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Isosorbide is a versatile chemical compound derived from the hydrogenation of sorbitol, featuring a six-membered ring structure with two adjacent hydroxyl groups. It is known for its stability, low toxicity, and solubility in water, making it a valuable building block in various industries.

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  • 652-67-5 Structure
  • Basic information

    1. Product Name: Isosorbide
    2. Synonyms: Dianhydro-D-glucitol 98%;1,4:3,6-DIANHYDRO-D-SORBITOL;1,4:3,6-DIANHYDROGLUCITOL;1,4:3,6-DIANHYDROSORBITOL;1,4:3,6-DIANHYDRO-D-GLUCITOL;(3S,3AR,6R,6AR)-HEXAHYDRO-FURO[3,2-B]FURAN-3,6-DIOL;D-ISOSORBIDE;DIANHYDRO-D-GLUCITOL
    3. CAS NO:652-67-5
    4. Molecular Formula: C6H10O4
    5. Molecular Weight: 146.14
    6. EINECS: 211-492-3
    7. Product Categories: Inhibitors;Food Additivies;Carbohydrates & Derivatives;Heterocycles;Intermediates & Fine Chemicals;Pharmaceuticals
    8. Mol File: 652-67-5.mol
    9. Article Data: 136
  • Chemical Properties

    1. Melting Point: 60-63 °C(lit.)
    2. Boiling Point: 175°C/2mmHg(lit.)
    3. Flash Point: 178.8 °C
    4. Appearance: Off-white to light yellow or beige/Crystals, Crystalline Solid or Mass
    5. Density: 1.0945 (rough estimate)
    6. Vapor Pressure: 4.71E-07mmHg at 25°C
    7. Refractive Index: 45 ° (C=5, H2O)
    8. Storage Temp.: Refrigerator
    9. Solubility: DMSO (Slightly), Methanol (Slightly), Water (Slightly)
    10. PKA: 13.17±0.40(Predicted)
    11. Water Solubility: Soluble in alcohols, water and ketones.
    12. Sensitive: Hygroscopic
    13. Merck: 14,5224
    14. BRN: 80510
    15. CAS DataBase Reference: Isosorbide(CAS DataBase Reference)
    16. NIST Chemistry Reference: Isosorbide(652-67-5)
    17. EPA Substance Registry System: Isosorbide(652-67-5)
  • Safety Data

    1. Hazard Codes: N/A
    2. Statements: 22
    3. Safety Statements: 24/25
    4. WGK Germany: 2
    5. RTECS: LZ4380000
    6. TSCA: Yes
    7. HazardClass: N/A
    8. PackingGroup: N/A
    9. Hazardous Substances Data: 652-67-5(Hazardous Substances Data)

652-67-5 Usage

Uses

Used in Detergent and Cleanser Industry:
Isosorbide is used as a reagent for the preparation of detergents and cleansers, providing enhanced cleaning properties and mildness to the skin.
Used in Cosmetics Industry:
Isosorbide is utilized in cosmetics as a humectant, helping to retain moisture and improve the texture and feel of the products.
Used in Agrochemical Industry:
Isosorbide serves as a reagent in the production of agrochemicals, contributing to the effectiveness and safety of these products.
Used in Pharmaceutical Industry:
Isosorbide is employed as a pharmaceutical intermediate for the synthesis of dimethyl ether and monoand dinitrate derivatives, which are used as vasodilators and in the treatment of coronary diseases.
Used in Cardiovascular Applications:
Isosorbide and its derivatives are used as vasodilators, helping to improve blood flow and treat conditions such as hydrocephalus and glaucoma.
Used in Polymer Industry:
Isosorbide is used as a building block for the synthesis of polymers like polycarbonates and polyesters, which have a wide range of applications in various industries, including automotive, electronics, and packaging.

Biological Functions

emergency treatment of acute angle-closure glaucoma. It should not be confused with isosorbide dinitrate, an antianginal drug.

Flammability and Explosibility

Nonflammable

Clinical Use

Isosorbide is basically a bicyclic form of sorbitol that is used orally to cause a reduction in intraocular pressure in glaucoma cases. Although a diuretic effect is noted, its ophthalmologic properties are its primary value.

Check Digit Verification of cas no

The CAS Registry Mumber 652-67-5 includes 6 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 3 digits, 6,5 and 2 respectively; the second part has 2 digits, 6 and 7 respectively.
Calculate Digit Verification of CAS Registry Number 652-67:
(5*6)+(4*5)+(3*2)+(2*6)+(1*7)=75
75 % 10 = 5
So 652-67-5 is a valid CAS Registry Number.
InChI:InChI=1/C6H10O4/c7-3-1-9-6-4(8)2-10-5(3)6/h3-8H,1-2H2/t3-,4-,5+,6+/m1/s1

652-67-5 Well-known Company Product Price

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  • TCI America

  • (I0407)  Isosorbide  >98.0%(GC)

  • 652-67-5

  • 25g

  • 245.00CNY

  • Detail
  • TCI America

  • (I0407)  Isosorbide  >98.0%(GC)

  • 652-67-5

  • 100g

  • 740.00CNY

  • Detail
  • TCI America

  • (I0407)  Isosorbide  >98.0%(GC)

  • 652-67-5

  • 500g

  • 1,620.00CNY

  • Detail
  • Alfa Aesar

  • (A13989)  D-Isosorbide, 98%   

  • 652-67-5

  • 50g

  • 226.0CNY

  • Detail
  • Alfa Aesar

  • (A13989)  D-Isosorbide, 98%   

  • 652-67-5

  • 250g

  • 787.0CNY

  • Detail
  • Alfa Aesar

  • (A13989)  D-Isosorbide, 98%   

  • 652-67-5

  • 1000g

  • 2821.0CNY

  • Detail
  • Alfa Aesar

  • (A13989)  D-Isosorbide, 98%   

  • 652-67-5

  • *5x1kg

  • 11312.0CNY

  • Detail
  • Aldrich

  • (329207)  Dianhydro-D-glucitol  98%

  • 652-67-5

  • 329207-100G

  • 712.53CNY

  • Detail
  • Aldrich

  • (329207)  Dianhydro-D-glucitol  98%

  • 652-67-5

  • 329207-500G

  • 2,160.99CNY

  • Detail

652-67-5SDS

SAFETY DATA SHEETS

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

Version: 1.0

Creation Date: Aug 12, 2017

Revision Date: Aug 12, 2017

1.Identification

1.1 GHS Product identifier

Product name Isosorbide

1.2 Other means of identification

Product number -
Other names dianhydro-D-sorbitol

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:652-67-5 SDS

652-67-5Synthetic route

D-sorbitol
50-70-4

D-sorbitol

Isosorbide
652-67-5

Isosorbide

Conditions
ConditionsYield
With 1,8-diazabicyclo[5.4.0]undec-7-ene; carbonic acid dimethyl ester In methanol at 90℃; for 48h; Time; Large scale;98%
With sulfuric acid In water at 150℃; under 75.0075 Torr; for 3h; Reagent/catalyst;96.1%
With silica-alumina In water at 244.84℃; Inert atmosphere;95%
Conditions
ConditionsYield
With SA-SiO2-60.5 at 120℃; under 7.50075 Torr; for 10h; Reagent/catalyst;A n/a
B n/a
C 84%
Conditions
ConditionsYield
With palladium 10% on activated carbon; hydrogen; triethylamine In ethanol; water at 0℃; under 2250.23 Torr; for 12h; Autoclave;A 81.55%
B 16.1%
Conditions
ConditionsYield
zinc(II) chloride In 1-methyl-3-octylimidazol-3-ium chloride at 150℃; for 1h; Product distribution / selectivity;A 3.8%
B 76%
With zirconium phosphate In neat (no solvent) at 210℃; for 2h; Catalytic behavior; Temperature; Time; Reagent/catalyst; Inert atmosphere; Autoclave;A 73%
B n/a
With hydrogen; palladium on activated charcoal at 160℃; under 2311.54 Torr; for 6h; Product distribution / selectivity; Autoclave; Neat (no solvent);A 72.68%
B 2.1%
D-sorbitol
50-70-4

D-sorbitol

A

2,5-anhydro-d-sorbitol
51607-79-5

2,5-anhydro-d-sorbitol

B

Isosorbide
652-67-5

Isosorbide

Conditions
ConditionsYield
With H-beta zeolite In neat (no solvent) at 126.84℃; under 525.053 Torr; for 2h; Catalytic behavior; Reagent/catalyst;A n/a
B 76%
Conditions
ConditionsYield
sulfuric acid In water at 125 - 145℃; under 18 - 20 Torr; Industry scale;A n/a
B 75%
C n/a
D n/a
E n/a
D-sorbitol
50-70-4

D-sorbitol

A

1,5-sorbitan

1,5-sorbitan

B

Isosorbide
652-67-5

Isosorbide

Conditions
ConditionsYield
With sulfuric acid In water at 200℃; under 30003 Torr; for 6h; Autoclave;A 8%
B 73%
D-sorbitol
50-70-4

D-sorbitol

A

2,5-anhydro-d-sorbitol
51607-79-5

2,5-anhydro-d-sorbitol

B

Isosorbide
652-67-5

Isosorbide

C

1,5-anhydro-D-glucitol
154-58-5

1,5-anhydro-D-glucitol

Conditions
ConditionsYield
With Amberlyst-15 at 120℃; under 7.50075 Torr; for 10h; Reagent/catalyst;A n/a
B 71%
C n/a
Conditions
ConditionsYield
With hydrogen; phosphotungstic acid; palladium on activated charcoal In water at 160℃; under 2311.54 Torr; for 20h; Product distribution / selectivity; Autoclave;A 13.06%
B 70.33%
C 5.73%
With hydrogen; palladium dichloride at 160℃; under 2311.54 Torr; for 6h; Product distribution / selectivity; Autoclave; Neat (no solvent);A 24.89%
B 55.76%
C 0.61%
Conditions
ConditionsYield
With pyridine hydrochloride at 185℃; for 10h;67%
With carbonic acid dimethyl ester In 1,4-dioxane; methanol at 120℃;1.07 g
With zinc(II) chloride at 300℃; under 71257.1 Torr; for 0.05h; Temperature; Pressure; Autoclave;
With 4-methyl-2-pentanone at 170℃; for 1h; Autoclave;97.5 %Chromat.
D-glucose
50-99-7

D-glucose

Isosorbide
652-67-5

Isosorbide

Conditions
ConditionsYield
Stage #1: D-glucose With sulfuric acid; hydrogen In water at 170℃; under 15001.5 Torr; for 2h; Autoclave;
Stage #2: In water at 200℃; under 30003 Torr; for 6h; Reagent/catalyst; Temperature; Pressure; Time; Autoclave;
65%
Conditions
ConditionsYield
In water at 251.84℃; for 10h; Kinetics; Temperature;A n/a
B 64.6%
C n/a
With toluene-4-sulfonic acid at 180℃; Reagent/catalyst;
Conditions
ConditionsYield
With hydrogen; nickel In methanol at 70℃; under 22800 Torr; for 3h;A 62%
B 38%
D-glucose
50-99-7

D-glucose

A

1,5-sorbitan

1,5-sorbitan

B

Isosorbide
652-67-5

Isosorbide

Conditions
ConditionsYield
Stage #1: D-glucose With sulfuric acid; hydrogen In water at 170℃; under 15001.5 Torr; for 2h; Autoclave;
Stage #2: In water at 200℃; under 30003 Torr; for 6h; Autoclave;
A 8%
B 62%
D-sorbitol
50-70-4

D-sorbitol

A

Isosorbide
652-67-5

Isosorbide

B

1,5-anhydro-D-glucitol
154-58-5

1,5-anhydro-D-glucitol

Conditions
ConditionsYield
With toluene-4-sulfonic acid; N,N,N-trimethyl-N-propylammonium bis(trifluoromethanesulfonyl)imide at 180℃; for 0.166667h; Reagent/catalyst; Temperature; Time; Microwave irradiation;A 61%
B 5%
With toluene-4-sulfonic acid; N,N,N-trimethyl-N-propylammonium bis(trifluoromethanesulfonyl)imide at 130℃; for 0.5h; Microwave irradiation; Ionic liquid;A 22%
B 26%
With N,N,N-trimethyl-N-propylammonium bis(trifluoromethanesulfonyl)imide at 180℃; for 0.166667h; Catalytic behavior; Reagent/catalyst; Microwave irradiation; chemoselective reaction;A 50 %Chromat.
B 18 %Chromat.
D-sorbitol
50-70-4

D-sorbitol

A

2,5-anhydro-d-sorbitol
51607-79-5

2,5-anhydro-d-sorbitol

B

Isosorbide
652-67-5

Isosorbide

C

1,4-anhydro-D-galactitol
32742-35-1

1,4-anhydro-D-galactitol

D

2,5-anhydro-D-mannitol
41107-82-8

2,5-anhydro-D-mannitol

Conditions
ConditionsYield
With sulfuric acid at 129.84℃; for 0.75h; Kinetics; Mechanism;A n/a
B 16%
C 58%
D n/a
D-sorbitol
50-70-4

D-sorbitol

A

Isosorbide
652-67-5

Isosorbide

B

2,5-anhydro-D-iditol
28218-55-5

2,5-anhydro-D-iditol

C

2,5-anhydro-D-mannitol
41107-82-8

2,5-anhydro-D-mannitol

Conditions
ConditionsYield
With Amberlite IR-120 (H+) at 170℃; under 10 Torr; for 2h;A 57%
B 4 % Spectr.
C 3 % Spectr.
Conditions
ConditionsYield
With H-beta zeolite modified with triphenylsilane at 126.84℃; under 525.053 Torr; for 1h; Catalytic behavior; Reagent/catalyst;A n/a
B 57%
C 18%
milled cellulose

milled cellulose

Isosorbide
652-67-5

Isosorbide

Conditions
ConditionsYield
With ruthenium on carbon; water; hydrogen at 189.84℃; under 37503.8 Torr; for 16h; Reagent/catalyst; Acidic conditions; Inert atmosphere;55.8%

652-67-5Relevant articles and documents

Heterogeneous cyclization of sorbitol to isosorbide catalyzed by a novel basic porous polymer-supported ionic liquid

Wang, Yao-Feng,Xu, Bao-Hua,Du, Yi-Ran,Zhang, Suo-Jiang

, p. 59 - 66 (2018)

In this study, heterogeneous cyclization of sorbitol to isosorbide under basic condition was realized for the first time with a novel porous polymer-supported ionic liquid as catalyst. These polymer-supported ILs were synthesized through the suspension polymerization of 4-vinylbenzyl chloride and divinylbenzene, followed by a quaternization reaction. As compared to those of non-porous, the porous polymers had high specific surface area and large number of active sites. Consequently, they exhibited excellent catalytic activity in the cyclization of sorbitol with dimethylcarbonate (DMC) to isosorbide. As a result, a high conversion of sorbitol (99%) was achieved with 83% yield of isosorbide under optimized conditions. Importantly, the catalysts could be easily separated by decantation and reused for five times without obvious loss of catalytic activity.

Aqueous-phase hydrodeoxygenation of sorbitol with Pt/SiO2-Al2O3: Identification of reaction intermediates

Li, Ning,Huber, George W.

, p. 48 - 59 (2010)

Aqueous-phase hydrodeoxygenation of sugar and sugar-derived molecules can be used to produce a range of alkanes and oxygenates. In this paper, we have identified the reaction intermediates and reaction chemistry for the aqueous-phase hydrodeoxygenation of sorbitol over a bifunctional catalyst (Pt/SiO2-Al2O3) that contains both metal (Pt) and acid (SiO2-Al2O3) sites. A wide variety of reactions occur in this process including C{single bond}C bond cleavage, C{single bond}O bond cleavage, and hydrogenation reactions. The key C{single bond}C bond cleavage reactions include: retro-aldol condensation and decarbonylation, which both occur on metal catalytic sites. Dehydration is the key C{single bond}O bond cleavage reaction and occurs on acid catalytic sites. Sorbitol initially undergoes dehydration and ring closure to produce cyclic C6 molecules or retro-aldol condensation reactions to produce primarily C3 polyols. Isosorbide is the major final product from sorbitol dehydration. Isosorbide then undergoes ring opening hydrogenation reactions and a dehydration/hydrogenation step to form 1,2,6-hexanetriol. The hexanetriol is then converted into hexanol and hexane by dehydration/hydrogenation. Smaller oxygenates are produced by C{single bond}C bond cleavage. These smaller oxygenates undergo dehydration/hydrogenation reactions to produce alkanes from C1-C5. The results from this paper suggest that hydrodeoxygenation chemistry can be tuned to make a wide variety of products from biomass-derived oxygenates.

METHOD FOR PURIFICATION OF ISOSORBIDE

-

Page/Page column 14; 15, (2021/02/26)

The invention relates to a process for purifying a crude isosorbide, in which the crude isosorbide is melted and converted, by cooling, into a crude isosorbide melt suspension consisting of isosorbide crystals and residual melt, the amount by weight of impurities in the isosorbide crystals being less than the amount by weight of impurities in the residual melt, optionally a part of the residual melt is separated off mechanically from the crude isosorbide suspension, further the isosorbide crystals in the melt isosorbide suspension are purified from residual melt by washing with a washing isosorbide melt, the amount by weight of impurities in the washing isosorbide melt being less than the amount by weight of impurities in the residual melt.

Sequential dehydration of sorbitol to isosorbide over acidified niobium oxides

Guo, Jiaxing,Huang, Long,Li, Cuiqing,Liu, Shanshan,Song, Yongji,Wang, Xincheng

, p. 4226 - 4234 (2021/06/30)

Isosorbide is a bio-based functional diol, which is prepared by sequential dehydration of sorbitol and widely used in plasticizers, monomers, solvents or pharmaceuticals. In this study, a variety of acidified Nb2O5catalysts were prepared and used for the sequential dehydration of sorbitol to isosorbide. Acidification can effectively regulate the surface acidity of catalysts, which was measured by pyridine infrared spectroscopy and NH3-TPD analysis. The catalytic performance was related to the surface acidity, including the reaction temperature and the amount of catalysts. After optimization of reaction conditions, the yield of isosorbide reached 84.1% with complete sorbitol conversion during reaction at 150 °C for 3 h over 2 M sulfuric acid modified Nb2O5. Finally, the reaction mechanism regarding the role of Lewis acid sites was discussed. This study is of great significance for further development of an efficient catalytic system for the dehydration of carbohydrates to isosorbide.

Efficient and selective aqueous photocatalytic mono-dehydration of sugar alcohols using functionalized yttrium oxide nanocatalysts

Cheng, Yu,Fan, Chao,Guo, Lina,Huang, Benhua,Li, Xiaoyong,Luque, Rafael,Ma, Xiaomo,Meng, Xu,Pan, Cheng,Sun, Yang,Yang, Juncheng,Zhang, Junjie,Zhang, Weining,Zheng, Aqun

, p. 5333 - 5344 (2020/09/17)

The mono-dehydration of sugar alcohols such as d-sorbitol and d-mannitol generates 1,4-sorbitan and 1,4-mannitan, respectively, which are relevant platform molecules for the synthesis of detergents and pharmaceuticals. Most reported catalytic systems provided access to di-dehydrated products, while mono-dehydration required special efforts, particularly regarding selectivity and reaction temperature. A series of functionalized yttrium oxides were prepared via sol-gel synthesis in this work, which not only showed an interesting micropipe-like morphology, but also contained functional components. These materials were investigated as photocatalysts in the dehydration of d-sorbitol and d-mannitol, exhibiting high selectivity to mono-dehydration. The effects of solvent, temperature and catalyst were fully discussed. A catalytic mechanism was proposed based on the experimental results and calculations.

Kinetic analyses of intramolecular dehydration of hexitols in high-temperature water

Yamaguchi, Aritomo,Mimura, Naoki,Shirai, Masayuki,Sato, Osamu

, (2019/11/29)

Intramolecular dehydration of the biomass-derived hexitols D-sorbitol, D-mannitol, and galactitol was investigated. These reactions were performed in high-temperature water at 523–573 K without added acid catalyst. The rate constants for the dehydration steps in the reaction networks were determined at various reaction temperatures, and the activation energies and pre-exponential factors were calculated from Arrhenius plots. The yield of each product was estimated as a function of reaction time and temperature using the calculated rate constants and activation energies. The maximum yield of each product from the dehydration reactions was predicted over a range of reaction time and temperature, allowing the selective production of these important platform chemicals.

Direct Amination of Isohexides via Borrowing Hydrogen Methodology: Regio- and Stereoselective Issues

Bahé, Florian,Grand, Lucie,Cartier, Elise,Jacolot, Ma?wenn,Moebs-Sanchez, Sylvie,Portinha, Daniel,Fleury, Etienne,Popowycz, Florence

supporting information, p. 599 - 608 (2020/02/04)

The regio and diastereoselective direct mono or diamination of bio-based isohexides (isosorbide and isomannide) has been developed through borrowing hydrogen (BH) methodology using a cooperative catalysis between an iridium complex and a Br?nsted acid. The access to chiral amino-alcohol (NH2-OH) and diamine (NH2-NH2), interesting optically pure bio-based monomers, was also proposed using BH strategy as a sustainable route for their obtention.

Direct conversion of cellulose into isosorbide over Ni doped NbOPO4catalysts in water

Guo, Jiaxing,He, Minyao,Li, Cuiqing,Liu, ShanShan,Song, Yongji,Wang, Hong,Wang, Xincheng

supporting information, p. 10292 - 10299 (2020/07/14)

Isosorbide is a versatile chemical intermediate for the production of a variety of drugs, chemicals, and polymers, and its efficient production from natural cellulose is of great significance. In this study, bifunctional catalysts based on niobium phosphates were prepared by a facile hydrothermal method and used for the direct conversion of cellulose to isosorbide under aqueous conditions. NH3-TPD analysis showed that a high acid content existed on the catalyst surface, and pyridine infrared spectroscopic analysis confirmed the presence of both Lewis acid and Br?nsted acid sites, both of which played an important role in the process of carbohydrate conversion. XRD and H2-TPR characterization determined the composition and the hydrogenation centers of the catalyst. An isosorbide yield of 47% could be obtained at 200 °C for 24 h under 3 MPa H2 pressure. The Ni/NbOPO4 bifunctional catalyst retains most of its activity after five consecutive runs with slightly decreased isosorbide yield of 44%. In addition, a possible reaction mechanism was proposed that the synergistic effect of surface acid sites and hydrogenation sites was favorable to enhancing the cascade dehydration and hydrogenation reactions during the conversion of cellulose to isosorbide. This study provides as an efficient strategy for the development of novel multifunctional heterogeneous catalysts for the one-pot valorisation of cellulose. This journal is

Biological upgrading of 3,6-anhydro-l-galactose from agarose to a new platform chemical

Kim, Dong Hyun,Liu, Jing-Jing,Lee, Jae Won,Pelton, Jeffrey G.,Yun, Eun Ju,Yu, Sora,Jin, Yong-Su,Kim, Kyoung Heon

, p. 1776 - 1785 (2020/03/26)

Recently, the utilization of renewable biomass instead of fossil fuels for producing fuels and chemicals has received much attention due to the global climate change. Among renewable biomass, marine algae are gaining importance as third generation biomass feedstocks owing to their advantages over lignocellulose. Particularly, red macroalgae have higher carbohydrate contents and simpler carbohydrate compositions than other marine algae. In red macroalgal carbohydrates, 3,6-anhydro-l-galactose (AHG) is the main sugar composing agarose along with d-galactose. However, AHG is not a common sugar and is chemically unstable. Thus, not only AHG but also red macroalgal biomass itself cannot be efficiently converted or utilized. Here, we biologically upgraded AHG to a new platform chemical, its sugar alcohol form, 3,6-anhydro-l-galactitol (AHGol), an anhydrohexitol. To accomplish this, we devised an integrated process encompassing a chemical hydrolysis process for producing agarobiose (AB) from agarose and a biological process for converting AB to AHGol using metabolically engineered Saccharomyces cerevisiae to efficiently produce AHGol from agarose with high titers and yields. AHGol was also converted to an intermediate chemical for plastics, isosorbide. To our knowledge, this is the first demonstration of upgrading a red macroalgal biomass component to a platform chemical via a new biological route, by using an engineered microorganism.

Catalytic dehydration of sorbitol to isosorbide in the presence of metal tosylate salts and metallized sulfonic resins

Dussenne, Corentin,Wyart, Hervé,Wiatz, Vincent,Suisse, Isabelle,Sauthier, Mathieu

, p. 61 - 66 (2018/12/11)

Homogeneous catalytic dehydration of sorbitol to isosorbide has been performed with a series of metal tosylates as catalysts. Conversions up to 100 % and selectivities into isosorbide up to 67% were obtained with Bi(OTs)3. The metals were exchanged with acidic sites of sulfonic resins and the resulting materials were evaluated as heterogeneous catalysts. On the contrary to their homogeneous counter parts, the heterogenized metal sites are non-active. The catalytic activity of the modified resins was systematically diminished in comparison to the native resins. The inhibition is greatly dependent on the nature of the metal and, on a larger extent, of the used resin for the cation exchange.

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