WO2011005735A1 - Green and atom-economical processes for producing phenolic antioxidants - Google Patents
Green and atom-economical processes for producing phenolic antioxidants Download PDFInfo
- Publication number
- WO2011005735A1 WO2011005735A1 PCT/US2010/041029 US2010041029W WO2011005735A1 WO 2011005735 A1 WO2011005735 A1 WO 2011005735A1 US 2010041029 W US2010041029 W US 2010041029W WO 2011005735 A1 WO2011005735 A1 WO 2011005735A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- tert
- butyl
- acetic acid
- acetoxymethylphenol
- butylphenol
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Ceased
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C37/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring
- C07C37/11—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring by reactions increasing the number of carbon atoms
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C37/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring
- C07C37/11—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring by reactions increasing the number of carbon atoms
- C07C37/16—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring by reactions increasing the number of carbon atoms by condensation involving hydroxy groups of phenols or alcohols or the ether or mineral ester group derived therefrom
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C67/00—Preparation of carboxylic acid esters
- C07C67/08—Preparation of carboxylic acid esters by reacting carboxylic acids or symmetrical anhydrides with the hydroxy or O-metal group of organic compounds
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/04—Oxygen-containing compounds
- C08K5/13—Phenols; Phenolates
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2601/00—Systems containing only non-condensed rings
- C07C2601/12—Systems containing only non-condensed rings with a six-membered ring
- C07C2601/16—Systems containing only non-condensed rings with a six-membered ring the ring being unsaturated
Definitions
- phenolic antioxidants When added to fuels, and/or used in the production thereof, phenolic antioxidants can extend storage life and protect fuel systems, increase resistance to oxidation, help control insoluble gum formation, and help petroleum and biofuel refiners and marketers meet stringent government regulations and OEM standards, including those requiring reduced emissions.
- phenolic antioxidants When added to lubricants, and/or used in the production thereof, phenolic antioxidants can enhance thermal stability, improve lubricant performance and reduce sludge formation, extending the useful life of lubricants in virtually any application. They reduce thickening and inhibit acid formation in a variety of applications, including engine oils, automatic transmission fluids, industrial oils, as well as compressor oil and gear and hydraulic oils.
- phenolic antioxidants When added to polymers, and/or used in the production thereof, phenolic antioxidants can maintain the performance integrity and processing stability of plastics, elastomers, adhesives and other materials.
- This invention meets the above-described needs by providing processes for producing 1 ,3,5-trimelhyl-2,4,6-tris(3 ,5-diaIkyl-4-hydiOxybenzyl)benzcne ("Product”), which processes comprise combining at least acetic acid, paraformaldehyde, 2,6-di-tert-butylphenol, and a secondary amine to yield at least 2,6-di-tert-butyl-4-acetoxymethylphenol, isolating at least the 2,6-di-tert-butyl-4-acetoxymethylphenol as a solid or a melt, dissolving at least the 2,6-di-tert-butyI-4-acetoxymethylphenol in acetic acid to form a solution, combining at least the solution, mesitylene, and a catalytic amount of an acid catalyst, and yielding at least a l,3,5-trimethyl-2,4,6-tris(3,5-
- This invention also provides processes for producing l,3,5-trimethyl-2,4,6-tris(3,5- dialkyl-4-hydroxybenzyl)benzene, which processes comprise combining acetic acid, paraformaldehyde, a secondary amine, and 2,6-di-tert-butylphenol to yield a solution comprising at least 2,6-di-tert-butyl-4-acetoxymethylphenol, combining at least the solution, mesitylene, and a catalytic amount of an acid catalyst, and yielding at least a 1,3,5-trimethyl- 2,4,6-tris(3,5-dialkyl-4-hydroxybenzyl)benzene.
- 2,6 ⁇ di-tert-butyl-4- acetoxymethylphenol is produced in situ, and no isolation step is required.
- processes that comprise combining at least acetic acid, paraformaldehyde, a secondary amine, and 2,6-di-tert-butylphenol to yield at least 2,6-di-tert-butyl-4-acetoxymethylphenol, combining at least the 2,6-di ⁇ tert-butyl-4-acetoxymethylphenol, mesitylene, and a catalytic amount of an acid catalyst, and yielding at least l,3,5-trimethyl-2,4,6-tris(3,5-dialkyl-4- hydroxybenzyl)benzene.
- paraformaldehyde is in excess as to the 2,6-di-tert-butylphenol, and wherein unreacted paraformaldehyde is recovered.
- This invention also provides product compositions comprising 2,6-di-tcrt-butyI-4- acetoxymethylphenol, 2,6-di-tert-butylphenol, 2 > 6-di-tert-butyl-4-hydroxymethylphenol, and 4,4'-methyIenebis(2,6-di-tert-butylphenol).
- 2,6-di-teit-butyl-4-methoxymethylphenol is dissolved in acetic acid and reacted with mesitylene in the presence of an acid catalyst like sulfuric acid to produce at least l,3,5-trimethyl-2,4,6-tris(3,5-diaIkyl-4-hydroxybenzyl)benzene.
- 2,6-di- tert-butyl-4-methoxymethylphenol may be dissolved in acetic acid and converted to 2,6-di-t- butyl-4-acetoxymethylphenol in the presence of catalytic amount of an acid catalyst and at temperatures of 20 to 100°C followed by the addition of niesitylene to produce at least 1 ,3,5- trimethyl-2,4,6-tris(3,5-dialkyl-4-hydroxybenzyl)benzene.
- the intermediate 2,6-di-t-butyl-4-acetoxymethylphenol is prepared from the reaction of 2,6-di-t-butylphenoI with paraformaldehyde in acetic acid solvent and a secondary amine producing a composition comprising 2,6-di-tert-butyl-4-acetoxymethylphenol, 2,6-di- tert-butylphenol, 2,6-di-tert-butyl-4-hydroxymethylphenol, and 4,4'-methylenebis(2,6-di-tert- butylphenol).
- the product 2, ⁇ -di-t-butyl-4-acetoxymethylphenol may be purified by crystallization or precipitation from the reaction mass.
- reaction mass maybe used for reaction with mesitylene in the presence of and acid catalyst.
- Paraformaldehyde and 2,6-di-t- butylphenol may be used in equal molar amounts or a 10 to 50% molar excess of formaldehyde may be used in producing the compositions of this invention.
- the intermediate 2 > 6-di-t-butyl-4-acetoxymethylphenol is prepared from the reaction of 2,6-di-t-butylphenol with excess paraformaldehyde in acetic acid solvent and a secondary amine.
- the intermediate 2,6-di-t-butyl-4-acetoxymethylphenol may be purified in the molten state by repeated washing with water to remove excess formaldehyde. It may further be purified by crystallization from acetic acid. Alternatively, it may be precipitated from a hydrocarbon solvent like heptane and filtered. Or, it may be crystallized from the reaction mixture by cooling the acetic acid reaction mixture to 0-15 0 C, and subsequently filtering the solid product. The product may be further purified by re-crystallization.
- 2,6-di-tert-butylphenol is first reacted with paraformaldehyde in acetic acid in the presence of a secondary amine followed by the acidification of the reaction mixture with an acid and addition of mesitylene producing 1,3,5- trimethyl-2,4,6-tris(3,5-dialkyl-4-hydroxybenzyl)benzene which is precipitated on cooling the reaction mixture to 5-10 0 C and isolating the product by filtration.
- 2,6-di-tert-butylphenol maybe used as a solid, or dissolved in the appropriate solvent, or as a melt.
- This invention is advantageous in that Product can be produced in the absence of a hydrocarbon solvent or a halohydrocarbon solvent, such as dichloromethane or 1,1 ,1- trichloroethane, or an alcohol such as methanol. Moreover, the process is carried out with an environmentally friendly "green” solvent like acetic acid which can be recycled thus minimizing emissions and hazardous waste. This process also eliminates isolation and purification of intermediates and reduces aqueous waste and organic wastes.
- a hydrocarbon solvent or a halohydrocarbon solvent such as dichloromethane or 1,1 ,1- trichloroethane
- an alcohol such as methanol
- This invention is additionally advantageous in that the intermediate 2,6-dialkyl-4-acetoxymethylphcnol can be produced in situ from 2,6-di-tert-butylphenol or 2,6-dialkyl-4-methoxymethylphenol and used without isolation or purification to produce l,3,5-trimethyl-2,4,6-tris(3,5-di-tert-butyl-4- hydroxybenzyl)benzcne.
- the 2,6-diallkylphenol moiety of the 2,6-dialkyl-4-methoxymethylphenol and 2,6- dialkyl-4-acctoxymcthylphenol which are reacted with mesitylene in the practice of this invention may be any one or more of the 2,6-dialkylphenol moieties of the 2,6-dialkyl-4- methoxymethylphenols of Mina et al. and Goddard et al., the teachings of which are incorporated herein by reference. Thus, as in Mina et al.
- the "alkyl" groups in the 2- and 6-positions may be alkyl, cycloalkyl, or aralkyl groups and may be the same or different; and the phenols include, e.g., the 2,6-dimethyl-, 2,6-diisopropyl-, 2,6- diisobutyl-, 2,6-di-sec-butyI-, 2,6-di-t-butyl-, 2,6-dicyclopentyl-, 2,6-dicyclohexyl-, 2,6- dibenzyl-, 2,6-di( ⁇ -methylbenzyl)-, 2-methyl-6-t-butyl-, 2-mcthyl-6-t-octyl-, 2-methyl-6- cyclopentyl-, 2-methyl- ⁇ -benzyl-, 2-mcthyl-6-( ⁇ -methylbenzyl)-, 2-isopropyl-6-( ⁇ , ⁇ - dimethyl
- the 2, ⁇ -dialkyl-4-methoxymethylphenol and 2,6-dialkyl-4-acetoxymethylphenol are employed in a stoichiometric sufficiency or excess, usually an amount such as to provide about 3-5, or about 3.3-4.0 mols of the phenol per mol of mesitylene.
- Processes of this invention utilize carboxylic acids with boiling points that are low, i.e., about the same as carboxylic acids such as acetic acid, propionic acid, and butyric acid, all of which can be used in processes of this invention,
- Processes of this invention utilize acid catalysts that are Bronsted acids and organic acids that have acidities stronger than acetic or propionic acid.
- Such acid catalysts have acidities stronger than carboxylic acids like acetic acid. Examples of such acids are alkyl sulfonic acids, aryl sulfonic acids, chloroacetic acid, trifluoroacetic acid, sulfuric acid and the like.
- Processes of this invention utilize secondary amines like dimethylamine, diethylamine, methyl ethyl amine, diisopropylamine, methyl isoproplyamine, ethylisopropylamine, dipropylamine, methylproplyamine, ethylpropylamine, di-butylamine, methylbutylamine, ethylbutylamine, proplybutyl amine, diphenylamine, phenylnaphthylamine, piperidine, piperazine and the like.
- the secondary amine acts as a catalyst in reactions that occur in processes of this invention.
- 0024] Processes of this invention can be conducted from about 50 0 C to about 12O 0 C with catalytic amounts of acid.
- the Product having 97-99.5% purity can be precipitated out of the reaction mixture as soon as it is formed.
- the Product can simply be filtered in air; the solid Product can be washed with water to remove acetic acid and dried at about 100 0 C under reduced pressure.
- Product may be further purified by re-crystallization from an appropriate solvent.
- Example 1 was repeated but 2,6-di-tert-butyl-4-methoxymethylphenoI (213.5 g of 89.2 wt%, 0.76 mol) was added as a melt to the reaction mixture.
- a portion of the produced product was processed to provide a product of improved purity, comprising 2,6-di-tert-butyl-4-acetoxymethylphenol (95%).
- a three-necked flask was charged with the thus-produced 2,6-di-tcrt-butyl-4-acetoxymethylphenol (18.1 g of 95%), mesitylene (2.4 g), acetic acid (80 g), and sulfuric acid (1 g, 98%) at room temperature and under nitrogen.
- the reaction mixture was stirred at room temperature for 22 hrs and at 6O 0 C for five more hours.
- NMR assay showed a 23 wt% solution of 2,6-di-tert-butyl-4-acetoxymethylphcnol.
- Mesitylene (17.2 g) was added, the mixture was stirred, sulfuric acid (14 g, 98%) was added, and the mixture was heated and held at 5O 0 C for five hours.
- GC Analysis showed the presence of unreacted starting material. The reaction mixture was heated and held at 8O 0 C for one hour. The reaction slurry was cooled to 5 0 C and filtered. The resulting pink powder was heated under vacuum (10-15 raraHg) and 75 0 C for one hour.
- reactants and components are identified as ingredients to be brought together in connection with performing a desired chemical reaction or in forming a combination to be used in conducting a desired reaction. Accordingly, even though the claims hereinafter may refer to substances, components and/or ingredients in the present tense ("comprises”, “is”, etc.), the reference is to the substance, component or ingredient as it existed at the time just before it was first contacted, combined, in situ blended or mixed with one or more other substances, components and/or ingredients in accordance with the present disclosure. Whatever transformations, if any, which occur as a reaction is conducted is what the claim is intended to cover.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
Description
Claims
Priority Applications (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR1020127000303A KR101750438B1 (en) | 2009-07-10 | 2010-07-06 | Green and atom-economical processes for producing phenolic antioxidants |
| US13/382,683 US8766016B2 (en) | 2009-07-10 | 2010-07-06 | Green and atom-economical processes for producing phenolic antioxidants |
| CN201080030923.1A CN102471197B (en) | 2009-07-10 | 2010-07-06 | Green and atom-economical processes for producing phenolic antioxidants |
| KR1020167034504A KR20170003982A (en) | 2009-07-10 | 2010-07-06 | Green and atom-economical processes for producing phenolic antioxidants |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US22471709P | 2009-07-10 | 2009-07-10 | |
| US61/224,717 | 2009-07-10 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2011005735A1 true WO2011005735A1 (en) | 2011-01-13 |
Family
ID=42492046
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/US2010/041029 Ceased WO2011005735A1 (en) | 2009-07-10 | 2010-07-06 | Green and atom-economical processes for producing phenolic antioxidants |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US8766016B2 (en) |
| KR (2) | KR101750438B1 (en) |
| CN (1) | CN102471197B (en) |
| TW (1) | TWI490195B (en) |
| WO (1) | WO2011005735A1 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102503778A (en) * | 2011-10-28 | 2012-06-20 | 淮安嘉诚高新化工股份有限公司 | Synthesis method of antioxidant 330 |
| CN105523899A (en) * | 2015-07-06 | 2016-04-27 | 中国科学院宁波材料技术与工程研究所 | Cleaner production method and use of bisphenol compound anti-oxidant |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113512232A (en) * | 2020-04-10 | 2021-10-19 | 中国石油天然气股份有限公司 | Macromolecular hindered phenol antioxidant and preparation method and application thereof |
| CN111718241B (en) * | 2020-07-29 | 2023-06-27 | 运城鸿博化工有限公司 | Industrial production method of hindered phenol antioxidant 1330 |
| CN113773256B (en) * | 2021-09-16 | 2022-11-18 | 精华制药集团南通有限公司 | Synthesis method of amber |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1931062A1 (en) * | 1968-06-21 | 1970-10-15 | Shell Int Research | Process for the preparation of 1,3,5-trialkyl-2,4,6-tris (3,5-dialkyl-4-hydroxybenzyl) benzenes |
| WO1984002336A1 (en) | 1982-12-16 | 1984-06-21 | Ethyl Corp | Antioxidant synthesis |
| US4992597A (en) | 1989-09-25 | 1991-02-12 | Ethyl Corporation | Antioxidant process |
| US4994628A (en) | 1989-09-25 | 1991-02-19 | Ethyl Corporation | Phenolic antioxidant process |
| US5292969A (en) | 1993-04-01 | 1994-03-08 | Ethyl Corporation | Phenolic antioxidant and process |
Family Cites Families (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1202762A (en) | 1968-06-21 | 1970-08-19 | Shell Int Research | Esters of substituted benzyl alcohols and polyphenols prepared from said esters |
| US3925488A (en) | 1971-05-24 | 1975-12-09 | Ethyl Corp | Process for the production of 1,3,5-trimethy-2,4,6-tris(3,5-di-tert-alkyl-4-hydroxybenzyl)benzene |
| US4340767A (en) | 1981-05-14 | 1982-07-20 | Ethyl Corporation | Antioxidant process using formaldehyde |
| US4754077A (en) | 1982-12-16 | 1988-06-28 | Ethyl Corporation | Antioxidant synthesis |
| JPS6130544A (en) | 1984-07-23 | 1986-02-12 | Mitsui Petrochem Ind Ltd | Preparation of 1,3,5-trialkyl-2,4,6-tris(3,5-dialkyl-4-hydroxybenzyl)benzene |
| DE69024445T2 (en) | 1989-09-25 | 1996-05-09 | Albemarle Corp | Manufacture of antioxidants |
| US5891952A (en) * | 1997-10-01 | 1999-04-06 | Henkel Corporation | Aqueous compositions containing polyphenol copolymers and processes for their preparation |
| FR2769310B1 (en) * | 1997-10-08 | 2000-02-18 | Rhodia Chimie Sa | PROCESS FOR AMIDOALKYLATION OF A PHENOLIC COMPOUND CARRYING AN ELECTRO-DONOR GROUP |
-
2010
- 2010-07-06 US US13/382,683 patent/US8766016B2/en active Active
- 2010-07-06 KR KR1020127000303A patent/KR101750438B1/en not_active Expired - Fee Related
- 2010-07-06 KR KR1020167034504A patent/KR20170003982A/en not_active Ceased
- 2010-07-06 CN CN201080030923.1A patent/CN102471197B/en not_active Expired - Fee Related
- 2010-07-06 WO PCT/US2010/041029 patent/WO2011005735A1/en not_active Ceased
- 2010-07-08 TW TW099122412A patent/TWI490195B/en not_active IP Right Cessation
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1931062A1 (en) * | 1968-06-21 | 1970-10-15 | Shell Int Research | Process for the preparation of 1,3,5-trialkyl-2,4,6-tris (3,5-dialkyl-4-hydroxybenzyl) benzenes |
| WO1984002336A1 (en) | 1982-12-16 | 1984-06-21 | Ethyl Corp | Antioxidant synthesis |
| US4992597A (en) | 1989-09-25 | 1991-02-12 | Ethyl Corporation | Antioxidant process |
| US4994628A (en) | 1989-09-25 | 1991-02-19 | Ethyl Corporation | Phenolic antioxidant process |
| US5292969A (en) | 1993-04-01 | 1994-03-08 | Ethyl Corporation | Phenolic antioxidant and process |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102503778A (en) * | 2011-10-28 | 2012-06-20 | 淮安嘉诚高新化工股份有限公司 | Synthesis method of antioxidant 330 |
| CN102503778B (en) * | 2011-10-28 | 2014-02-12 | 淮安嘉诚高新化工股份有限公司 | Synthesis method of antioxidant 330 |
| CN105523899A (en) * | 2015-07-06 | 2016-04-27 | 中国科学院宁波材料技术与工程研究所 | Cleaner production method and use of bisphenol compound anti-oxidant |
| CN105523899B (en) * | 2015-07-06 | 2017-07-28 | 中国科学院宁波材料技术与工程研究所 | A kind of clean preparation method of bisphenol compound antioxidant and application |
Also Published As
| Publication number | Publication date |
|---|---|
| US20120108854A1 (en) | 2012-05-03 |
| CN102471197A (en) | 2012-05-23 |
| KR20120035178A (en) | 2012-04-13 |
| US8766016B2 (en) | 2014-07-01 |
| KR101750438B1 (en) | 2017-06-23 |
| TW201111333A (en) | 2011-04-01 |
| KR20170003982A (en) | 2017-01-10 |
| CN102471197B (en) | 2015-01-14 |
| TWI490195B (en) | 2015-07-01 |
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