WO2011005735A1 - Green and atom-economical processes for producing phenolic antioxidants - Google Patents

Green and atom-economical processes for producing phenolic antioxidants Download PDF

Info

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
Application number
PCT/US2010/041029
Other languages
French (fr)
Inventor
Mahmood Sabahi
Thomas Robert Nicholas
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Albemarle Corp
Original Assignee
Albemarle Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Albemarle Corp filed Critical Albemarle Corp
Priority to KR1020127000303A priority Critical patent/KR101750438B1/en
Priority to US13/382,683 priority patent/US8766016B2/en
Priority to CN201080030923.1A priority patent/CN102471197B/en
Priority to KR1020167034504A priority patent/KR20170003982A/en
Publication of WO2011005735A1 publication Critical patent/WO2011005735A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C37/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring
    • C07C37/11Preparation 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
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C37/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring
    • C07C37/11Preparation 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
    • C07C37/16Preparation 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
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00Preparation of carboxylic acid esters
    • C07C67/08Preparation of carboxylic acid esters by reacting carboxylic acids or symmetrical anhydrides with the hydroxy or O-metal group of organic compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/04Oxygen-containing compounds
    • C08K5/13Phenols; Phenolates
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2601/00Systems containing only non-condensed rings
    • C07C2601/12Systems containing only non-condensed rings with a six-membered ring
    • C07C2601/16Systems 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.

Landscapes

  • 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

Processes for producing 1,3,5-trimethyI-2,4,6-tris(3,5-dialkyl-4- hydroxybenzyl)benzene are provided, in particular such processes that utilize 2,6-di-tert- butylphenol, paraformaldehyde, a secondary amine, mesitylene, and acetic acid.

Description

GREEN AND ATOM-ECONOMICAL PROCESSES FOR PRODUCING
PHENOLIC ANTIOXIDANTS
BACKGROUND
[0001] 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.
[0002] 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.
[0003] 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.
[0004] It is known that l,3,5-trimethyl-2,4,6-tris(3,5-dialkyl-4-hydroxybenzyl)benzenes are useful phenolic antioxidants - and processes for making these l,3,5-trimethyl-2,4,6-tris(3,5- dialkyl-4-hydroxybenzyl)benzenes are known, For example, it is known that 1,3,5-trimethyl- 2,4,6-tris(3,5-dialkyI-4-hydroxybenzyl)benzenes can be prepared by reacting mesitylene with the appropriate 2,6-dialkyl-4-methoxymethylphenol in the presence of an acidic catalyst. See, e.g., U.S. Pat. Nos. 4,992,597 (Mina et al.), 4,994,628 (Goddard et al.), and 5,292,969 (Berris). See also International Publication No. WO 84/02336 (Mina).
[0005] However, given the extensive need for all of the products in which 1,3,5-trimethyl- 2,4,ό-tris(3,5-dialkyl-4-hydroxybenzyl)benzcne antioxidants are useful, there is a need for improved and environmentally friendly "green" processes for producing such antioxidants that would eliminate the use of hazardous solvents, eliminate the isolation of intermediates, significantly reduce hazardous waste, and lower costs. THE INVENTION
[0006] 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-dialkyl-4-hydroxybenzyl)benzene. Such processes further comprise recovering the acetic acid for use in another process.
[0007] 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. In such processes, 2,6~di-tert-butyl-4- acetoxymethylphenol is produced in situ, and no isolation step is required. Also provided are 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. Also provided are such processes wherein the paraformaldehyde is in excess as to the 2,6-di-tert-butylphenol, and wherein unreacted paraformaldehyde is recovered.
[0008] 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).
[0009] Also provided are processes that comprise combining at least acetic acid, paraformaldehyde, a secondary amine, and 2,6-di-tert-butylphcnoI to yield at least 2,6-di-tert- butyl-4-acetoxymethyIphenol, isolating at least the 2,6-di-tert-butyl-4-acetoxymethylphenol as a solid or a melt, dissolving at least the 2,ό-di-tcrt-butyl-4-acetoxyinethylphenol solid or melt in at least 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- dialkyl-4-liydroxybenzy])benzene.
fOOlO] Also provided are 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-acetoxymethyIphenol, isolating at least the 2,6-di-tert-butyl-4- acetoxymcthylphenol as a solid or a melt, combining at least the 2,6-di-tert-butyl-4- acetoxymethylphenol, 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.
[0011] Also provided are processes that comprise combining at least acetic acid, paraformaldehyde, a secondary amine, and 2,6-di-tert-butylphenol to yield a solution comprising at least 2,ό-di-tert-butyl-4-acetoxymethylphenol, acidifying the solution, combining at least the 2,ό-di-tert-butyl-4-acetoxymethylphenol, mesitylene, and a catalytic amount of an acid catalyst, and yielding at least a l,3,5-trimethyl-2,4,6-tris(3,5-dialkyl-4- hydroxybenzyl)benzene.
[0012] Also provided are processes that comprise combining at least 2,6-di-tert-butyl-4- methoxymethylphenol, acetic acid, mesitylene, and an acid catalyst, and yielding at least l,3,5-trimethyl-2,4,6-tris(3,5-dialkyl-4-hydroxybenzyl)benzene.
[0013] The reaction scheme for one of the processes of this invention can be illustrated as follows:
Figure imgf000004_0001
In this process, 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. Alternatively, 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.
[0014] The reaction scheme for another one of the processes of this invention can be illustrated as follows:
Figure imgf000005_0001
2 , 6-d i-t-butyl -4-acetoxyphenol
In this process, 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,ό-di-t-butyl-4-acetoxymethylphenol may be purified by crystallization or precipitation from the reaction mass. Or the 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.
[0015] The reaction scheme for another one of the processes of this invention can be illustrated as follows:
+ 3 Acetic acid
Figure imgf000005_0002
In this process, 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 0-150C, and subsequently filtering the solid product. The product may be further purified by re-crystallization.
(0016] Yet another reaction scheme for the processes of this invention can be illustrated as follows:
Figure imgf000006_0001
In this one-pot, two-step, one solvent process, 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 5-100C and isolating the product by filtration.
[0017] In the processes of this invention, 2,6-di-tert-butylphenol maybe used as a solid, or dissolved in the appropriate solvent, or as a melt. In the laboratory operations, it was usually dissolved in the solvent of the reaction for convenience. However, it is known to the people skilled in the art that in industrial operations it would conveniently be utilized as a melt (liquid) with or without the use of a diluting solvent.
[0018] 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. 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.
[0019] 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. and Goddard 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(α-methylbenzyl)-, 2-methyl-6-t-butyl-, 2-mcthyl-6-t-octyl-, 2-methyl-6- cyclopentyl-, 2-methyl-ό-benzyl-, 2-mcthyl-6-(α-methylbenzyl)-, 2-isopropyl-6-(α,α - dimethylbenzyl)-, and 2-t-butyl-6-cyclooctyl-4- phenols.
[0020] As is customary in l,3,5-trimethyl-2,4,6-tris(3,5-dialkyl-4-hydroxybenzyl)benzene syntheses, the 2,ό-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.
[0021] 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,
[0022] 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.
[0023] 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 500C to about 12O0C with catalytic amounts of acid.
[0025] In the processes of this invention, the Product having 97-99.5% purity can be precipitated out of the reaction mixture as soon as it is formed. At the end of the reaction, the Product can simply be filtered in air; the solid Product can be washed with water to remove acetic acid and dried at about 1000C under reduced pressure. Product may be further purified by re-crystallization from an appropriate solvent.
EXAMPLES
[0026] The following examples are illustrative of the principles of this invention. It is understood that this invention is not limited to any one specific embodiment exemplified herein, whether in the examples or the remainder of this patent application.
Example 1: Preparation of l,3,5-trimethyl-2,4,6-tris(3,5-di-tert-butyl-4- hydroxy benzyl) benzene
[0027] In a four-necked flask equipped with a stirrer, distillation head, heated-addition funnel, and thermometer was placed mesitylene (30 g, 0.25 mol) and acetic acid (52 g) at room temperature and under a mild flow of nitrogen. 2,6-di-tert-Butyl-4- methoxymethylphenol (213.5 g of 89.2 wt%, 0.76 mol) was dissolved in acetic acid (520 g) and placed in the heated addition funnel (total volume of 750 mL) and a fraction of it (27%) was added to the reaction mixture and heated to 7O0C. Sulfuric acid (3.9 g of 98%) was added with stirring and after five minutes, the addition of 2,6-di-tert-butyl-4- methoxymcthylphenol solution at 7O0C was started and it was completed in three hours. The condensate was collected and analysis showed a mixture of methyl acetate and acetic acid. After a total of six hours at 700C, acetic acid was partially removed by distillation under reduced pressure (225 g, at 50-550C and 70 ramHg). The resulting slurry was filtered and the solid was dried in air (196.3 g) then dissolved in heptane (1000 g) and heated to 75-8O0C and washed with water (2x500 g) and adjusted the pH to about 5 by addition of potassium carbonate. The organic phase was dried by azeotropic distillation. Upon cooling to about 50C, l,3,5-trimethyl-2,4,6-tris(3,5-di-tert-butyl-4-hydroxybenzyl)benzene precipitated as a white powder that was isolated and dried. LC analysis showed 98.5% of 1 ,3,5-trimethyl- 2,4,6-tris(3,5-di-tert-butyl-4-hydroxybcnzyl)benzene, and 0.21 wt% of l,3,5-trimethyl-2,4- di(3 , 5 - di-tert-butyl -4 -hydroxybenzyl )b enzene.
Example 2: Preparation of l,3,5-trimethyl-2,4,6-tris(3,5-di-tert~butyl-4- hydroxybenzyijbenzene
[0028] 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.
Example 3: Preparation of l,3,5-trimethyl-2,4,6-tris(3,5-dϊ-tert-butyl-4- hydroxybenzyl)benzene
[0029] Mesitylene (12 g, 0.1 mol) and 2,6-di-tert-butyl-4-methoxymethylphenol (80 g of 98%, 0.31 mol) were added to a reactor containing acetic acid (280 g) and the mixture was stirred at room temperature under nitrogen. Sulfuric acid (0.5 g of 98%) was added and the reaction mixture was heated at 600C for six hours. The resulting slurry was filtered and the solid was washed with water (500 g), dissolved in heptane and dried by azeotropic removal of water. The product, l,3,5-trimethyl-2,436-tris(3,5-di-teit-butyl-4-hydroxybenzyl)benzene, precipitated on cooling to 0-5°C and isolated as white powder (63 g, 81.4%). Analysis showed 97.4% of l,3,5-trimethyl-2,4,6-tris(3,5-di-tert-butyl-4-hydroxybenzyl)benzene, and 1.9 wt% of l,3,5-trimethyl-2,4-di(3,5-di-tert-butyl-4-hydroxybenzyl)benzene.
Example 4: Preparation of l,3,5-trimethyl-2,4,6-tris(3,5-di-tert-butyl-4- hydroxybenzyl)benzene froni 2,6~di-tert-butyl-4-acetoxymethylphenol
Example 4(a) - Preparation of 2,6-di-tert-butyl-4-acetoxymethylphenoI
[0030] 2,6-di-tert-Butylphenol (131.8 g, 0.64 mol) was dissolved in acetic acid (150 g) and the resulting solution was added to a flask containing paraformaldehyde (26.2 g of 95%), diethyl amine (5.8 g) and acetic acid (450 g) over a period of five hours and at reflux temperature. After 1 1 hrs, most of the solvent was removed under reduced pressure and 650C and the residue was heated to 85-900C and the resulting melt was washed with hot water at 90-95°C (3x200 g). The product was dried by addition of heptane and azeotropic distillation and isolated as a bright yellow solid (178 g) after cooling to about 5°C. Analysis by GC- mass, GC, and NMR showed a product comprising 2,6-di-tert-butyl-4-acetoxymethylphenol (85.5 %), 2,6-di-tert-butylphenol (0.6%), 2!6-di-tert-butyl-4-hydroxymethylphenol (2.5%), and 4,4'-methylenebis(256-di-tert-butylphenol) (4%).
Example 4(b) - Preparation of l,3,5-trimethyl-2,4,6-tris(3,5-di-tert-butyI-4- hydroxy benzyl) benzene
[0031] To an acetic acid solution of 73 g of the thus produced product comprising 2,6-di- tert-butyl-4-acetoxymethylphenol (85.5% by GC) was added mesitylene (2.4 g) and sulfuric acid (2 g, 98%); the resulting solution was heated at 600C for six hours. Most of the acetic acid was removed under reduced pressure and 65-7O0C; the resulting paste was dissolved in heptane (120 g); and the resulting solution was washed with water (2x60 g) at 70-750C. The solution was dried by azeotropic removal of water and cooled to ambient temperature; 1,3,5- trimethyl-2,4,6-tris(3,5-di-tert-butyl-4-hydroxybenzyl)benzene was isolated as an off-white solid (8. I g).
Example 4(c) - Preparation of l,3,5-trimethyl-2,4,6-tris(3,5-di-tert-butyl-4- hydroxybenzyl)benzene
[0032] Experiment 3(b) was repeated with the crude acetic acid solution of 2,6-di-tert- butyl-4-acetoxymethylphenol (170 g), mesitylene (18.6 g), and sulfuric acid (5 g). After three hours of heating at 6O0C the reaction mixture was poured over cold water (500 g) and the solid precipitate was filtered and dried in air. The crude product was dissolved in heptane (600 g), washed the organic layer with water (3x100 g) at 8O0C, and dried by azeotropic distillation. Product was precipitated after cooling to 2 - 3°C and isolated as an off-white solid (75 g). Analysis showed 97.1% of l ,3,5-trimethyl-2,4,6-tris(3,5-di-tert-butyl-4- hydroxybenzyl)benzene and 1.9 wt% l,3,5-trimethyl-2,4-di(3,5-di-tert-butyl-4- hydroxybenzyl)benzene.
Example 4(d) - Preparation of l,3,5-trimethyl-2,4,6-tris(3,5-di-tert-butyI-4- hydroxybenzyl)benzene
[0033] 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 6O0C for five more hours. The slurry was cooled to 100C and filtered and the solid was washed with water (400 mL) and dried under vacuum at 70-750C to afford 13.8 g white powder. LC- Analysis showed 99% l,3)5-trimethyl-2,4J6-tris(3,5-di-tert-butyl-4- hydroxybenzyl)benzene, 0.7 wt% l,3,5-trimethyl-2,4-di(3,5-di-tert-butyl-4- hydroxybenzyl)benzene, and 0.02 wt% of 4,4'-methyienebis(2,6-di-tert-butylphenol).
Example 5: Preparation of l,3,5-trimethyl-2,4,6-tris(3,5-dMert-butyl-4- hydroxybenzyl) benzene from 2,6-di-tert-butylphenol
[0034] In a four-necked flask equipped with a stirrer, condenser, thermocouple, and an addition funned was placed paraformaldehyde (26.2 g of 95%), diethyl amine (6.2 g), and acetic acid (350). 2,6-di-tert-Butylphenol (132 g) was dissolved in acetic acid (150 g) and placed in the addition funnel. A portion of this solution (38%) was added to the stirred reaction mixture at room temperature and heated up to 1100C. After one hour another portion (31%) was added and refluxing was continued. After two hours at these conditions, the rest of the solution (31%) was added and refluxed for a total of eight hours. The reaction mixture was concentrated under reduced pressure and at 650C and the resulting paste was washed with water (3x150 g) at 95-1000C. Heptane (200 g) was added to the residue and dried by azeotropic distillation. Heptane was removed under vacuum at 7O0C. Crude product weighed 154 g with a purity of 83% by GC. This was re-dissolved in acetic acid (460 g) and mesitylene (18 g) was added and stirred at room temperature. Sulfuric acid (5 g, 98%) was added and heated at 400C for five hours. GC Analysis showed less than 2% unreacted starting material. The reaction slurry was added to water (700 g) and filtered. The crude solid was dissolved in heptane (500 g) and heated to 850C and the organic layer was washed with water (3x100 g) and dried by azeotropic distillation. The solvent was removed under reduced pressure and l,3,5-trimethyl-2,4,6-tris(3,5-di-tert-butyl-4-hydroxybenzyl)benzene was isolated as an off-white powder (95 g).
Example 6: Preparation of l,3,5-trimethyl"2,4,6-tris(3,5-di-terf.-butyl-4- hydroxy benzyl) benzene from 2,6-di-tert-butylphenol
[0035] In a four-necked flask equipped with a stirrer, condenser, thermocouple, and an addition funned was placed paraform aldehyde (20.5 g of 95%), diethyl amine (4.3 g), and acetic acid (250). 2,6-di-tert-Butylρhenol (112 g) was dissolved in acetic acid (200 g) and placed in the addition funnel. A portion of this solution (67%) was added to the stirred reaction mixture at room temperature and heated up to 1100C. After three hours the rest of solution was added and refluxing was continued for a total of six 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 5O0C for five hours. GC Analysis showed the presence of unreacted starting material. The reaction mixture was heated and held at 8O0C for one hour. The reaction slurry was cooled to 50C and filtered. The resulting pink powder was heated under vacuum (10-15 raraHg) and 750C for one hour. Analysis of the product (86 g) showed 96.1% of l,3,5-trimethyl-2,4,6-tris(3,5-di-tert-butyl-4~hydroxybenzyl)benzene and 1.9 wt% of 1,3,5- trimethy]-2,4-di(3,5-di-tert-butyl-4-hydroxybenzyl)benzene. Analysis of the filtrate showed 2.22 wt% l ,3,5-trimethyl-2,4-di(3,5-di-tert-butyl-4-hydroxybenzyl)benzene and 0.4 wt% of l,3,5-trimethyl-2,4,6-tris(3,5-di-tert-butyl-4-hydroxybenzyl)benzene along with other impurities.
[0036] It is to be understood that the reactants and components referred to by chemical name or formula anywhere in the specification or claims hereof, whether referred to in the singular or plural, are identified as they exist prior to being combined with or coming into contact with another substance referred to by chemical name or chemical type (e.g., another reactant, a solvent, or etc.). It matters not what chemical changes, trans formations and/or reactions, if any, take place in the resulting combination or solution or reaction medium as such changes, transformations and/or reactions are the natural result of bringing the specified reactants and/or components together under the conditions called for pursuant to this disclosure. Thus the 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. Thus the fact that a substance, component or ingredient may have lost its original identity through a chemical reaction or transformation during the course of contacting, combining, blending or mixing operations, if conducted in accordance with this disclosure and with the application of common sense and the ordinary skill of a chemist, is thus wholly immaterial for an accurate understanding and appreciation of the true meaning and substance of this disclosure and the claims thereof. As will be familiar to those skilled in the art, the terms "combined", "combining", and the like as used herein mean that the components that are "combined" or that one is "combining" are put into a container with each other. Likewise a "combination" of components means the components having been put together in a container.
[0037] While the present invention has been described in terms of one or more preferred embodiments, it is to be understood that other modifications may be made without departing from the scope of the invention, which is set forth in the claims below.

Claims

1. A process comprising:
combining in a container at least acetic acid, paraformaldehyde, a secondary amine, and 2,6-di-tert-butylphenol and refluxing at about 1000C to about 140°C for at least about 2 hours,
adding mesitylene and a catalytic amount of an acid catalyst to the container, and
yielding at least l,3,5-trimethyl-2,4,6-tris(3,5-dialkyl-4- hydroxybenzyl)benzene having a purity of at least about 98%.
2. A process comprising: combining at least 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 l,3,5-trimethyl-2,4,6-tris(3,5-dialkyl-4- hydroxybenzyl)bcnzene.
3. The process according to claim 2 wherein the paraformaldehyde is in excess as to the 2,6-di-tert-butylphenol.
4. The process according to claim 3 further comprising recovering unreacted paraformaldehyde.
5. A process comprising:
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,
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-butyl-4-acetoxymethylphenol solid or melt in at least 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-dialkyl-4- hydroxybenzyl)benzene.
6. A process comprising:
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,
isolating at least the 2,6-di-tert-butyl-4-acetoχymethylρhenol as a solid or a melt,
combining at least the 2,6-di-tert-butyl-4-acetoxymcthylphenol, mesitylene, and a catalytic amount of an acid catalyst, and
yielding at least a l,335-trimethyl-2,4,6-tris(3,5-dialkyl-4- hydroxybenzyl)benzene.
7. A process comprising: combining at least acetic acid, paraformaldehyde, a secondary amine, and 2,6- di-tert-butylphenol to yield a solution comprising at least 2,6-di-tcrt-butyI-4- acetoxymethylphenol,
acidifying the solution,
combining at least the 2,6-di-tert-butyl-4-acetoxymethylρhenol, mesitylene, and a catalytic amount of an acid catalyst, and
yielding at least a l,3,5-trimethyl-2,4,6-tris(3,5-dialkyl-4- hydroxybenzyl)benzene.
8. The process according to any of claims 1 - 7, wherein the secondary amine comprises dimethylamine, diethylamine, methylethyl amine, diisopropylamine, methylisoproplyamine, cthylisopropyl amine, dipropyl amine, methylproplyamine, ethylpropylamine, di-butylamine, methylbutylamine, ethylbutylamine, proplybutylamine, diphenylamine, phenylnaphthylamine, piperidine, or piperazine.
9. The process according to any of claims 1 - 7, wherein the secondary amine comprises dimethylamine or diethylamine.
10. The process according to any of claims 1 - 7, wherein the acid catalyst comprises an alkyl sulfonic acid, an aryl sulfonic acid, chloroacetic acid, trifluoroacetic acid, or sulfuric acid.
1 1. The process according to any of claims 1 - 7, wherein the acid catalyst comprises sulfuric acid.
12. The process according to any of claims 1 - 7, further comprising recovering unreacted acetic acid.
13. The process according to any of claims 1 - 7, further comprising recovering unreacted acetic acid and repeating the process using the recovered acetic acid.
14. The process according to any of claims 5 or 6, wherein isolating at least the 2,6-di-tert-butyl-4-acetoxymethylphenol as a solid or a melt,
is replaced with
isolating at least the 2,6-di-tert-butyl-4-acetoxymethylphenol as a solid or a melt and purifying the 2,6-di-tert-butyl-4-acetoxymethylphenol.
15. The process according to claim 14, wherein the purifying of the 2,6-di-tert- butyl-4-acetoxymethylphcnol comprises washing the 2,6-di-tert-butyl-4- acetoxymethylphcnol with water a plurality of times, crystallizing the 2,6-di-tcrt-butyl-4- acetoxymethylphenol from the acetic acid, precipitating the 2,6-di-tert-butyl-4- acetoxymethylphenol from a hydrocarbon solvent.
16. The process according to claim 14, wherein the purifying of the 2,6-di-tert- butyl-4-acetoxymethylphenol comprises crystallizing the 2,6-di-tert-butyl-4- acetoxymethylphenol from the acetic acid, and further comprising recovering the acetic acid and repeating the process using the recovered acetic acid with new batches of paraformaldehyde, secondary amine, and 2,6-di-tert-butylphenol.
17. The process according to any one of claims 2 - 7, further comprising recovering the acetic acid and repeating the process using the recovered acetic acid with new batches of paraformaldehyde, secondary amine, and 2,6-di-tcrt-butylphenol.
18. A process comprising combining at least 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 -acetoxymethylpheno 1.
19. A product comprising 2,6-di4ert-butyl-4-acetoxymethylphenol, 2,6-di-tert- butylphenol, 2,6-di-tert-butyl-4-hydroxymethylphenol, and 4,4'-methylenebis(2,6-di-tert- butylphenol).
PCT/US2010/041029 2009-07-10 2010-07-06 Green and atom-economical processes for producing phenolic antioxidants Ceased WO2011005735A1 (en)

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)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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

Patent Citations (5)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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

Similar Documents

Publication Publication Date Title
Hosseini-Sarvari TiO2 as a new and reusable catalyst for one-pot three-component syntheses of α-aminophosphonates in solvent-free conditions
US5166355A (en) Process for preparing substituted 2,2'-methylene-bis-[6-(2H-benzotriazol-2-yl)-4-hydrocarbyl-phenols]
US8766016B2 (en) Green and atom-economical processes for producing phenolic antioxidants
CN102712576A (en) Method for producing aromatic formamides
ME01849B (en) Process for the synthesis of strontium ranelate and its hydrates
Henry et al. 1, 3-and 1, 4-Dialkyl-5-iminotetrazoles
CN100506768C (en) 2,4-di-(1-phenylisopropyl) phenol preparation method
CN109942436B (en) A kind of method for preparing N,N-dialkylaniline compound by alkylation of p-toluenesulfonic acid alkyl ester
JPH1112258A (en) Production of 3-aryldihydro-1,3-benzoxazine compound
CN1091097C (en) Preparation method of N-substituted glycine or glycine ester
JP5693035B2 (en) Method for producing substituted 1,4-quinone methides
JP5266708B2 (en) Process for producing hydroxypentafluorosulfanylbenzene compounds
CN108047258B (en) Method for synthesizing aminopyridine borate
WO2020260418A1 (en) Methods for preparing benzoxazines
WO2020127386A1 (en) Methods for preparing intermediates
CN101508663A (en) Synthesis of meta-methylthio diphenylamine
EP1912961B1 (en) Process of producing bepromoline
CN101203474A (en) C-Alkylation Process for Hydroxylated Aromatic Compounds
CN101555218B (en) Synthetic method of azoxybenzene compound
CN101372476B (en) Catalyst-free and solvent-free method for synthesizing pyrazole heterocycles
CN110577520B (en) Preparation method of 6-nitro-4-substituted amino quinazoline derivative
JP4145082B2 (en) Substituted phenols
CN109970733B (en) Simple preparation method of vemurafenib and analogue thereof
JP2008308458A (en) Production method of pyridinecarbonyl compound
JPS60190729A (en) Production of trimethylol heptane

Legal Events

Date Code Title Description
WWE Wipo information: entry into national phase

Ref document number: 201080030923.1

Country of ref document: CN

121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 10731889

Country of ref document: EP

Kind code of ref document: A1

WWE Wipo information: entry into national phase

Ref document number: 10238/DELNP/2011

Country of ref document: IN

ENP Entry into the national phase

Ref document number: 20127000303

Country of ref document: KR

Kind code of ref document: A

WWE Wipo information: entry into national phase

Ref document number: 13382683

Country of ref document: US

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 10731889

Country of ref document: EP

Kind code of ref document: A1