GB641250A - Process for the manufacture of di-isopropyl-benzene hydro-peroxides and products resulting therefrom - Google Patents

Process for the manufacture of di-isopropyl-benzene hydro-peroxides and products resulting therefrom

Info

Publication number
GB641250A
GB641250A GB1711847A GB1711847A GB641250A GB 641250 A GB641250 A GB 641250A GB 1711847 A GB1711847 A GB 1711847A GB 1711847 A GB1711847 A GB 1711847A GB 641250 A GB641250 A GB 641250A
Authority
GB
United Kingdom
Prior art keywords
hydroperoxides
benzene
hydroperoxide
mono
aqueous
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.)
Expired
Application number
GB1711847A
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.)
Distillers Co Yeast Ltd
Distillers Co Ltd
Original Assignee
Distillers Co Yeast Ltd
Distillers Co Ltd
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
Priority to BE498321D priority Critical patent/BE498321A/xx
Application filed by Distillers Co Yeast Ltd, Distillers Co Ltd filed Critical Distillers Co Yeast Ltd
Priority to GB1711847A priority patent/GB641250A/en
Priority to FR968209D priority patent/FR968209A/en
Publication of GB641250A publication Critical patent/GB641250A/en
Expired 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
    • C07C37/08Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring by decomposition of hydroperoxides, e.g. cumene hydroperoxide
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/132Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C407/00Preparation of peroxy compounds
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C407/00Preparation of peroxy compounds
    • C07C407/003Separation; Purification; Stabilisation; Use of additives
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C409/00Peroxy compounds
    • C07C409/02Peroxy compounds the —O—O— group being bound between a carbon atom, not further substituted by oxygen atoms, and hydrogen, i.e. hydroperoxides
    • C07C409/04Peroxy compounds the —O—O— group being bound between a carbon atom, not further substituted by oxygen atoms, and hydrogen, i.e. hydroperoxides the carbon atom being acyclic
    • C07C409/08Compounds containing six-membered aromatic rings
    • C07C409/12Compounds containing six-membered aromatic rings with two alpha,alpha-dialkylmethyl hydroperoxy groups bound to carbon atoms of the same six-membered aromatic ring
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C45/00Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
    • C07C45/51Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by pyrolysis, rearrangement or decomposition
    • C07C45/53Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by pyrolysis, rearrangement or decomposition of hydroperoxides

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

Di-isopropyl-benzene is emulsified in an aqueous solution and the resulting dispersion brought into intimate contact with molecular oxygen at an elevated temperature, whereby the mono- and di-hydroperoxides are formed. The reaction occurs most readily with p-di-isopropyl-benzene, less easily with the m-isomer and not at all or only very slightly with the o-isomer. The commercially available material (obtained as a by-product in the condensation of propylene and benzene) consists of a mixture of all three isomers, from which the p-form can be separated by fractionation. The p-form may be used to prepare the p-hydroperoxides, and the residual mixture of o- and m-forms to give the m-hydroperoxides. Alternatively, the commercial product may be treated directly, when a mixture of m- and p-hydroperoxides is obtained. It is preferred to hydrogenate the commercial product over Raney nickel to remove unsaturated compounds. The aqueous dispersion is preferably made with the aid of emulsifying agents such as alkali stearates, ricinoleates or lauryl sulphates as in Specification 610,293, and is free from heavy metal compounds or other substances which catalyse the decomposition of peroxides. The pH is preferably between 7.5 and 10.5. The oxygen may be pure, or a mixture rich in oxygen or air may be used. The reaction temperature is preferably between 60 DEG C. and the boiling point of the liquid, preferably 80-95 DEG C., and the pressure may be atmospheric or higher. The introduction of oxygen is continued until the peroxides start to decompose, this point being determined by analysis of the mixture. Absorption of oxygen may be promoted by peroxides previously formed in the liquid or added thereto, or by the addition of benzene diazoacetate or lead tetra-acetate which liberate free radicals at the reaction temperature. The process may be continuous or batch. Two methods are available for the separation of the products: (1) the emulsion is allowed to break and is separated while hot into aqueous and oily layers, the former containing some peroxides and being returned for re-use. The p-di-hydroperoxide crystallizes from the oily layer on cooling and is purified by washing with benzene; residual amounts in the liquid are precipitated by adding benzene. The oily layer may be distilled under reduced pressure (before or after crystallization of the p-di-hydroperoxide) to remove unchanged hydrocarbons, and if the distillation is carried to completion some mono-hydroperoxides are found in the distillate. The residue is cooled or diluted with benzene to precipitate any p-di-hydroperoxide, leaving the mono-hydroperoxides and the m-di-hydroperoxide in the liquid fraction. Method (2) may be applied to the product of method (1) or to the initial emulsion, and depends on the relative solubilities of the peroxides in aqueous sodium hydroxide. The mixture is treated with 10 per cent sodium hydroxide and the aqueous and oily layers separated. The former is brought to a pH around 7 (e.g. 6.5-8), preferably by bubbling in carbon dioxide, and the precipitate filtered off and washed with benzene, giving the p-di-hydroperoxide. The benzene is distilled from the washings to give the m-di-hydroperoxide. The oily layer insoluble in 10 per cent sodium hydroxide is treated with 40-50 per cent sodium hydroxide, when the sodium salt of the p-mono-hydroperoxide is precipitated; this can be hydrolysed to the free peroxide by warming with water. The solution from the 40-50 per cent alkali is separated into aqueous and oily layers, the former being rejected. The latter is distilled in vacuo to remove hydrocarbons leaving the m-mono-hydroperoxide. Examples are given. Phenols are obtained by treating the hydroperoxides with mineral acids. Thus the p-mono-hydroperoxide gives p-isopropyl-phenol, and the di-hydroperoxides yield resorcinol and hydroquinone respectively. Ketones result from the treatment of the hydroperoxides with aqueous ferrous sulphate, the mono-hydroperoxides giving isopropylacetophenones and the di-hydroperoxides diacetyl benzenes. Acetone is a by-product in the conversion into phenols as above. Carbinols which are mono- and di-(b -hydroxyisopropyl)-benzenes are obtained by reduction of the hydroperoxides with aqueous sodium sulphite. On dehydration with alkali bisulphates they yield (a -methyl-vinyl)-benzenes. Specification 626,095 also is referred to.
GB1711847A 1947-06-28 1947-06-28 Process for the manufacture of di-isopropyl-benzene hydro-peroxides and products resulting therefrom Expired GB641250A (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
BE498321D BE498321A (en) 1947-06-28
GB1711847A GB641250A (en) 1947-06-28 1947-06-28 Process for the manufacture of di-isopropyl-benzene hydro-peroxides and products resulting therefrom
FR968209D FR968209A (en) 1947-06-28 1948-06-25 Peroxide compounds

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB1711847A GB641250A (en) 1947-06-28 1947-06-28 Process for the manufacture of di-isopropyl-benzene hydro-peroxides and products resulting therefrom

Publications (1)

Publication Number Publication Date
GB641250A true GB641250A (en) 1950-08-09

Family

ID=10089580

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1711847A Expired GB641250A (en) 1947-06-28 1947-06-28 Process for the manufacture of di-isopropyl-benzene hydro-peroxides and products resulting therefrom

Country Status (3)

Country Link
BE (1) BE498321A (en)
FR (1) FR968209A (en)
GB (1) GB641250A (en)

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2785205A (en) * 1954-07-01 1957-03-12 Hercules Powder Co Ltd Recovery of phenols
US2820832A (en) * 1954-06-18 1958-01-21 Ici Ltd Production of hydroperoxides
DE969266C (en) * 1951-04-28 1958-05-14 Rhone Poulenc Sa Process for the production of cumene hydroperoxide by the catalytic oxidation of cumene
US2862857A (en) * 1954-07-01 1958-12-02 Hercules Powder Co Ltd Azeotropic distillation of monohydric and dihydric phenols
US2911391A (en) * 1952-12-31 1959-11-03 Hercules Powder Co Ltd Polymer hydroperoxides
US2915557A (en) * 1956-06-05 1959-12-01 Shell Dev Process for recovering di-isopropylbenzene-di-hydroperoxide from di-isopropylbenzene oxidation products
US2950320A (en) * 1953-05-27 1960-08-23 Hercules Powder Co Ltd 5-benzoyl pentanol-1
DE1247313B (en) * 1959-06-24 1967-08-17 Hibernia Ag Process for the production of diisopropylbenzene dihydroperoxides
US3993696A (en) * 1973-05-02 1976-11-23 Sumitomo Chemical Company, Limited Method for recovering hydroperoxide
EP0084417A1 (en) * 1982-01-07 1983-07-27 Sumitomo Chemical Company, Limited Production of aromatic carbonyl compounds including novel acetophenones
EP0012613B1 (en) * 1978-12-14 1984-08-08 Mobil Oil Corporation A process for producing 3-alkylphenols and 1,3-dihydroxybenzene
US4929771A (en) * 1987-12-09 1990-05-29 Ciba-Geigy Corporation Process for the preparation of alkyl-substituted phenols or naphthols
EP0796833A2 (en) * 1996-03-20 1997-09-24 Rütgers Kureha Solvents GmbH Process for the preparation of hydroxyaromatics
CN113135819A (en) * 2021-04-29 2021-07-20 北京工业大学 Method for improving yield of resorcinol prepared by m-diisopropylbenzene oxidation

Families Citing this family (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE947309C (en) * 1952-06-19 1956-08-16 Rhone Poulenc Sa Process for the production of hydroquinone
DE947308C (en) * 1952-06-19 1956-08-16 Rhone Poulenc Sa Process for the production of hydroquinone
DE961168C (en) * 1952-08-23 1957-04-04 Distillers Co Yeast Ltd Process for the preparation of m- and p-diisopropylbenzene dihydroperoxides
US2736753A (en) * 1952-09-10 1956-02-28 Hercules Powder Co Ltd Recovery of phenols
US2790010A (en) * 1952-12-18 1957-04-23 Hooker Electrochemical Co Synthesis of meta-substituted phenols
US2784238A (en) * 1953-02-21 1957-03-05 Hercules Powder Co Ltd Catalyst reactivation in process for production of resorcinols
DE1084731B (en) * 1953-06-13 1960-07-07 Distillers Co Yeast Ltd Process for the production of resorcinol
US2820064A (en) * 1953-06-24 1958-01-14 Eastman Kodak Co Autoxidation of hydrocarbons
US2856432A (en) * 1953-09-04 1958-10-14 Hercules Powder Co Ltd Aromatic dihydroperoxide production
US2856433A (en) * 1953-09-05 1958-10-14 Hercules Powder Co Ltd Separation of organic compounds
DE961708C (en) * 1953-09-05 1957-04-11 Distillers Co Yeast Ltd Process for the production of dihydroperoxides from the mixtures obtained in the oxidation of substituted aromatic hydrocarbons
US2812357A (en) * 1954-01-12 1957-11-05 Hercules Powder Co Ltd Removal of hydroperoxide carbinols from aromatic hydroperoxides
US2805258A (en) * 1955-05-23 1957-09-03 Koppers Co Inc Process for the preparation of hydroperoxides from diisopropylbenzenes
DE1643971C3 (en) * 1967-07-13 1975-04-10 Bayer Ag, 5090 Leverkusen m- and p-isopropenylphenyl-dimethylcarbinol and processes for their preparation

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE969266C (en) * 1951-04-28 1958-05-14 Rhone Poulenc Sa Process for the production of cumene hydroperoxide by the catalytic oxidation of cumene
US2911391A (en) * 1952-12-31 1959-11-03 Hercules Powder Co Ltd Polymer hydroperoxides
US2950320A (en) * 1953-05-27 1960-08-23 Hercules Powder Co Ltd 5-benzoyl pentanol-1
US2820832A (en) * 1954-06-18 1958-01-21 Ici Ltd Production of hydroperoxides
US2785205A (en) * 1954-07-01 1957-03-12 Hercules Powder Co Ltd Recovery of phenols
US2862857A (en) * 1954-07-01 1958-12-02 Hercules Powder Co Ltd Azeotropic distillation of monohydric and dihydric phenols
US2915557A (en) * 1956-06-05 1959-12-01 Shell Dev Process for recovering di-isopropylbenzene-di-hydroperoxide from di-isopropylbenzene oxidation products
DE1247313B (en) * 1959-06-24 1967-08-17 Hibernia Ag Process for the production of diisopropylbenzene dihydroperoxides
US3993696A (en) * 1973-05-02 1976-11-23 Sumitomo Chemical Company, Limited Method for recovering hydroperoxide
EP0012613B1 (en) * 1978-12-14 1984-08-08 Mobil Oil Corporation A process for producing 3-alkylphenols and 1,3-dihydroxybenzene
EP0084417A1 (en) * 1982-01-07 1983-07-27 Sumitomo Chemical Company, Limited Production of aromatic carbonyl compounds including novel acetophenones
US4929771A (en) * 1987-12-09 1990-05-29 Ciba-Geigy Corporation Process for the preparation of alkyl-substituted phenols or naphthols
EP0796833A2 (en) * 1996-03-20 1997-09-24 Rütgers Kureha Solvents GmbH Process for the preparation of hydroxyaromatics
EP0796833A3 (en) * 1996-03-20 1998-04-01 Rütgers Kureha Solvents GmbH Process for the preparation of hydroxyaromatics
US6107527A (en) * 1996-03-20 2000-08-22 Rutgers Kureha Solvents Gmbh Process for the production of hydroxy-aromatic substances
CN113135819A (en) * 2021-04-29 2021-07-20 北京工业大学 Method for improving yield of resorcinol prepared by m-diisopropylbenzene oxidation

Also Published As

Publication number Publication date
BE498321A (en)
FR968209A (en) 1950-11-22

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