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4740-78-7 Usage

Chemical Properties

Clear liquid

Uses

Glycerol formal is used as a dye emulsifier and as a cosolvent for drug delivery.

Check Digit Verification of cas no

The CAS Registry Mumber 4740-78-7 includes 7 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 4 digits, 4,7,4 and 0 respectively; the second part has 2 digits, 7 and 8 respectively.
Calculate Digit Verification of CAS Registry Number 4740-78:
(6*4)+(5*7)+(4*4)+(3*0)+(2*7)+(1*8)=97
97 % 10 = 7
So 4740-78-7 is a valid CAS Registry Number.

4740-78-7SDS

SAFETY DATA SHEETS

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

Version: 1.0

Creation Date: Aug 11, 2017

Revision Date: Aug 11, 2017

1.Identification

1.1 GHS Product identifier

Product name 1,3-Dioxan-5-ol

1.2 Other means of identification

Product number -
Other names Glycerol formal

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:4740-78-7 SDS

4740-78-7Synthetic route

glycerol formal
4740-78-7

glycerol formal

formaldehyd
50-00-0

formaldehyd

glycerol
56-81-5

glycerol

A

1,3-dioxolane-4-methanol
5464-28-8

1,3-dioxolane-4-methanol

B

glycerol formal
4740-78-7

glycerol formal

Conditions
ConditionsYield
With dihydrogen peroxide; nitric acid; cetyltrimethylammonim bromide; ferric nitrate In water at 80℃; for 5h; Reagent/catalyst; Temperature;A n/a
B 95.6%
With hydrogenchlorideA 44%
B 56%
With hydrogenchloride In water at 40℃; for 24h; Yields of byproduct given;
Dimethoxymethane
109-87-5

Dimethoxymethane

glycerol
56-81-5

glycerol

A

1,3-dioxolane-4-methanol
5464-28-8

1,3-dioxolane-4-methanol

B

glycerol formal
4740-78-7

glycerol formal

Conditions
ConditionsYield
A 6%
B 94%
With toluene-4-sulfonic acid; lithium bromide In ethyl acetate at 20℃; for 16h; Yield given. Yields of byproduct given;
With toluene-4-sulfonic acid; lithium bromide at 20℃; for 16h; Product distribution; Mechanism; other temperature, other substrates, reactants;
glycerol
56-81-5

glycerol

A

1,3-dioxolane-4-methanol
5464-28-8

1,3-dioxolane-4-methanol

B

glycerol formal
4740-78-7

glycerol formal

C

glycolic Acid
79-14-1

glycolic Acid

D

ethyl 2-hydroxyacetate
623-50-7

ethyl 2-hydroxyacetate

E

diglycerol
627-82-7

diglycerol

F

oxiranyl-methanol
556-52-5

oxiranyl-methanol

G

hydroxy-2-propanone
116-09-6

hydroxy-2-propanone

H

acrolein
107-02-8

acrolein

Conditions
ConditionsYield
With pretreated aluminium vanadium phosphate In water at 280℃; under 760.051 Torr; Catalytic behavior; Activation energy; Reagent/catalyst; Temperature;A n/a
B n/a
C n/a
D n/a
E n/a
F n/a
G n/a
H 62%
glycerol
56-81-5

glycerol

(HCHO)n

(HCHO)n

A

1,3-dioxolane-4-methanol
5464-28-8

1,3-dioxolane-4-methanol

B

glycerol formal
4740-78-7

glycerol formal

Conditions
ConditionsYield
With toluene-4-sulfonic acidA 60%
B 40%
1,3-dioxan-5-ol benzoate
49784-60-3

1,3-dioxan-5-ol benzoate

glycerol formal
4740-78-7

glycerol formal

Conditions
ConditionsYield
With sodium In methanol; chloroform at 20℃; for 48h;48%
With potassium hydroxide
With methanol; chloroform; sodium methylate
formaldehyd
50-00-0

formaldehyd

glycerol
56-81-5

glycerol

glycerol formal
4740-78-7

glycerol formal

Conditions
ConditionsYield
With hydrogen cation36%
With hydrogenchloride at 0℃;
at 160 - 200℃; im Druckrohr und Destillation des Reaktionsprodukts unter vermindertem Druck;
With hydrogenchloride
With Amberlyst-15 at 100℃; for 1h; Temperature; Reagent/catalyst;
glycerol
56-81-5

glycerol

polyoxymethylene

polyoxymethylene

A

1,3-dioxolane-4-methanol
5464-28-8

1,3-dioxolane-4-methanol

B

glycerol formal
4740-78-7

glycerol formal

Conditions
ConditionsYield
With bismuth(lll) trifluoromethanesulfonate In 1,4-dioxane at 40℃; for 0.5h; Sealed tube; Sonication;A 15%
B 28%
formaldehyd
50-00-0

formaldehyd

methanesulfonyl chloride
124-63-0

methanesulfonyl chloride

glycerol
56-81-5

glycerol

A

glycerol formal
4740-78-7

glycerol formal

B

1,3-dioxolan-4-ylmethyl methanesulfonate

1,3-dioxolan-4-ylmethyl methanesulfonate

Conditions
ConditionsYield
With triethylamine Multistep reaction;
formaldehyd
50-00-0

formaldehyd

p-toluenesulfonyl chloride
98-59-9

p-toluenesulfonyl chloride

glycerol
56-81-5

glycerol

A

glycerol formal
4740-78-7

glycerol formal

B

(1,3-dioxolan-4-yl)methyl 4-methylbenzenesulfonate
85608-69-1

(1,3-dioxolan-4-yl)methyl 4-methylbenzenesulfonate

Conditions
ConditionsYield
With triethylamine Yield given. Multistep reaction. Yields of byproduct given;
hydrogenchloride
7647-01-0

hydrogenchloride

glycerol
56-81-5

glycerol

polyoxymethylene

polyoxymethylene

A

1,3-dioxolane-4-methanol
5464-28-8

1,3-dioxolane-4-methanol

B

glycerol formal
4740-78-7

glycerol formal

Conditions
ConditionsYield
at 130℃;
at 100℃;
sulfuric acid
7664-93-9

sulfuric acid

glycerol
56-81-5

glycerol

polyoxymethylene

polyoxymethylene

A

1,3-dioxolane-4-methanol
5464-28-8

1,3-dioxolane-4-methanol

B

glycerol formal
4740-78-7

glycerol formal

Conditions
ConditionsYield
at 130℃;
at 100℃;
hydrogenchloride
7647-01-0

hydrogenchloride

formaldehyd
50-00-0

formaldehyd

glycerol
56-81-5

glycerol

A

1,3-dioxolane-4-methanol
5464-28-8

1,3-dioxolane-4-methanol

B

glycerol formal
4740-78-7

glycerol formal

1,3,5-Trioxan
110-88-3

1,3,5-Trioxan

glycerol
56-81-5

glycerol

A

1,3-dioxolane-4-methanol
5464-28-8

1,3-dioxolane-4-methanol

B

glycerol formal
4740-78-7

glycerol formal

Conditions
ConditionsYield
With sodium tetrachloroaurate dihydrate In 1,4-dioxane at 100℃; for 16h; Kinetics; Reagent/catalyst; Temperature; Time; Solvent;
C9H16O4
1404077-71-9

C9H16O4

2,2-Dimethyl-propionic acid [1,3]dioxolan-4-ylmethyl ester

2,2-Dimethyl-propionic acid [1,3]dioxolan-4-ylmethyl ester

A

1,3-dioxolane-4-methanol
5464-28-8

1,3-dioxolane-4-methanol

B

glycerol formal
4740-78-7

glycerol formal

Conditions
ConditionsYield
With sodium hydroxide In ethanol at 20℃; for 18h; Inert atmosphere;
glycerol
56-81-5

glycerol

A

glycerol formal
4740-78-7

glycerol formal

B

3-methoxy-1-propanal
2806-84-0

3-methoxy-1-propanal

C

acetaldehyde
75-07-0

acetaldehyde

D

hydroxy-2-propanone
116-09-6

hydroxy-2-propanone

E

acrolein
107-02-8

acrolein

Conditions
ConditionsYield
With H-ZSM5 In water at 340℃; under 760.051 Torr; for 6h; Reagent/catalyst; Inert atmosphere;
formaldehyd
50-00-0

formaldehyd

glycerol
56-81-5

glycerol

A

1,3-dioxolane-4-methanol
5464-28-8

1,3-dioxolane-4-methanol

B

glycerol formal
4740-78-7

glycerol formal

C

C9H16O6

C9H16O6

D

C8H14O6

C8H14O6

E

C7H12O6

C7H12O6

Conditions
ConditionsYield
With cesium 12-tungstophosphate at 70℃; Reagent/catalyst;
benzaldehyde
100-52-7

benzaldehyde

glycerol
56-81-5

glycerol

glycerol formal
4740-78-7

glycerol formal

Conditions
ConditionsYield
With zinc-modified strong acid polystyrene cation exchange at 150℃; for 5h;
glycerol
56-81-5

glycerol

A

1,3-dioxolane-4-methanol
5464-28-8

1,3-dioxolane-4-methanol

B

glycerol formal
4740-78-7

glycerol formal

C

formic acid
64-18-6

formic acid

Conditions
ConditionsYield
With dihydrogen peroxide In water at 200℃; for 10h; Catalytic behavior; Reagent/catalyst; Flow reactor; Autoclave; Green chemistry; chemoselective reaction;
glycerol
56-81-5

glycerol

A

1,3-dioxolane-4-methanol
5464-28-8

1,3-dioxolane-4-methanol

B

glycerol formal
4740-78-7

glycerol formal

C

formic acid
64-18-6

formic acid

D

acetic acid
64-19-7

acetic acid

E

hydroxy-2-propanone
116-09-6

hydroxy-2-propanone

Conditions
ConditionsYield
With dihydrogen peroxide In water at 200℃; for 13h; Flow reactor; Autoclave; Green chemistry; chemoselective reaction;
glycerol
56-81-5

glycerol

A

1,3-dioxolane-4-methanol
5464-28-8

1,3-dioxolane-4-methanol

B

glycerol formal
4740-78-7

glycerol formal

C

formic acid
64-18-6

formic acid

D

acetic acid
64-19-7

acetic acid

Conditions
ConditionsYield
With dihydrogen peroxide In water at 200℃; for 21h; Catalytic behavior; Time; Flow reactor; Autoclave; Green chemistry; chemoselective reaction;
glycerol
56-81-5

glycerol

A

1,3-dioxolane-4-methanol
5464-28-8

1,3-dioxolane-4-methanol

B

glycerol formal
4740-78-7

glycerol formal

C

hydroxy-2-propanone
116-09-6

hydroxy-2-propanone

Conditions
ConditionsYield
With alumina; dihydrogen peroxide In water at 200℃; for 4h; Catalytic behavior; Time; Flow reactor; Autoclave; chemoselective reaction;
glycerol formal
4740-78-7

glycerol formal

1-hexadecylcarboxylic acid
57-10-3

1-hexadecylcarboxylic acid

hexadecanoic acid [1,3]dioxan-5-yl ester
163550-89-8

hexadecanoic acid [1,3]dioxan-5-yl ester

Conditions
ConditionsYield
With dmap; dicyclohexyl-carbodiimide Esterification;93%
glycerol formal
4740-78-7

glycerol formal

cis-Octadecenoic acid
112-80-1

cis-Octadecenoic acid

(Z)-Octadec-9-enoic acid [1,3]dioxan-5-yl ester
277749-20-9

(Z)-Octadec-9-enoic acid [1,3]dioxan-5-yl ester

Conditions
ConditionsYield
With dmap; dicyclohexyl-carbodiimide Esterification;92%
glycerol formal
4740-78-7

glycerol formal

epichlorohydrin
106-89-8

epichlorohydrin

1,3-bis[(1,3-dioxan-5-yl)oxy]propan-2-ol
1333247-50-9

1,3-bis[(1,3-dioxan-5-yl)oxy]propan-2-ol

Conditions
ConditionsYield
With tetrabutylammomium bromide; water; potassium hydroxide at 20 - 60℃; for 48h; Inert atmosphere; neat (no solvent);90%
glycerol formal
4740-78-7

glycerol formal

10-undecenoic acid
112-38-9

10-undecenoic acid

undec-10-enoic acid [1,3]dioxan-5-yl ester
277749-21-0

undec-10-enoic acid [1,3]dioxan-5-yl ester

Conditions
ConditionsYield
With dmap; dicyclohexyl-carbodiimide Esterification;89%
glycerol formal
4740-78-7

glycerol formal

1-decanoic acid
334-48-5

1-decanoic acid

decanoic acid [1,3]dioxan-5-yl ester
15180-87-7

decanoic acid [1,3]dioxan-5-yl ester

Conditions
ConditionsYield
With dmap; dicyclohexyl-carbodiimide Esterification;82%
glycerol formal
4740-78-7

glycerol formal

n-docosanoic acid
112-85-6

n-docosanoic acid

docosanoic acid [1,3]dioxan-5-yl ester
277749-19-6

docosanoic acid [1,3]dioxan-5-yl ester

Conditions
ConditionsYield
With dmap; dicyclohexyl-carbodiimide Esterification;80%
glycerol formal
4740-78-7

glycerol formal

valeric acid
109-52-4

valeric acid

pentanoic acid [1,3]dioxan-5-yl ester
15180-73-1

pentanoic acid [1,3]dioxan-5-yl ester

Conditions
ConditionsYield
With dmap; dicyclohexyl-carbodiimide Esterification;80%
glycerol formal
4740-78-7

glycerol formal

E-6-amino-9-<1-methyl-2-(tetrahydropyran-2-yloxy)ethenyl>-9H-purine

E-6-amino-9-<1-methyl-2-(tetrahydropyran-2-yloxy)ethenyl>-9H-purine

9-[2-Bromo-1-([1,3]dioxan-5-yloxy)-1-methyl-2-(tetrahydro-pyran-2-yloxy)-ethyl]-9H-purin-6-ylamine

9-[2-Bromo-1-([1,3]dioxan-5-yloxy)-1-methyl-2-(tetrahydro-pyran-2-yloxy)-ethyl]-9H-purin-6-ylamine

Conditions
ConditionsYield
With N-Bromosuccinimide Ambient temperature;60%
glycerol formal
4740-78-7

glycerol formal

pivaloyl chloride
3282-30-2

pivaloyl chloride

2,2-Dimethyl-propionic acid [1,3]dioxolan-4-ylmethyl ester

2,2-Dimethyl-propionic acid [1,3]dioxolan-4-ylmethyl ester

Conditions
ConditionsYield
With 1,3-dioxolane-4-methanol; pyridine In dichloromethane Inert atmosphere;44%
glycerol formal
4740-78-7

glycerol formal

2-(2H-tetrazol-5-yl)-N-[4-(trifluoromethyl)phenyl]aniline

2-(2H-tetrazol-5-yl)-N-[4-(trifluoromethyl)phenyl]aniline

2-(2-(1,3-dioxan-5-yl)-2H-tetrazol-5-yl)-N-(4-(trifluoromethyl)phenyl)aniline

2-(2-(1,3-dioxan-5-yl)-2H-tetrazol-5-yl)-N-(4-(trifluoromethyl)phenyl)aniline

Conditions
ConditionsYield
With di-isopropyl azodicarboxylate; triphenylphosphine In tetrahydrofuran at 0 - 20℃; for 16h; Inert atmosphere;42.6%
glycerol formal
4740-78-7

glycerol formal

6-amino-9-(isopropenyl)-9H-purine
159383-03-6

6-amino-9-(isopropenyl)-9H-purine

9-[2-Bromo-1-([1,3]dioxan-5-yloxy)-1-methyl-ethyl]-9H-purin-6-ylamine

9-[2-Bromo-1-([1,3]dioxan-5-yloxy)-1-methyl-ethyl]-9H-purin-6-ylamine

Conditions
ConditionsYield
With N-Bromosuccinimide Ambient temperature;30%
glycerol formal
4740-78-7

glycerol formal

1,3-dioxan-5-one
87683-81-6

1,3-dioxan-5-one

Conditions
ConditionsYield
With Collins reagent12%
With pyridinium chlorochromate In dichloromethane
glycerol formal
4740-78-7

glycerol formal

carbonochloridic acid, chloromethyl ester
22128-62-7

carbonochloridic acid, chloromethyl ester

chloromethyl (1,3-dioxan-5-yl) carbonate
214543-57-4

chloromethyl (1,3-dioxan-5-yl) carbonate

Conditions
ConditionsYield
With pyridine In diethyl ether at 0℃; for 20h;5%
glycerol formal
4740-78-7

glycerol formal

benzoyl chloride
98-88-4

benzoyl chloride

1,3-dioxan-5-ol benzoate
49784-60-3

1,3-dioxan-5-ol benzoate

Conditions
ConditionsYield
With quinoline
With pyridine
glycerol formal
4740-78-7

glycerol formal

phenyl isocyanate
103-71-9

phenyl isocyanate

phenyl-carbamic acid-[1,3]dioxan-5-yl ester
92368-06-4

phenyl-carbamic acid-[1,3]dioxan-5-yl ester

glycerol formal
4740-78-7

glycerol formal

dimethyl sulfate
77-78-1

dimethyl sulfate

5-methoxy-1,3-dioxane
99586-36-4

5-methoxy-1,3-dioxane

Conditions
ConditionsYield
With potassium hydroxide
glycerol formal
4740-78-7

glycerol formal

5-chloro-1,3-dioxane
51953-54-9

5-chloro-1,3-dioxane

Conditions
ConditionsYield
With pyridine; thionyl chloride
glycerol formal
4740-78-7

glycerol formal

phosgene
75-44-5

phosgene

C5H7ClO4

C5H7ClO4

1,3-dioxolane-4-methanol
5464-28-8

1,3-dioxolane-4-methanol

glycerol formal
4740-78-7

glycerol formal

2-chloro-1,3,2-dioxaphosphinane
6362-89-6

2-chloro-1,3,2-dioxaphosphinane

A

2-(1,3-dioxan-5-yloxy)-1,3,2-dioxaphosphorinane
219133-84-3

2-(1,3-dioxan-5-yloxy)-1,3,2-dioxaphosphorinane

B

2-[1,2-(methylenedioxy)propyloxy]-1,3,2-dioxaphosphorinane
219133-79-6

2-[1,2-(methylenedioxy)propyloxy]-1,3,2-dioxaphosphorinane

Conditions
ConditionsYield
With triethylamine In diethyl ether at -10 - 20℃; for 1h; phosphorylation; Title compound not separated from byproducts;

4740-78-7Relevant academic research and scientific papers

An efficient method for the refinement of 1,3-methyleneglycerol via bridged acetal exchange and the synthesis of a symmetrically branched glycerol trimer

Hattori, Hatsuhiko,Matsushita, Tsuyoshi,Yoshitomi, Kohsuke,Katagiri, Ayato,Nemoto, Hisao

, p. 2365 - 2373 (2012)

Acid-catalyzed equilibrium of a mixture of 1,2- and 1,3-methyleneglycerol in 1,4-dioxane affords predominantly the 1,3-isomer via bridged acetal exchange. The minor 1,2-isomer is removed via sequential pivaloylation and tritylation to afford the desired 1,3-isomer in >99.5% purity. A symmetrically branched triglycerol is efficiently synthesized starting from the purified 1,3-isomer. Georg Thieme Verlag Stuttgart · New York.

Glycerol acetalization with formaldehyde using water-tolerant solid acids

Chen, Lin,Nohair, Bendaoud,Kaliaguine, Serge

, p. 143 - 152 (2016)

The acid-catalyzed reaction of glycerol with aqueous formaldehyde was studied using various heterogeneous catalysts for the production of glycerol formal. Owing to the high amount of water involved in the reaction medium, three types of water-tolerant heterogeneous catalysts namely acid functionalized periodic mesoporous organosilicas (PMOs), zeolite ZSM-5 and a heteropoly compound Cs2.5H0.5PW12O40 as well as commercial catalyst Amberlyst-15 were used for glycerol acetalization. The activity of Cs2.5H0.5PW12O40 was found superior to that of the other catalysts and the glycerol conversion was over 70% within 60 min of reaction time. The effects of different parameters including temperature, feed composition and catalyst content, were studied as well. The distribution of the two glycerol formal isomers could be controlled by changing reaction parameters. Optimum reactive parameters were studied to control the distribution of the acetal isomers aiming to reach a high selectivity to the six-member ring isomer.

Mesoporous Zr-SBA-16 catalysts for glycerol valorization processes: Towards biorenewable formulations

Gonzalez-Arellano, Camino,Parra-Rodriguez, Leticia,Luque, Rafael

, p. 2287 - 2292 (2014)

Zr-containing SBA-16 materials were utilized in glycerol valorization for the production of esters (via reaction with levulinic acid) and glycerol formal (GF) via acetalisation with paraformaldehyde. The materials were found to be highly active and selective for the production of valuable compounds from glycerol using benign by design solventless protocols which employ mild reaction conditions. Certain materials were also found to be highly reusable and stable under the investigated conditions.

Biomass alcoholysis method for petroleum-based plastic POM

-

Paragraph 0030-0052, (2021/05/01)

The invention discloses a biomass alcoholysis method for petroleum-based plastic POM. According to the method, simple biomass derivative alcohol and the petroleum-based plastic POM are allowed to generate a cyclic acetal product through dehydration condensation under catalytic conditions; low reaction cost and high added value are realized, and only water is byproduced and is easy to separate; and an obtained product has high added value, can be used for preparing organic solvents such as lignin and chromatographic analysis solvents, metal surface treatment agents or medical intermediates and monomers, realizes green, efficient and low-cost recovery, and has a high practical application value.

Interaction of triols with formaldehyde and acetone: Experimental and theoretical study

Sultanova, Rimma,Borisevich, Sophia,Raskil'dina, Gulnara,Borisova, Julianna,Baykova, Irina,Spirikhin, Leonid,Khursan, Sergey,Zlotsky, Simon

, p. 1144 - 1151 (2020/02/25)

Experimental and theoretical aspects of the condensation of glycerol and its homologs (1,2,3- and 1,2,4-butanetriols) with formaldehyde and acetone are studied under conditions of acid catalysis. Calculation of the thermodynamic parameters of the resulting products by the composite method CBS-QB3 shows that the six-membered heterocycles, the products of the interaction of triols with formaldehyde, are thermodynamically more stable than the five-membered acetals, while the reaction of the same triols with acetone is preferable for the formation of the five-membered acetals. This is due to the fact that the regioselectivity of the studied reactions is determined by the structural features and reactivity of the carbocations formed in a condensed medium during the course of the reaction. According to the theoretical data obtained experimentally, during the condensation of glycerol and 1,2,4-butanetriol with formaldehyde in the most stable form of the six-membered cyclic carbocation, intramolecular hydrogen bonding and anomeric stabilization due to the axially oriented hydroxyl group take place. As a result, cation 1b–1 is 1.2–1.6 kJ/mol more stable than its five-membered isomers (1a–1 and 1b–2). It leads to the predominant formation of 1,3-dioxane (3b). However, upon condensation of butanetriol-1,2,3 with formaldehyde, the intermediate cation 4a–1 turns out to be significantly more stable than the other isomers due to the strong intramolecular hydrogen bond in the six-membered ring with the participation of the hydroxyl group of the substituent and the hydroxyl group of the cationic center, leading to the predominant formation of the dioxolane 6a.

A bifunctional catalyst based on Nb and v oxides over alumina: Oxidative cleavage of crude glycerol to green formic acid

Chagas, Poliane,Figueiredo, Marcio P.,Hensen, Emiel J. M.,Oliveira, Henrique S.,Oliveira, Luiz Carlos A.,Sangiorge, Daniel L.,Siqueira, Kisla P. F.

, p. 8538 - 8544 (2020/06/19)

A bimetallic vanadium and niobium oxide catalyst using alumina as support was developed for the conversion of crude glycerol from biodiesel production into formic acid. The high dispersion of the active oxide phase combined with the presence of acid and redox active centers resulted in a high glycerol conversion (>90% for 25 h) with a good selectivity for formic acid (~55%). This process is the first example of a heterogeneous liquid-phase process for the conversion of crude glycerol to formic acid, which is an important chemical intermediate currently derived from petroleum feedstock.

Method for preparing glycerolformal

-

Paragraph 0029-0034, (2019/04/11)

The invention discloses a method for preparing glycerolformal. According to the invention, SO42-/Fe2O3-CNTS super acid is used as a catalyst for compounding glycerolformal, so that the method has theadvantages that reaction temperature is low, catalyst activity is high, no new water-carrying agent is brought, yield of reaction products is 95% or above and hexatomic ring products are high in proportion.

Glycerolformal industrial production method

-

Paragraph 0029-0032, (2019/05/22)

The invention discloses a glycerolformal industrial production method. The glycerolformal industrial production method achieves synthesis of glycerolformal by taking SO42-/ZrO2-CNTS (carbon nanotubes)super acids as catalysts. The glycerolformal industrial production method is low in reaction temperature, high in activity of catalysts, free from introduction of new water-carrying agent and short in reaction time; the products achieve a yield of higher than 92% and a high proportional ratio of hexatomic ring products.

Method for preparing glycerol benzaldehyde

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Paragraph 0032; 0033, (2019/04/17)

The invention discloses a method for preparing glycerol benzaldehyde. Metal zinc modified strong acid cation exchange resin is used as a catalyst for synthesizing the glycerol benzaldehyde. Owing to modification of metal zinc, the strong acid cation exchange resin has the function of activating aldehydic carbonyl, glycerol conversion rate reaches up to 95% or more, and product yield is 88% or more.

Highly Efficient Glycerol Acetalization over Supported Heteropoly Acid Catalysts

Chen, Lin,Nohair, Bendaoud,Zhao, Dongyuan,Kaliaguine, Serge

, p. 1918 - 1925 (2018/03/28)

The acetalization of glycerol with acetone to yield solketal was catalyzed by Cs2.5H0.5PW12O40 (Cs2.5) supported on mesoporous silica under mild conditions. It gave a high glycerol conversion and selectivity to the targeted product even at room temperature (23 °C). We studied the use of both bulk and supported Cs2.5 as catalysts in another highly efficient glycerol acetalization reaction with paraformaldehyde, which gave much higher activity than with formaldehyde solution. For the reaction with acetone, the supported Cs2.5 showed a higher activity than the bulk material because of the high surface area of the mesoporous support. Interestingly, the supported Cs2.5 gave a lower conversion than the bulk for the reaction with paraformaldehyde. This is probably because of the high viscosity of the reaction system with the solid reagent paraformaldehyde. Overall, there is a complex relationship between catalyst, reaction conditions, which include the molar ratio of reactants and temperature, reaction mechanism and thermodynamics that affects the achieved activity and byproduct formation. A discussion about these interactions is included for each reaction.

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