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92867-55-5 Usage

General Description

Propane, 1,2,3-tris(1,1-dimethylethoxy)-, is a chemical compound with the molecular formula C15H32O3. It is a derivative of propane that contains three 1,1-dimethylethoxy groups attached to the carbon atoms. Propane, 1,2,3-tris(1,1-dimethylethoxy)- is mainly used as a solvent, particularly in industrial and laboratory settings. It has a high solvency power and low toxicity, making it suitable for a wide range of applications. Additionally, it is also used as a reagent in organic synthesis and as a component in the formulation of specialty chemicals. Overall, propane, 1,2,3-tris(1,1-dimethylethoxy)- is a versatile and valuable chemical compound with various practical uses.

Check Digit Verification of cas no

The CAS Registry Mumber 92867-55-5 includes 8 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 5 digits, 9,2,8,6 and 7 respectively; the second part has 2 digits, 5 and 5 respectively.
Calculate Digit Verification of CAS Registry Number 92867-55:
(7*9)+(6*2)+(5*8)+(4*6)+(3*7)+(2*5)+(1*5)=175
175 % 10 = 5
So 92867-55-5 is a valid CAS Registry Number.

92867-55-5SDS

SAFETY DATA SHEETS

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

Version: 1.0

Creation Date: Aug 13, 2017

Revision Date: Aug 13, 2017

1.Identification

1.1 GHS Product identifier

Product name 2-[2,3-bis[(2-methylpropan-2-yl)oxy]propoxy]-2-methylpropane

1.2 Other means of identification

Product number -
Other names tri-tert-butyl glycerol ether

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:92867-55-5 SDS

92867-55-5Synthetic route

glycerol
56-81-5

glycerol

isobutene
115-11-7

isobutene

A

1,2-di-tert-butylglycerol ether
162507-72-4

1,2-di-tert-butylglycerol ether

B

3-(tert-butoxy)propane-1,2-diol
74338-98-0

3-(tert-butoxy)propane-1,2-diol

C

1,3-di-tert-buthyl glycerol ether
79808-30-3

1,3-di-tert-buthyl glycerol ether

D

tri-tert-butyl glycerol ether
92867-55-5

tri-tert-butyl glycerol ether

Conditions
ConditionsYield
With A35 resin acid at 75℃; under 11251.1 Torr; for 20h; Inert atmosphere;A n/a
B n/a
C 80%
D n/a
glycerol
56-81-5

glycerol

tert-butyl alcohol
75-65-0

tert-butyl alcohol

A

1,2-di-tert-butylglycerol ether
162507-72-4

1,2-di-tert-butylglycerol ether

B

3-(tert-butoxy)propane-1,2-diol
74338-98-0

3-(tert-butoxy)propane-1,2-diol

C

1,3-di-tert-buthyl glycerol ether
79808-30-3

1,3-di-tert-buthyl glycerol ether

D

tri-tert-butyl glycerol ether
92867-55-5

tri-tert-butyl glycerol ether

Conditions
ConditionsYield
With 1-methyl-imidazolium p-toluenesulfonic acid at 100℃; under 11251.1 Torr; for 24h; Inert atmosphere;A n/a
B n/a
C 65%
D n/a
With unilamellar MFI zeolite nanosheet at 119.84℃; for 12h; Reagent/catalyst; Autoclave;
glycerol
56-81-5

glycerol

tert-butyl alcohol
75-65-0

tert-butyl alcohol

A

3-(tert-butoxy)propane-1,2-diol
74338-98-0

3-(tert-butoxy)propane-1,2-diol

B

1,3-di-tert-buthyl glycerol ether
79808-30-3

1,3-di-tert-buthyl glycerol ether

C

tri-tert-butyl glycerol ether
92867-55-5

tri-tert-butyl glycerol ether

Conditions
ConditionsYield
With pillared clay treatedwith fuming sulfuric acid: AS100 at 119.84℃; for 10h; Reagent/catalyst; Temperature; Inert atmosphere; Autoclave; High pressure;A 60%
B 33.2%
C 5.4%
With tert-butyl alcohol over sulfonated hybrid silicas at 75℃; for 24h; Reagent/catalyst;
tert-butyl methyl ether
1634-04-4

tert-butyl methyl ether

glycerol
56-81-5

glycerol

A

1,2-di-tert-butylglycerol ether
162507-72-4

1,2-di-tert-butylglycerol ether

B

3-(tert-butoxy)propane-1,2-diol
74338-98-0

3-(tert-butoxy)propane-1,2-diol

C

1,3-di-tert-buthyl glycerol ether
79808-30-3

1,3-di-tert-buthyl glycerol ether

D

tri-tert-butyl glycerol ether
92867-55-5

tri-tert-butyl glycerol ether

Conditions
ConditionsYield
With A35 resin acid at 70℃; under 11251.1 Torr; for 24h; Inert atmosphere;A n/a
B n/a
C 60%
D n/a
tert-butyl methyl ether
1634-04-4

tert-butyl methyl ether

glycerol
56-81-5

glycerol

tri-tert-butyl glycerol ether
92867-55-5

tri-tert-butyl glycerol ether

Conditions
ConditionsYield
With sulfuric acid at 25℃; for 12h; Molecular sieve;45%
glycerol
56-81-5

glycerol

tert-butyl alcohol
75-65-0

tert-butyl alcohol

tri-tert-butyl glycerol ether
92867-55-5

tri-tert-butyl glycerol ether

Conditions
ConditionsYield
at 100℃; for 1h; Catalytic behavior; Reagent/catalyst; Temperature; Concentration; Time; Autoclave; Inert atmosphere;11%
With H-Beta zeolite at 74.84℃; for 24h; Catalytic behavior; Temperature; Time; Autoclave;
With sulfonated carbons from olive stones at 75℃; for 0.25h; Temperature; Microwave irradiation; High pressure;
tert-butyl methyl ether
1634-04-4

tert-butyl methyl ether

tri-tert-butyl glycerol ether
92867-55-5

tri-tert-butyl glycerol ether

Conditions
ConditionsYield
With di-tert-butyl peroxide Irradiation;
glycerol
56-81-5

glycerol

isobutene
115-11-7

isobutene

A

3-(tert-butoxy)propane-1,2-diol
74338-98-0

3-(tert-butoxy)propane-1,2-diol

B

1,3-di-tert-buthyl glycerol ether
79808-30-3

1,3-di-tert-buthyl glycerol ether

C

tri-tert-butyl glycerol ether
92867-55-5

tri-tert-butyl glycerol ether

Conditions
ConditionsYield
strong acidic catalyst at 80 - 100℃;
glycerol
56-81-5

glycerol

isobutene
115-11-7

isobutene

tri-tert-butyl glycerol ether
92867-55-5

tri-tert-butyl glycerol ether

Conditions
ConditionsYield
β-Zeolite at 85℃; under 4380.18 - 8000.32 Torr; for 3h; Product distribution / selectivity;
methanesulfonic acid at 70℃; for 6h; Product distribution / selectivity;
sulfuric acid at 66℃; for 10h;
With S-B(1.4) sulfonic acid-functionalized pentasyl-type zeolite for 24h; Reagent/catalyst; Concentration; Time;
With dodecylaminesulfonic acid-functionalised hexagonal mesoporous silica for 24h; Reagent/catalyst; Autoclave;
glycerol
56-81-5

glycerol

isobutene
115-11-7

isobutene

A

2,2-dimethylhexane
590-73-8

2,2-dimethylhexane

B

tri-tert-butyl glycerol ether
92867-55-5

tri-tert-butyl glycerol ether

C

tert-butyl alcohol
75-65-0

tert-butyl alcohol

Conditions
ConditionsYield
sulfuric acid at 80℃; for 10h; Product distribution / selectivity;
glycerol
56-81-5

glycerol

isobutene
115-11-7

isobutene

A

2,2-dimethylhexane
590-73-8

2,2-dimethylhexane

B

tri-tert-butyl glycerol ether
92867-55-5

tri-tert-butyl glycerol ether

Conditions
ConditionsYield
Amberlyst 38 dry at 80℃; for 7h; Product distribution / selectivity;
glycerol
56-81-5

glycerol

isobutene
115-11-7

isobutene

A

1,2-di-tert-butylglycerol ether
162507-72-4

1,2-di-tert-butylglycerol ether

B

3-(tert-butoxy)propane-1,2-diol
74338-98-0

3-(tert-butoxy)propane-1,2-diol

C

1,3-di-tert-buthyl glycerol ether
79808-30-3

1,3-di-tert-buthyl glycerol ether

D

tri-tert-butyl glycerol ether
92867-55-5

tri-tert-butyl glycerol ether

E

2-tert-butoxy-1,3-propanediol
73757-68-3

2-tert-butoxy-1,3-propanediol

Conditions
ConditionsYield
With water at 70℃; for 17h; Concentration; Reagent/catalyst; Time; Overall yield = 81.7 %;
glycerol
56-81-5

glycerol

tert-butyl alcohol
75-65-0

tert-butyl alcohol

A

1,2-di-tert-butylglycerol ether
162507-72-4

1,2-di-tert-butylglycerol ether

B

3-(tert-butoxy)propane-1,2-diol
74338-98-0

3-(tert-butoxy)propane-1,2-diol

C

1,3-di-tert-buthyl glycerol ether
79808-30-3

1,3-di-tert-buthyl glycerol ether

D

tri-tert-butyl glycerol ether
92867-55-5

tri-tert-butyl glycerol ether

E

2-tert-butoxy-1,3-propanediol
73757-68-3

2-tert-butoxy-1,3-propanediol

Conditions
ConditionsYield
With A-15 resin at 80℃; for 27h; Concentration; Reagent/catalyst; Temperature; Time; Overall yield = 53.2 %;
With Amberlyst 36 dry sulfogroup cation exchange resin at 95 - 135℃;
With Amberlyst 15 In water at 70℃; Reagent/catalyst; Temperature; Time;
glycerol
56-81-5

glycerol

tert-butyl alcohol
75-65-0

tert-butyl alcohol

A

1,2-di-tert-butylglycerol ether
162507-72-4

1,2-di-tert-butylglycerol ether

B

tri-tert-butyl glycerol ether
92867-55-5

tri-tert-butyl glycerol ether

C

4-(tert-butoxymethyl)-2,2-dimethyl-1,3-dioxolane
122977-52-0

4-(tert-butoxymethyl)-2,2-dimethyl-1,3-dioxolane

D

2-tert-butoxy-1,3-propanediol
73757-68-3

2-tert-butoxy-1,3-propanediol

E

(R,S)-2,2-dimethyl-1,3-dioxolane-4-methanol
100-79-8

(R,S)-2,2-dimethyl-1,3-dioxolane-4-methanol

Conditions
ConditionsYield
at 119.84℃; for 1.5h; Reagent/catalyst; Time; Temperature; Autoclave;
glycerol
56-81-5

glycerol

A

methanol
67-56-1

methanol

B

1-butylene
106-98-9

1-butylene

C

(Z)-2-Butene
590-18-1

(Z)-2-Butene

D

propene
187737-37-7

propene

E

methane
34557-54-5

methane

F

trans-2-Butene
624-64-6

trans-2-Butene

G

ethane
74-84-0

ethane

H

propane
74-98-6

propane

I

Isobutane
75-28-5

Isobutane

J

ethene
74-85-1

ethene

K

1,2,3-trimethoxy glycerol ether
20637-49-4

1,2,3-trimethoxy glycerol ether

L

tri-tert-butyl glycerol ether
92867-55-5

tri-tert-butyl glycerol ether

M

ethylbenzene
100-41-4

ethylbenzene

N

toluene
108-88-3

toluene

O

acrolein
107-02-8

acrolein

P

isobutene
115-11-7

isobutene

Q

n-butane
106-97-8

n-butane

R

benzene
71-43-2

benzene

Conditions
ConditionsYield
With zeolite HZSM-5 In water at 340℃; Catalytic behavior; Reagent/catalyst; Flow reactor;
glycerol
56-81-5

glycerol

A

methanol
67-56-1

methanol

B

1-butylene
106-98-9

1-butylene

C

(Z)-2-Butene
590-18-1

(Z)-2-Butene

D

propene
187737-37-7

propene

E

methane
34557-54-5

methane

F

trans-2-Butene
624-64-6

trans-2-Butene

G

ethane
74-84-0

ethane

H

propane
74-98-6

propane

I

Isobutane
75-28-5

Isobutane

J

ethene
74-85-1

ethene

K

tri-tert-butyl glycerol ether
92867-55-5

tri-tert-butyl glycerol ether

L

ethylbenzene
100-41-4

ethylbenzene

M

toluene
108-88-3

toluene

N

acrolein
107-02-8

acrolein

O

isobutene
115-11-7

isobutene

P

n-butane
106-97-8

n-butane

Q

benzene
71-43-2

benzene

Conditions
ConditionsYield
With zeolite-like silico aluminophosphate SAPO-34 In water at 340℃; Flow reactor;
glycerol
56-81-5

glycerol

isobutene
115-11-7

isobutene

A

2,4,4-trimethyl-1-pentene
107-39-1

2,4,4-trimethyl-1-pentene

B

3-(tert-butoxy)propane-1,2-diol
74338-98-0

3-(tert-butoxy)propane-1,2-diol

C

1,3-di-tert-buthyl glycerol ether
79808-30-3

1,3-di-tert-buthyl glycerol ether

D

tri-tert-butyl glycerol ether
92867-55-5

tri-tert-butyl glycerol ether

Conditions
ConditionsYield
With Amberlyst 15TM 0.4M Na+-exchange at 75℃; under 3750.38 - 7500.75 Torr; for 6h; Inert atmosphere; Autoclave;

92867-55-5Downstream Products

92867-55-5Relevant articles and documents

Microwave-assisted synthesis of sulfonic acid-functionalized microporous materials for the catalytic etherification of glycerol with isobutene

Gonzalez, Maria Dolores,Salagre, Pilar,Taboada, Elena,Llorca, Jordi,Cesteros, Yolanda

, p. 2230 - 2239 (2013)

Commercial Beta, ZSM-5 and mordenite zeolites and commercial montmorillonite K-10 were successfully sulfonated by a one-step simple method using microwaves. Different amounts of the sulfonating agent were required to maximize the incorporation of sulfonic groups for each structure. This has been related to the different dealumination degree suffered by the starting samples during sulfonation together with the different accessibility of the silanols to the sulfonic groups depending on the arrangement and size of their pores. All optimised sulfonated catalysts showed total conversion and very high selectivity (79-91%) to h-GTBE (glycerol di- and tri-ethers), in spite of their microporosity, due to the incorporation of the sulfonic groups that led to a higher number and strength of Bronsted acid sites. Pore size and arrangement together with the external surface area of the catalysts affected the accessibility of the acid sites to the reactants, explaining the evolution of the catalytic results with time for each structure.

Cesium exchanged tungstophosphoric acid supported on tin oxide: An efficient solid acid catalyst for etherification of glycerol with tert-butanol to synthesize biofuel additives

Srinivas,Raveendra,Parameswaram,Prasad, P.S. Sai,Lingaiah

, p. 7 - 14 (2016)

Cesium exchanged tungstophosphoric acid (CsTPA) supported on tin oxide catalysts were prepared and their physio-chemical properties were derived from X-ray diffraction, FT-IR, laser Raman spectroscopy and temperature programmed desorption of NH3/sub

Tuning the acidic and textural properties of ordered mesoporous silicas for their application as catalysts in the etherification of glycerol with isobutene

González, María Dolores,Salagre, Pilar,Mokaya, Robert,Cesteros, Yolanda

, p. 171 - 178 (2014)

Several silicas (MCM-41, SBA-15 and HMS) were acid-modified by incorporating aluminium or by introducing phosphorus species or sulfonic groups. The modified silicas maintained mesostructural ordering and a narrow pore size distribution. However, Their surface area and pore volume was lower than that of unmodified samples. The incorporation of aluminum in the structure of MCM-41 and SBA-15 increased the amount of Br?nsted acid sites, leading to greater catalytic activity (i.e., higher conversion values) for glycerol etherification with isobutene than pure silicas, but their relatively weak acid strength resulted in low selectivity to di- and tri-tertiary butyl ethers of glycerol (h-GTBE). The introduction of phosphoric groups, with higher acidity strength, improved the selectivity to h-GTBE, and glycerol triether was detected in low amounts. Interestingly, HMS synthesized with dodecylamine and later sulfonated exhibited total conversion and 84% of selectivity to h-GTBE (26% to glycerol triether) after 24 h of reaction. The presence of textural mesoporosity in HMS reduced diffusion limitations, and consequently increased the incorporation of sulfonic groups and their accessibility, leading to higher catalytic activity.

Preparation method of 1,3-propanediol

-

Paragraph 0069-0072, (2019/09/17)

The invention discloses a preparation method of 1,3-propanediol, and relates to the technical field of chemical synthesis. According to the scheme, glycerol is used as a raw material to prepare 1,3 propylene glycol by using a functional group directional protection method, that is, a terminal hydroxyl group is selectively protected through an etherification reaction, secondary hydroxyl group is removed through a sulfonylation reaction and a reduction reaction, and a protective group is removed. The process of the preparation method provided by the invention has the characteristics of high yield, few byproducts, low cost, easy separation and the like, is an environment-friendly and economical route, overcomes the defects of complex operation and low yield in the prior art, and has a wide development prospect.

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