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6938-94-9

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6938-94-9 Usage

Uses

diisopropyl adipate is a low-viscosity emollient. It increases a preparation’s spreadability.

Flammability and Explosibility

Nonflammable

Check Digit Verification of cas no

The CAS Registry Mumber 6938-94-9 includes 7 digits separated into 3 groups by hyphens. The first part of the number,starting from the left, has 4 digits, 6,9,3 and 8 respectively; the second part has 2 digits, 9 and 4 respectively.
Calculate Digit Verification of CAS Registry Number 6938-94:
(6*6)+(5*9)+(4*3)+(3*8)+(2*9)+(1*4)=139
139 % 10 = 9
So 6938-94-9 is a valid CAS Registry Number.
InChI:InChI=1/C12H22O4/c1-9(2)15-11(13)7-5-6-8-12(14)16-10(3)4/h9-10H,5-8H2,1-4H3

6938-94-9SDS

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 Adipic Acid Diisopropyl Ester

1.2 Other means of identification

Product number -
Other names Hexanedioic acid, bis(1-methylethyl) ester

1.3 Recommended use of the chemical and restrictions on use

Identified uses For industry use only. Flavouring Agent: FLAVOURING_AGENT
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:6938-94-9 SDS

6938-94-9Synthetic route

hexanedioic acid dimethyl ester
627-93-0

hexanedioic acid dimethyl ester

isopropyl alcohol
67-63-0

isopropyl alcohol

adipic acid diisopropyl ester
6938-94-9

adipic acid diisopropyl ester

Conditions
ConditionsYield
With tetramethylammonium methyl carbonate for 8h; Molecular sieve; Reflux; Green chemistry;98%
Adipic acid
124-04-9

Adipic acid

isopropyl alcohol
67-63-0

isopropyl alcohol

adipic acid diisopropyl ester
6938-94-9

adipic acid diisopropyl ester

Conditions
ConditionsYield
With thionyl chloride; sodium carbonate for 2h; Heating;89%
carbon monoxide
201230-82-2

carbon monoxide

diisopropyl (E)-hex-3-enedioate
90157-48-5

diisopropyl (E)-hex-3-enedioate

A

adipic acid diisopropyl ester
6938-94-9

adipic acid diisopropyl ester

B

diisopropyl 3-formylhexanedioate

diisopropyl 3-formylhexanedioate

Conditions
ConditionsYield
With triphenyl phosphite; (acetylacetonato)dicarbonylrhodium (l); hydrogen In tetrahydrofuran at 70℃; under 3750.38 - 15001.5 Torr; for 16h; Schlenk technique; Autoclave;A n/a
B 88%
isopropyl alcohol
67-63-0

isopropyl alcohol

2,4-dinitro-benzenesulfonic acid 2-oxo-cyclohexyl ester
518068-80-9

2,4-dinitro-benzenesulfonic acid 2-oxo-cyclohexyl ester

adipic acid diisopropyl ester
6938-94-9

adipic acid diisopropyl ester

Conditions
ConditionsYield
With Oxone; toluene-4-sulfonic acid at 65℃; for 2h;85%
carbon monoxide
201230-82-2

carbon monoxide

buta-1,3-diene
106-99-0

buta-1,3-diene

isopropyl alcohol
67-63-0

isopropyl alcohol

adipic acid diisopropyl ester
6938-94-9

adipic acid diisopropyl ester

Conditions
ConditionsYield
With palladium(II) trifluoroacetate; toluene-4-sulfonic acid; 1,2-bis[di(t-butyl)phosphinomethyl]benzene In toluene at 120℃; under 30003 Torr; for 24h; Autoclave; Green chemistry; regioselective reaction;73%
With palladium(II) trifluoroacetate; HeMaRaphos; toluene-4-sulfonic acid In toluene at 120℃; under 30003 Torr; for 24h; regioselective reaction;83 %Chromat.
2-nitrocyclohexanone
4883-67-4

2-nitrocyclohexanone

isopropyl alcohol
67-63-0

isopropyl alcohol

adipic acid diisopropyl ester
6938-94-9

adipic acid diisopropyl ester

Conditions
ConditionsYield
With dipotassium peroxodisulfate; sulfuric acid at 80℃; for 3h;71%
Tetrahydrofurfuryl alcohol
97-99-4

Tetrahydrofurfuryl alcohol

adipic acid diisopropyl ester
6938-94-9

adipic acid diisopropyl ester

A

adipic acid isopropyl ester-tetrahydrofurfuryl ester
97159-24-5

adipic acid isopropyl ester-tetrahydrofurfuryl ester

B

hexanedioic acid bis-tetrahydrofurfuryl ester
105-02-2

hexanedioic acid bis-tetrahydrofurfuryl ester

Conditions
ConditionsYield
With aluminum isopropoxide at 170℃;
farnesol
4602-84-0

farnesol

adipic acid diisopropyl ester
6938-94-9

adipic acid diisopropyl ester

A

isopropyl farnesyl adipate
935542-35-1

isopropyl farnesyl adipate

B

difarnesyl adipate
935542-33-9

difarnesyl adipate

Conditions
ConditionsYield
zircornium(IV) n-propoxide In propan-1-ol at 160 - 165℃; under 22.5023 Torr; for 2h; Purification / work up;
octane-2,7-diol
19686-96-5

octane-2,7-diol

adipic acid diisopropyl ester
6938-94-9

adipic acid diisopropyl ester

polymer, iterative tandem catalysis polymerization, ee = 43%, molecular weight = 3.3 kDa (GPC); monomer(s): 2,7-octanediol; diisopropyl adipate

polymer, iterative tandem catalysis polymerization, ee = 43%, molecular weight = 3.3 kDa (GPC); monomer(s): 2,7-octanediol; diisopropyl adipate

Conditions
ConditionsYield
With Novozym 435; 2,4-dimethyl-3-pentanol; 3 A molecular sieve; Shvo's catalyst In toluene at 70℃; under 210.021 Torr; for 390h; Kinetics;
2,9-decanediol
14021-92-2

2,9-decanediol

adipic acid diisopropyl ester
6938-94-9

adipic acid diisopropyl ester

polymer, iterative tandem catalysis polymerization, ee = 46%, molecular weight = 3.7 kDa (GPC); monomer(s): 2,9-decanediol; diisopropyl adipate

polymer, iterative tandem catalysis polymerization, ee = 46%, molecular weight = 3.7 kDa (GPC); monomer(s): 2,9-decanediol; diisopropyl adipate

Conditions
ConditionsYield
With Novozym 435; 2,4-dimethyl-3-pentanol; 3 A molecular sieve; Shvo's catalyst In toluene at 70℃; under 210.021 Torr; for 310h; Kinetics;
adipic acid diisopropyl ester
6938-94-9

adipic acid diisopropyl ester

2,8-nonanediol
39997-24-5

2,8-nonanediol

polymer, iterative tandem catalysis polymerization, ee = 41%, molecular weight = 3.7 kDa (GPC); monomer(s): 2,8-nonanediol; diisopropyl adipate

polymer, iterative tandem catalysis polymerization, ee = 41%, molecular weight = 3.7 kDa (GPC); monomer(s): 2,8-nonanediol; diisopropyl adipate

Conditions
ConditionsYield
With Novozym 435; 2,4-dimethyl-3-pentanol; 3 A molecular sieve; Shvo's catalyst In toluene at 70℃; under 210.021 Torr; for 390h; Kinetics;
adipic acid diisopropyl ester
6938-94-9

adipic acid diisopropyl ester

1,4-bis(1-hydroxyethyl)benzene
6781-43-7

1,4-bis(1-hydroxyethyl)benzene

polymer, iterative tandem catalysis polymerization, ee = 94%, molecular weight = 8.3 kDa (GPC); monomer(s): 1,1'-(1,4-phenylene)diethanol; diisopropyl adipate

polymer, iterative tandem catalysis polymerization, ee = 94%, molecular weight = 8.3 kDa (GPC); monomer(s): 1,1'-(1,4-phenylene)diethanol; diisopropyl adipate

Conditions
ConditionsYield
With Novozym 435; 2,4-dimethyl-3-pentanol; 3 A molecular sieve; Shvo's catalyst In toluene at 70℃; under 210.021 Torr; for 171h; Kinetics;
adipic acid diisopropyl ester
6938-94-9

adipic acid diisopropyl ester

1,4-bis(1-hydroxyethyl)benzene
6781-43-7

1,4-bis(1-hydroxyethyl)benzene

A

polymer, iterative tandem catalysis polymerization, ee = 94%, molecular weight = 8.3 kDa (GPC); monomer(s): 1,1'-(1,4-phenylene)diethanol; diisopropyl adipate

polymer, iterative tandem catalysis polymerization, ee = 94%, molecular weight = 8.3 kDa (GPC); monomer(s): 1,1'-(1,4-phenylene)diethanol; diisopropyl adipate

B

isopropyl alcohol
67-63-0

isopropyl alcohol

Conditions
ConditionsYield
With 2,4-dimethyl-3-pentanol; 3 A molecular sieve; Novozym 435 In toluene at 70℃; under 210.021 Torr; for 171h;A 97 % Turnov.
B n/a
adipic acid diisopropyl ester
6938-94-9

adipic acid diisopropyl ester

polymer, iterative tandem catalysis polymerization, ee = 92%, molecular weight = 10.7 kDa (GPC); monomer(s): 1,1'-(1,3-phenylene)diethanol; diisopropyl adipate

polymer, iterative tandem catalysis polymerization, ee = 92%, molecular weight = 10.7 kDa (GPC); monomer(s): 1,1'-(1,3-phenylene)diethanol; diisopropyl adipate

Conditions
ConditionsYield
With Novozym 435; 2,4-dimethyl-3-pentanol; 3 A molecular sieve; Shvo's catalyst In toluene at 70℃; under 210.021 Torr; for 215h; Kinetics;
adipic acid diisopropyl ester
6938-94-9

adipic acid diisopropyl ester

A

polymer, iterative tandem catalysis polymerization, ee = 92%, molecular weight = 10.7 kDa (GPC); monomer(s): 1,1'-(1,3-phenylene)diethanol; diisopropyl adipate

polymer, iterative tandem catalysis polymerization, ee = 92%, molecular weight = 10.7 kDa (GPC); monomer(s): 1,1'-(1,3-phenylene)diethanol; diisopropyl adipate

B

isopropyl alcohol
67-63-0

isopropyl alcohol

Conditions
ConditionsYield
With 2,4-dimethyl-3-pentanol; 3 A molecular sieve; Novozym 435 In toluene at 70℃; under 210.021 Torr; for 215h;A 98 % Turnov.
B n/a
adipic acid diisopropyl ester
6938-94-9

adipic acid diisopropyl ester

polymer, iterative tandem catalysis polymerization, ee = 92%, molecular weight = 7.7 kDa (GPC); monomer(s): 1,1'-(1,3-phenylene)diethanol; diisopropyl adipate

polymer, iterative tandem catalysis polymerization, ee = 92%, molecular weight = 7.7 kDa (GPC); monomer(s): 1,1'-(1,3-phenylene)diethanol; diisopropyl adipate

Conditions
ConditionsYield
With Novozym 435; 2,4-dimethyl-3-pentanol; 3 A molecular sieve; Shvo's catalyst In toluene at 70℃; under 210.021 Torr; for 121h; Kinetics;
adipic acid diisopropyl ester
6938-94-9

adipic acid diisopropyl ester

A

polymer, iterative tandem catalysis polymerization, ee = 92%, molecular weight = 7.7 kDa (GPC); monomer(s): 1,1'-(1,3-phenylene)diethanol; diisopropyl adipate

polymer, iterative tandem catalysis polymerization, ee = 92%, molecular weight = 7.7 kDa (GPC); monomer(s): 1,1'-(1,3-phenylene)diethanol; diisopropyl adipate

B

isopropyl alcohol
67-63-0

isopropyl alcohol

Conditions
ConditionsYield
With 2,4-dimethyl-3-pentanol; 3 A molecular sieve; Novozym 435 In toluene at 70℃; under 210.021 Torr; for 121h;A 98 % Turnov.
B n/a
adipic acid diisopropyl ester
6938-94-9

adipic acid diisopropyl ester

polymer, iterative tandem catalysis polymerization, ee = 93%, molecular weight = 7.2 kDa (GPC); monomer(s): 1,1'-(1,3-phenylene)diethanol; diisopropyl adipate

polymer, iterative tandem catalysis polymerization, ee = 93%, molecular weight = 7.2 kDa (GPC); monomer(s): 1,1'-(1,3-phenylene)diethanol; diisopropyl adipate

Conditions
ConditionsYield
With Novozym 435; 2,4-dimethyl-3-pentanol; 3 A molecular sieve; Shvo's catalyst In toluene at 70℃; under 210.021 Torr; for 121h; Kinetics;
adipic acid diisopropyl ester
6938-94-9

adipic acid diisopropyl ester

A

polymer, iterative tandem catalysis polymerization, ee = 93%, molecular weight = 7.2 kDa (GPC); monomer(s): 1,1'-(1,3-phenylene)diethanol; diisopropyl adipate

polymer, iterative tandem catalysis polymerization, ee = 93%, molecular weight = 7.2 kDa (GPC); monomer(s): 1,1'-(1,3-phenylene)diethanol; diisopropyl adipate

B

isopropyl alcohol
67-63-0

isopropyl alcohol

Conditions
ConditionsYield
With 2,4-dimethyl-3-pentanol; 3 A molecular sieve; Novozym 435 In toluene at 70℃; under 210.021 Torr; for 121h;A 97 % Turnov.
B n/a
adipic acid diisopropyl ester
6938-94-9

adipic acid diisopropyl ester

polymer, iterative tandem catalysis polymerization, ee = 95%, molecular weight = 12.3 kDa (GPC); monomer(s): 1,1'-(1,3-phenylene)diethanol; diisopropyl adipate

polymer, iterative tandem catalysis polymerization, ee = 95%, molecular weight = 12.3 kDa (GPC); monomer(s): 1,1'-(1,3-phenylene)diethanol; diisopropyl adipate

Conditions
ConditionsYield
With Novozym 435; 2,4-dimethyl-3-pentanol; 3 A molecular sieve; Shvo's catalyst In toluene at 70℃; under 210.021 Torr; for 121h; Kinetics;
adipic acid diisopropyl ester
6938-94-9

adipic acid diisopropyl ester

A

polymer, iterative tandem catalysis polymerization, ee = 95%, molecular weight = 12.3 kDa (GPC); monomer(s): 1,1'-(1,3-phenylene)diethanol; diisopropyl adipate

polymer, iterative tandem catalysis polymerization, ee = 95%, molecular weight = 12.3 kDa (GPC); monomer(s): 1,1'-(1,3-phenylene)diethanol; diisopropyl adipate

B

isopropyl alcohol
67-63-0

isopropyl alcohol

Conditions
ConditionsYield
With 2,4-dimethyl-3-pentanol; 3 A molecular sieve; Novozym 435 In toluene at 70℃; under 210.021 Torr; for 121h;A 99 % Turnov.
B n/a
adipic acid diisopropyl ester
6938-94-9

adipic acid diisopropyl ester

polymer, iterative tandem catalysis polymerization, ee = 95%, molecular weight = 4.5 kDa (GPC); monomer(s): 1,1'-(1,3-phenylene)diethanol; diisopropyl adipate

polymer, iterative tandem catalysis polymerization, ee = 95%, molecular weight = 4.5 kDa (GPC); monomer(s): 1,1'-(1,3-phenylene)diethanol; diisopropyl adipate

Conditions
ConditionsYield
With Novozym 435; 2,4-dimethyl-3-pentanol; 3 A molecular sieve; Shvo's catalyst In toluene at 70℃; under 210.021 Torr; for 223h; Kinetics;

6938-94-9Relevant academic research and scientific papers

Oxidation of cyclohexanone and/or cyclohexanol catalyzed by Dawson-type polyoxometalates using hydrogen peroxide

Dermeche, Leila,Idrissou, Yasmina,Mazari, Tassadit,Moudjahed, Mohammed,Rabia, Cherifa

, (2022/03/07)

The oxidation of cyclohexanone, cyclohexanol or cyclohexanone/cyclohexanol mixture using as catalyst, Dawson-type polyoxometalates (POMs) of formula, α- and β-K6P2W18O62, α-K6P2Mo6W12O62 and α1-K7P2Mo5VW12O62 and hydrogen peroxide, carried out at 90 °C with a reaction time of 20 h, led to a high number of mono- and di-acids which were identified by GC-MS. Levulinic, 6-hydroxyhexanoic, adipic, glutaric and succinic acids, major products were evaluated by HPLC. Regardless of the substrate nature, all POMs exhibited high catalytic activity with 94–99% of conversion, whereas the formation of the different products is sensitively related to both the composition and symmetry of the POMs and the substrate nature. The main products are adipic acid in the presence of α-K6P2Mo6W12O62 and α1-K7P2Mo5VW12O62, levulinic acid in the presence of α1-K7P2Mo5VW12O62 and β-K6P2W18O62 and 6-hydroxyhexanoic acid in the presence of α- and β-K6P2W18O62. Graphical abstract: High catalytic activity was observed with?α- and?β-K6P2W18O62, α-K6P2Mo6W12O62 and α1-K7P2Mo5VW12O62 Dawson-type for the oxidation of cyclohexanone, cyclohexanol or cyclohexanone/cyclohexanol mixture, in the hydrogen peroxide presence, to several oxygenated products. Adipic, levulinic and 6-hydroxyhexanoic acids are the main products. The peroxo- species formed in situ could be the active sites.[Figure not available: see fulltext.]

Preparation process and equipment of diisopropyl adipate

-

Paragraph 0078-0119, (2021/07/01)

The invention relates to a preparation process of diisopropyl adipate. The finished product of diisopropyl adipate is obtained through esterification reaction, dealcoholization, distillation, water washing, dehydration and filtration. A homogeneous catalyst selected in the esterification reaction has high catalytic activity and improves the reaction efficiency, then a film evaporator is combined for separation and refining, a catalyst in the product is effectively removed, the product quality is improved, some impurities influencing the product quality are rapidly and effectively removed through warm water washing, and the obtained product is high in purity, can be stored for a long time, and has neglected corrosion to equipment and extremely small pollution to the environment. In addition, the invention also provides equipment for the preparation process of diisopropyl adipate. The equipment comprises a reaction kettle, a condenser, a water segregator, a distillation kettle, a dealcoholization tower, the film evaporator, a washing tank, a dehydrator, a filtering device and a finished product tank.

A Heterogeneous Pt-ReOx/C Catalyst for Making Renewable Adipates in One Step from Sugar Acids

Jang, Jun Hee,Ro, Insoo,Christopher, Phillip,Abu-Omar, Mahdi M.

, p. 95 - 109 (2021/01/12)

Renewable adipic acid is a value-added chemical for the production of bioderived nylon. Here, the one-step conversion of mucic acid to adipates was achieved in high yield through deoxydehydration (DODH) and catalytic transfer hydrogenation (CTH) by a bifunctional Pt-ReOx/C heterogeneous catalyst with isopropanol as solvent and reductant. The Pt-ReOx/C catalyst is reusable and was regenerated at least five times. The catalyst exhibits a broad substrate scope of various diols. Spectroscopic studies of Pt-ReOx/C revealed ReVII and Pt0 as the relevant species for DODH and CTH, respectively. Isotope labeling experiments support a monohydride mechanism for CTH over Pt. This work demonstrates a reusable bifunctional catalyst for a one-step valorization of sugar acids to a practical monomer, which opens the door to multifunctional catalysis streamlining valorization of biomass-derived molecules.

Efficient Palladium-Catalyzed Carbonylation of 1,3-Dienes: Selective Synthesis of Adipates and Other Aliphatic Diesters

Yang, Ji,Liu, Jiawang,Ge, Yao,Huang, Weiheng,Ferretti, Francesco,Neumann, Helfried,Jiao, Haijun,Franke, Robert,Jackstell, Ralf,Beller, Matthias

supporting information, p. 9527 - 9533 (2021/03/08)

The dicarbonylation of 1,3-butadiene to adipic acid derivatives offers the potential for a more cost-efficient and environmentally benign industrial process. However, the complex reaction network of regioisomeric carbonylation and isomerization pathways, make a selective and direct transformation particularly difficult. Here, we report surprising solvent effects on this palladium-catalysed process in the presence of 1,2-bis-di-tert-butylphosphin-oxylene (dtbpx) ligands, which allow adipate diester formation from 1,3-butadiene, carbon monoxide, and methanol with 97 % selectivity and 100 % atom-economy under scalable conditions. Under optimal conditions a variety of di- and triesters from 1,2- and 1,3-dienes can be obtained in good to excellent yields.

Direct synthesis of adipic acid esters via palladium-catalyzed carbonylation of 1,3-dienes

Yang, Ji,Liu, Jiawang,Neumann, Helfried,Franke, Robert,Jackstell, Ralf,Beller, Matthias

, p. 1514 - 1517 (2020/01/08)

The direct carbonylation of 1,3-butadiene offers the potential for a more cost-efficient and environmentally benign route to industrially important adipic acid derivatives. However, owing to the complex reaction network of regioisomeric carbonylation and isomerization pathways, a selective practical catalyst for this process has thus far proven elusive. Here, we report the design of a pyridyl-substituted bidentate phosphine ligand (HeMaRaphos) that, upon coordination to palladium, catalyzes adipate diester formation from 1,3-butadiene, carbon monoxide, and butanol with 97% selectivity and 100% atom-economy under industrially viable and scalable conditions (turnover number > 60,000). This catalyst system also affords access to a variety of other di- and triesters from 1,2- and 1,3-dienes.

Metal-free transesterification catalyzed by tetramethylammonium methyl carbonate

Hatano, Manabu,Tabata, Yuji,Yoshida, Yurika,Toh, Kohei,Yamashita, Kenji,Ogura, Yoshihiro,Ishihara, Kazuaki

supporting information, p. 1193 - 1198 (2018/03/27)

Environmentally benign metal-free tetramethylammonium methyl carbonate is effective as a catalyst for the chemoselective, scalable, and reusable transesterification of various esters and alcohols in common organic solvents. In situ-generated highly active species, tetramethylammonium alkoxides, can greatly avoid self-decomposition at ≤110 °C, and are reusable. In particular, chelating substrates, such as amino alcohols, diols, triols, sugar derivatives, alkaloids, α-amino acid esters, etc., which deactivate conventional metal salt catalysts, can be used. A 100 gram scale biodiesel production was also demonstrated.

Desymmetrizing Hydroformylation of Dihydromuconic Acid Diesters: Application to the Synthesis of (±)-Vindeburnol

Salacz, Laura,Charpentier, Cyrille,Suffert, Jean,Girard, Nicolas

, p. 2257 - 2262 (2017/02/26)

The desymmetrizing hydroformylation of internal alkenes derived from dihydromuconic acid is described. The study of this reaction afforded easy access to polyfunction aldehydes. After the evaluation of the reactivity of the dimethyl ester derivative with various primary amines, this methodology was used to design a rapid synthesis of (±)-vindeburnol from tryptamine in only two steps.

CYCLOHEXANE OXIDATION PROCESS BYPRODUCT DERIVATIVES AND METHODS FOR USING THE SAME

-

Page/Page column 50-51, (2010/08/05)

Disclosed are ester compositions, solvents, cleaning formulations, curing agents, reactive diluent solvents, controlled acid function release agents, polyol monomers, drilling mud and methods of making and using the same. Disclosed compositions include: a) about 10 to 60 weight percent methyl hydroxycaproate; b) about 20 to 80 weight percent dimethyl adipate; c) about 1 to 15 wt % of dimethyl glutarate; d) about 0.1 to 5 wt % of dimethyl succinate; e) about 0.1 to 7 wt % of at least one cyclohexanediol; and f) less than about 20 wt% oligomeric esters.

SKIN EXTERNAL PREPARATIONS AND COSMETICS

-

, (2010/12/29)

An object of the present invention is to provide skin external preparations and cosmetics which contain a branched acyl carnitine and have excellent formulation stability. A skin external preparation of the present invention includes a carnitine derivative represented by the following Formula (1) and/or a carnitine derivative salt represented by the following Formula (2), and an amphoteric surfactant. In Formula (1), R1 and R2 are each independently a C1-18 optionally branched, saturated or unsaturated aliphatic hydrocarbon group. In Formula (2), R1 and R2 are the same as in Formula (1), X? is a specific anion and Y+ is a specific cation.

Synergism of microwaves and immobilized enzyme catalysis in synthesis of adipic acid esters in nonaqueous media

Yadav, Ganapati D.,Lathi, Piyush S.

, p. 1699 - 1705 (2007/10/03)

Low-energy microwave irradiation leads to enhancement by a factor of up to 2.63 in comparison with conventional heating in immobilized lipase-catalyzed esterification of adipic acid with various alcohols and this effect is due to the greater frequency of collision, without any change in activation energy of the two modes of heating. Copyright Taylor & Francis, Inc.

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