051 Torr; for 6h; Catalytic behavior; Schlenk technique;A 10%
B 54%
C 5%
With oxygen; sodium hydroxide In water at 59.84℃; under 760.051 Torr; for 7h; Product distribution / selectivity; Closed type batch reactor;A n/a
B 70 %Chromat.
C n/a
With oxygen; sodium hydroxide In water at 60℃; under 2250.23 Torr; for 24h;
glycerol
56-81-5

glycerol

A

LACTIC ACID
849585-22-4

LACTIC ACID

B

glyceric acid
473-81-4

glyceric acid

Conditions
ConditionsYield
With oxygen; sodium hydroxide In water at 70℃; pH=3.56; Temperature; pH-value; Flow reactor;A 38%
B 47.3%
With oxygen; sodium hydroxide In water at 89.84℃; under 760.051 Torr;
With sodium hydroxide at 90℃; under 760.051 Torr; Reagent/catalyst;
With oxygen; sodium hydroxide In water at 50℃; under 2250.23 Torr; Catalytic behavior;
With oxygen; sodium hydroxide at 110℃; under 2250.23 Torr; for 0.5h; Reagent/catalyst;
glycerol
56-81-5

glycerol

A

LACTIC ACID
849585-22-4

LACTIC ACID

B

tartronic acid
80-69-3

tartronic acid

C

glyceric acid
473-81-4

glyceric acid

Conditions
ConditionsYield
With oxygen; sodium hydroxide In water at 85℃; pH=3.56; Temperature; pH-value; Flow reactor;A 46.5%
B 5.5%
C 38.1%
With oxygen; sodium hydroxide In water at 50℃; under 2250.23 Torr; for 4h; Catalytic behavior;
With lithium hydroxide monohydrate at 90℃; under 760.051 Torr; for 6h; Catalytic behavior; Inert atmosphere;
glycerol
56-81-5

glycerol

A

LACTIC ACID
849585-22-4

LACTIC ACID

B

glyceric acid
473-81-4

glyceric acid

C

dihydroxyacetone
96-26-4

dihydroxyacetone

D

acetic acid
64-19-7

acetic acid

E

Glyceraldehyde
56-82-6

Glyceraldehyde

Conditions
ConditionsYield
With oxygen In water at 60℃; under 3750.38 Torr; for 5h; Catalytic behavior; Autoclave;A 45%
B n/a
C n/a
D n/a
E n/a
glycerol
56-81-5

glycerol

A

glycolic Acid
79-14-1

glycolic Acid

B

tartronic acid
80-69-3

tartronic acid

C

glyceric acid
473-81-4

glyceric acid

D

oxalic acid
144-62-7

oxalic acid

Conditions
ConditionsYield
With water; oxygen In water at 24.84℃; under 760.051 Torr; for 6h; Catalytic behavior; Reagent/catalyst; Concentration; Schlenk technique;A 11%
B 13%
C 42%
D 12%
With potassium carbonate In water at 80℃; for 24h;
With water; oxygen; sodium hydroxide at 50℃; under 2280.15 Torr; Reagent/catalyst;
allyl alcohol
107-18-6

allyl alcohol

A

glyceric acid
473-81-4

glyceric acid

B

acrylic acid
79-10-7

acrylic acid

C

3-hydroxypropionic acid
503-66-2

3-hydroxypropionic acid

Conditions
ConditionsYield
With oxygen; sodium hydroxide In water at 50℃; Reagent/catalyst; Sonication;A 6.9%
B 30.1%
C 7.2%
Conditions
ConditionsYield
With copper(II) sulfate at 100℃; Product distribution; Rate constant; Thermodynamic data; study of the oxidation reaction of D-lyxose by cupric ion, kinetic mesurements, ΔS(excit.),;A 14%
B 30%
C 22%
D 15%
E 12%
D-glucose
50-99-7

D-glucose

A

glycolic Acid
79-14-1

glycolic Acid

B

glyceric acid
473-81-4

glyceric acid

Conditions
ConditionsYield
With oxygen In water at 160℃; under 13680.9 Torr; for 20h; Temperature; Pressure; Reagent/catalyst; Green chemistry;A 29.3%
B 17.8%
With oxygen In water at 160℃; under 13680.9 Torr; for 20h;
allyl alcohol
107-18-6

allyl alcohol

A

glyceric acid
473-81-4

glyceric acid

B

3-hydroxypropionic acid
503-66-2

3-hydroxypropionic acid

Conditions
ConditionsYield
With cerium(IV) oxide Reagent/catalyst;A 19%
B 23.2%
With nano gold salt supported on cerium oxideA 10.7%
B 9.4%
glycerol
56-81-5

glycerol

A

glycolic Acid
79-14-1

glycolic Acid

B

glyceric acid
473-81-4

glyceric acid

C

Glyceraldehyde
56-82-6

Glyceraldehyde

Conditions
ConditionsYield
With perchloric acid In ethanol at 20℃; pH=1; Reagent/catalyst; Electrochemical reaction;A 7%
B 7.6%
C 20.3%
Glyceraldehyde
56-82-6

Glyceraldehyde

A

formic acid
64-18-6

formic acid

B

glyceric acid
473-81-4

glyceric acid

Conditions
ConditionsYield
With carbon dioxide; hydrogen; oxygen In water at 30℃; under 8274.59 Torr; for 6h; Catalytic behavior; Reagent/catalyst; Time; Autoclave;A 14%
B 10%
cellulose

cellulose

A

LACTIC ACID
849585-22-4

LACTIC ACID

B

propylene glycol
57-55-6

propylene glycol

C

glyceric acid
473-81-4

glyceric acid

D

D-sorbitol
50-70-4

D-sorbitol

E

ethylene glycol
107-21-1

ethylene glycol

Conditions
ConditionsYield
With hydrogen In water at 240℃; under 30003 Torr; for 1h;A 12.6%
B 11.6%
C 10.2%
D 10.1%
E 9.1%
D-Fructose
57-48-7

D-Fructose

glyceric acid
473-81-4

glyceric acid

Conditions
ConditionsYield
With copper(II) hydroxide; sodium hydroxide
D-Mannose
3458-28-4

D-Mannose

glyceric acid
473-81-4

glyceric acid

Conditions
ConditionsYield
With copper(II) hydroxide; sodium hydroxide
2,3-diaminopropanoic acid
515-94-6

2,3-diaminopropanoic acid

glyceric acid
473-81-4

glyceric acid

Conditions
ConditionsYield
im Tierkoerper;
With cis-nitrous acid
serin
302-84-1

serin

glyceric acid
473-81-4

glyceric acid

Conditions
ConditionsYield
With cis-nitrous acid
With hydrogenchloride; sodium nitrite In water at 0 - 20℃; for 17.0833h; Schlenk technique; Inert atmosphere;
(RS)-isoserine
632-12-2

(RS)-isoserine

glyceric acid
473-81-4

glyceric acid

Conditions
ConditionsYield
With cis-nitrous acid at 40 - 50℃;
2,3-dibromopropionic acid
600-05-5

2,3-dibromopropionic acid

glyceric acid
473-81-4

glyceric acid

Conditions
ConditionsYield
With water; silver(l) oxide
L-arabinose
5328-37-0

L-arabinose

glyceric acid
473-81-4

glyceric acid

Conditions
ConditionsYield
With copper(II) hydroxide; sodium hydroxide
With air in alkalischer Loesungen;
With dihydrogen peroxide in alkalischer Loesungen;
D-glucose
50-99-7

D-glucose

glyceric acid
473-81-4

glyceric acid

Conditions
ConditionsYield
With copper(II) hydroxide; sodium hydroxide
With air in alkalischer Loesungen;
With dihydrogen peroxide in alkalischer Loesungen;
D-Galactose
59-23-4

D-Galactose

glyceric acid
473-81-4

glyceric acid

Conditions
ConditionsYield
With Fehling's solution
With air in alkalischer Loesungen;
With dihydrogen peroxide in alkalischer Loesungen;
(+/-)-calcium glycerate dihydrate
67525-74-0

(+/-)-calcium glycerate dihydrate

glyceric acid
473-81-4

glyceric acid

Conditions
ConditionsYield
Gaerung durch den Bacillus aethaceticus;
glyceric acid
473-81-4

glyceric acid

3-iodopropanoic acid
141-76-4

3-iodopropanoic acid

Conditions
ConditionsYield
With hydrogen iodide; hydrogen; palladium dichloride at 100℃; under 20686.5 Torr; for 10h; Reagent/catalyst; Temperature; Sealed tube;99%
With hydrogen iodide; hydrogen; palladium dichloride In water at 100℃; under 20686.5 Torr; for 10h; Pressure; Reagent/catalyst; Temperature;99%
With hydrogen iodide; hydrogen; palladium dichloride at 170℃; under 155149 Torr; for 25h; Temperature; Pressure; Sealed tube;99.9%
methanol
67-56-1

methanol

glyceric acid
473-81-4

glyceric acid

methyl glycerate
615-34-9

methyl glycerate

Conditions
ConditionsYield
With toluene-4-sulfonic acid In water for 12h; Inert atmosphere; Reflux;99%
With boron trifluoride methanol complex for 1h; Heating;75.7%
at 180℃; methyl ester of/the/ d-glyceric acid;
glyceric acid
473-81-4

glyceric acid

mono(6-amino-6-deoxy)-per(2,3,6-O-methyl)-β-cyclodextrin
129867-48-7

mono(6-amino-6-deoxy)-per(2,3,6-O-methyl)-β-cyclodextrin

6I-(2,3-dihydroxypropionamido)-6I-deoxy-2I,3I-di-O-methylhexakis(2II-VII,3II-VII,6II-VII-tri-O-methyl)cyclomaltoheptaose
1407657-67-3

6I-(2,3-dihydroxypropionamido)-6I-deoxy-2I,3I-di-O-methylhexakis(2II-VII,3II-VII,6II-VII-tri-O-methyl)cyclomaltoheptaose

Conditions
ConditionsYield
Stage #1: glyceric acid With benzotriazol-1-ol; diisopropyl-carbodiimide In N,N-dimethyl-formamide at 20℃; for 1.5h; Inert atmosphere;
Stage #2: mono(6-amino-6-deoxy)-per(2,3,6-O-methyl)-β-cyclodextrin With triethylamine In chloroform; N,N-dimethyl-formamide at 20℃; for 2.5h; Inert atmosphere;
91%
glyceric acid
473-81-4

glyceric acid

tartronic acid
80-69-3

tartronic acid

Conditions
ConditionsYield
With oxygen In water at 60℃; under 2250.23 Torr; for 9h; Mechanism; Autoclave;75%
glyceric acid
473-81-4

glyceric acid

N1-(5-((2,6-dichloro-3,5-dimethoxybenzyl)oxy)pyrimidin-2-yl)-6-methylbenzene-1,2-diamine

N1-(5-((2,6-dichloro-3,5-dimethoxybenzyl)oxy)pyrimidin-2-yl)-6-methylbenzene-1,2-diamine

N-(2-((5-((2,6-dichloro-3,5-dimethoxybenzyl)oxy)pyrimidin-2-yl)amino)-3-methylphenyl)-2,3-dihydroxypropanamide

N-(2-((5-((2,6-dichloro-3,5-dimethoxybenzyl)oxy)pyrimidin-2-yl)amino)-3-methylphenyl)-2,3-dihydroxypropanamide

Conditions
ConditionsYield
With N-ethyl-N,N-diisopropylamine; N-[(dimethylamino)-3-oxo-1H-1,2,3-triazolo[4,5-b]pyridin-1-yl-methylene]-N-methylmethanaminium hexafluorophosphate In N,N-dimethyl-formamide at 20℃;67%
glyceric acid
473-81-4

glyceric acid

A

formic acid
64-18-6

formic acid

B

glycolic Acid
79-14-1

glycolic Acid

Conditions
ConditionsYield
With aluminium(III) triflate; dihydrogen peroxide In acetonitrile at 70℃; for 12h;A 57.8%
B 8.1%
glyceric acid
473-81-4

glyceric acid

A

3-iodopropanoic acid
141-76-4

3-iodopropanoic acid

B

2,3-diiodopropionic acid

2,3-diiodopropionic acid

Conditions
ConditionsYield
With rhodium on carbon; hydrogen iodide; hydrogen; iodine In water at 99.84℃; under 20686.5 Torr; for 1h; Reagent/catalyst; Temperature; Autoclave;A 52%
B 14%
glyceric acid
473-81-4

glyceric acid

3,3'-((2,2'-dichloro-[1,1'-biphenyl]-3,3'-diyl)bis(oxy))bis(propan-1-amine)

3,3'-((2,2'-dichloro-[1,1'-biphenyl]-3,3'-diyl)bis(oxy))bis(propan-1-amine)

trifluoroacetic acid
76-05-1

trifluoroacetic acid

N,N'-(((2,2'-dichloro-[1,1'-biphenyl]-3,3'-diyl)bis(oxy))bis(propane-3,1-diyl))bis(2,3-dihydroxypropanamide) trifluoroacetate

N,N'-(((2,2'-dichloro-[1,1'-biphenyl]-3,3'-diyl)bis(oxy))bis(propane-3,1-diyl))bis(2,3-dihydroxypropanamide) trifluoroacetate

Conditions
ConditionsYield
Stage #1: glyceric acid; 3,3'-((2,2'-dichloro-[1,1'-biphenyl]-3,3'-diyl)bis(oxy))bis(propan-1-amine) With 4-methyl-morpholine; 1-hydroxy-7-aza-benzotriazole; 1-ethyl-(3-(3-dimethylamino)propyl)-carbodiimide hydrochloride In water; N,N-dimethyl-formamide at 20℃; for 18h;
Stage #2: trifluoroacetic acid In water; acetonitrile
50%
glyceric acid
473-81-4

glyceric acid

benzyl bromide
100-39-0

benzyl bromide

rac-benzyl 2,3-dihydroxypropanoate
73573-57-6

rac-benzyl 2,3-dihydroxypropanoate

Conditions
ConditionsYield
With potassium carbonate In N,N-dimethyl-formamide at 20℃; for 48h;46%
ethanol
64-17-5

ethanol

glyceric acid
473-81-4

glyceric acid

ethyl 2,3-dihydroxypropionate
615-51-0

ethyl 2,3-dihydroxypropionate

Conditions
ConditionsYield
With hydrogenchloride Heating;32%
at 180 - 190℃; ethyl ester of/the/ d-glyceric acid;
at 190℃; Man fraktionert das Produkt im Vakuum;
at 190℃;
glyceric acid
473-81-4

glyceric acid

C23H38MnN6O4

C23H38MnN6O4

C29H46MnN6O10

C29H46MnN6O10

Conditions
ConditionsYield
With benzotriazol-1-ol; 1-ethyl-(3-(3-dimethylamino)propyl)-carbodiimide hydrochloride; potassium hydroxide In water at 20℃; pH=6 - 7;32%
glyceric acid
473-81-4

glyceric acid

6-(3-fluoro-4-methoxybenzyl)-2,3,4,7-tetrahydro-1H-indolo[2,3-c][1,7]naphthyridine
1207632-14-1

6-(3-fluoro-4-methoxybenzyl)-2,3,4,7-tetrahydro-1H-indolo[2,3-c][1,7]naphthyridine

1-[6-(3-fluoro-4-methoxybenzyl)-1,2,4,7-tetrahydro-3H-indolo[2,3-c][1,7]naphthyridin-3-yl]-2,3-dihydroxypropan-1-one
1207633-34-8

1-[6-(3-fluoro-4-methoxybenzyl)-1,2,4,7-tetrahydro-3H-indolo[2,3-c][1,7]naphthyridin-3-yl]-2,3-dihydroxypropan-1-one

Conditions
ConditionsYield
With benzotriazol-1-ol; 1-ethyl-(3-(3-dimethylamino)propyl)-carbodiimide hydrochloride; triethylamine In dichloromethane; water at 20℃; for 18h; Molecular sieve;25%

473-81-4Relevant academic research and scientific papers

The selective oxidation of glycerol over metal-free photocatalysts: insights into the solvent effect on catalytic efficiency and product distribution

Fan, Mingming,Haryonob, Agus,Jiang, Pingping,Leng, Yan,Yue, Chengguang,Zhang, Pingbo

, p. 3385 - 3392 (2021/06/06)

Selective oxidation of glycerol to high value-added derivatives is a promising biomass conversion pathway, but the related reaction mechanism, in particular the solvent effect, is rarely studied. In this work, O-doped g-C3N4was used as a metal-free catalyst to catalyze the selective oxidation of glycerol in different solvents. It was found that solvents can affect both catalytic efficiency and product distribution. A series of controlled experiments and theoretical calculation were applied to attest that the difference in interaction between glycerol and catalysts in different solvents is the main factor: competitive adsorption and hydrogen bond network from water inhibit the adsorption and activation of glycerol on the catalyst surface and reduce the conversion efficiency, while in acetonitrile, the stronger adsorption makes the oxidation reaction continue to yield esters. Two reaction routes in different solvents over O-doped g-C3N4are proposed for the first time, which is helpful for people to better understand the related reaction mechanism.

PROCESSES FOR PREPARING ALDARIC, ALDONIC, AND URONIC ACIDS

-

Paragraph 0110-0111, (2021/05/29)

Various processes for preparing aldaric acids, aldonic acids, uronic acids, and/or lactone(s) thereof are described. For example, processes for preparing a C2-C7 aldaric acid and/or lactone(s) thereof by the catalytic oxidation of a C2-C7 aldonic acid and/or lactone(s) thereof and/or a C2-C7 aldose are described.

A proof of concept for cooperation from the quinone groups adjacent to N sites during the metal-free oxidation of glycerol by nitrogen-rich graphene oxide

Barlocco, Ilaria,Dogra, Ashima,Gupta, Neeraj,Sharma, Vinit,Villa, Alberto

supporting information, p. 19651 - 19654 (2021/11/12)

Glycerol is a key by-product in biodiesel production and can be utilized in the synthesis of value-added chemicals. The low cost and fairly abundant availability of glycerol can be advantageous in producing a variety of pharmaceuticals and cosmetic products. Among the various catalytic transformations, selective oxidation is a promising pathway for the valorization of glycerol. In this present report, we deliver a first proof of concept for the involvement of quinone groups adjacent to N sites on the GO surface, for the selective oxidation of glycerol to dihydroxyacetone (DHA). Graphene oxide is covalently functionalized with 2,4-dihydroxypyridine (DHP), which resembles the identified active sites in the carbon clusters. As anticipated, the DHP-functionalized graphene oxide catalyst (DHP@GO) improved the conversion of glycerol to DHA, the main product, along with minor amounts of glyceric acid (GA) and fumaric acid (FA).

Assembly of platinum nanoparticles and single-atom bismuth for selective oxidation of glycerol

Huang, Ning,Jiang, Dong,Jiang, Pingping,Leng, Yan,Lu, Yubing,Tian, Jinshu,Yue, Chenguang,Zhang, Pingbo,Zhang, Zihao

supporting information, p. 25576 - 25584 (2021/12/07)

Selective oxidation of the secondary hydroxyl group of glycerol to dihydroxyacetone (DHA) is an extremely challenging yet important reaction. The main difficulty is that the three hydroxyl groups in glycerol are prone to randomly oxidize, resulting in an unsatisfactory DHA selectivity. We show here that an assembly of platinum nanoparticles (NPs, ~2 nm) and N-stabilized single-atom bismuth (Bi), namely Pt/Bi@NC, shows a record-high DHA selectivity of ~95.0% towards glycerol oxidation under optimized reaction conditions. Characterization and theoretical calculations confirm that single-atom Bi in the vicinity of Pt NPs provides a preferred site to chelate with the primary -OH of glycerol, and its secondary -OH is prone to bind to a surface Pt atom of a Pt NP with a shorter Pt-H bond length. This as-formed unique adsorption configuration of glycerol on the Pt-Bi dual site significantly facilitates the oxidation of the secondary -OH of glycerol, thus contributing to a record-high selectivity to DHA. This journal is

Transfer hydrogenation of CO2into formaldehyde from aqueous glycerol heterogeneously catalyzed by Ru bound to LDH

Deng, Lidan,Liu, Xiaowei,Xu, Jie,Zhou, Zijian,Feng, Shixiang,Wang, Zheng,Xu, Minghou

supporting information, p. 5167 - 5170 (2021/05/31)

Aqueous glycerol was used in this study as a liquid-phase hydrogen source for the hydrogenation of CO2. It was found that hydrogen could be efficiently evolved from aqueous glycerol upon highly dispersed Ru on layered double hydroxide (LDH), inducing the transformation of CO2 into formaldehyde under base-free conditions at low temperature.

Selective oxidation of glycerol over different shaped WO3 supported Pt NPs

Yang, Lihua,Jiang, Yuanyuan,Zhu, Zihui,Hou, Zhaoyin

, (2021/04/19)

In this work, different shaped WO3 (rod-like, lamellar and cuboid) supported Pt catalysts were prepared in a facile routine and tested in the selective oxidation of glycerol in base-free aqueous solution. Characterizations indicated that rod-like WO3 supported Pt catalyst (Pt/R-WO3) possesses higher surface area because of the formation of vertical pore channels and highly exposed plane (100), the deposited Pt atoms combined strongly with the terminal [sbnd]W[dbnd]O in rod-like WO3. These properties promoted the adsorption, storage and surface diffusion of oxygen over Pt/R-WO3 which exhibited the excellent activity for the selective oxidation of glycerol. And the higher amount of acid sites on the surface of Pt/R-WO3 enhanced the selectivity of glyceric acid. The calculated turnover frequency of each Pt atom in Pt/R-WO3 reached 946 h–1 at 60 °C.

Influence of Pd and Au on electrochemical valorization of glycerol over Ni-rich surfaces

Houache, Mohamed S.E.,Shubair, Asma,Sandoval, Mario G.,Safari, Reza,Botton, Gianluigi A.,Jasen, Paula V.,González, Estela A.,Baranova, Elena A.

, p. 1 - 13 (2021/03/03)

Herein we synthesized bi-metallic Pd@Ni and Au@Ni core-shell-like nanoparticles (NPs) for glycerol electrooxidation reaction (GEOR) in alkaline media. The morphological, structural and surface properties of the NPs were evaluated using a range of physicochemical techniques. The catalytic activity and stability were studied using the three-electrode electrochemical cell and 25 cm2- continuous electrolysis cell. Among different atomic ratios, Ni80Pd20 and Ni90Au10 nanoparticles showed the highest current densities which are ~4.5 and 4.2 times higher than spherical Ni, respectively. The addition of Pd and Au (a remarkable glycerate selectivity of ~73.1% and 65.7% for Ni80Pd20 and Ni90Au10 catalysts at 1.3 V and 50 °C, respectively. Notably, after 6 h of electrolysis Pd@Ni and Au@Ni tend to suppress the C-C bond cleavage, compared to Ni at any applied potentials and temperatures. The DFT calculations predicted that the addition of Pd or Au to Ni reduces the work function of M@Ni NPs, which strengthens the OH adsorption and enhances the removal of GEOR intermediates.

Hydrogen and chemicals from alcohols through electrochemical reforming by Pd-CeO2/C electrocatalyst

Bellini, Marco,Pagliaro, Maria V.,Marchionni, Andrea,Filippi, Jonathan,Miller, Hamish A.,Bevilacqua, Manuela,Lavacchi, Alessandro,Oberhauser, Werner,Mahmoudian, Jafar,Innocenti, Massimo,Fornasiero, Paolo,Vizza, Francesco

, (2021/01/25)

The development of low-cost and sustainable hydrogen production is of primary importance for a future transition to sustainable energy. In this work, the selective and simultaneous production of pure hydrogen and chemicals from renewable alcohols is achieved using an anion exchange membrane electrolysis cell (electrochemical reforming) employing a nanostructured Pd-CeO2/C anode. The catalyst exhibits high activity for alcohol electrooxidation (e.g. 474 mA cm?2 with EtOH at 60 °C) and the electrolysis cell produces high volumes of hydrogen (1.73 l min?1 m?2) at low electrical energy input (Ecost = 6 kWh kgH2?1 with formate as substrate). A complete analysis of the alcohol oxidation products from several alcohols (methanol, ethanol, 1,2-propandiol, ethylene glycol, glycerol and 1,4-butanediol) shows high selectivity in the formation of valuable chemicals such as acetate from ethanol (100%) and lactate from 1,2-propandiol (84%). Importantly for industrial application, in batch experiments the Pd-CeO2/C catalyst achieves conversion efficiencies above 80% for both formate and methanol, and 95% for ethanol.

Ambient base-free glycerol oxidation over bimetallic PdFe/SiO2 by in situ generated active oxygen species

Underhill, Ricci,Douthwaite, Mark,Lewis, Richard J.,Miedziak, Peter J.,Armstrong, Robert D.,Morgan, David J.,Freakley, Simon J.,Davies, Thomas,Folli, Andrea,Murphy, Damien M.,He, Qian,Akdim, Ouardia,Edwards, Jennifer K.,Hutchings, Graham J.

, p. 303 - 324 (2021/01/07)

Low temperature oxidation of alcohols over heterogeneous catalysts is exceptionally challenging, particularly under neutral conditions. Herein, we report on an efficient, base-free method to oxidise glycerol over a 0.5%Pd-0.5%Fe/SiO2 catalyst at ambient temperature in the presence of gaseous H2 and O2. The exceptional catalytic performance was attributed to the in situ formation of highly reactive surface-bound oxygenated species, which promote the dehydrogenation on the alcohol. The PdFe bimetallic catalyst was determined to be significantly more active than corresponding monometallic analogues, highlighting the important role both metals have in this oxidative transformation. Fe leaching was confirmed to occur over the course of the reaction but sequestering experiments, involving the addition of bare carbon to the reactions, confirmed that the reaction was predominantly heterogeneous in nature. Investigations with electron paramagnetic resonance spectroscopy suggested that the reactivity in the early stages was mediated by surface-bound reactive oxygen species; no homogeneous radical species were observed in solution. This theory was further evidenced by a direct H2O2 synthesis study, which confirmed that the presence of Fe in the bimetallic catalyst neither improved the synthesis of H2O2 nor promoted its decomposition over the PdFe/SiO2 catalyst.

Electro-oxidation of glycerol into formic acid by nickel-copper electrocatalysts

Shen, Yi,Zhang, Jiali

, (2021/09/11)

Herein, non-precious metallic nickel-copper electrocatalysts were synthesized for electro-oxidation of glycerol in alkaline electrolytes. Activated carbon felt (ACF) is used as a supporting material because of its good conductivity, chemical inertness, and porous structure which is conducive to the transport of the reactants/electrons. The structural features of the catalysts were characterized by scanning electron microscopy, X-ray diffraction and X-ray photoelectron spectroscopy. The electrochemical activity of the catalysts was revealed by cyclic voltammetry, linear sweeping voltammetry, and chronoamperometry. The electrochemical results show that the Cu1Ni1@ACF catalyst possesses the highest current density of 1.31 mA cm-2 at 1.895 V. High-performance liquid chromatography results show that the as-prepared catalysts have high selectivities for formic acid (FA). Especially, the Cu1Ni1@ACF catalyst yields a selectivity of 97.4% for FA, which has so far been the largest value reported in the literature. Additionally, the effects of applied potentials and reaction time on product selectivity were studied.

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