US3923848A - Process for preparing high molecular weight aliphatic carboxylic acids by chromosulfuric acid oxidation of {60 -olefins - Google Patents

Process for preparing high molecular weight aliphatic carboxylic acids by chromosulfuric acid oxidation of {60 -olefins Download PDF

Info

Publication number
US3923848A
US3923848A US498567A US49856774A US3923848A US 3923848 A US3923848 A US 3923848A US 498567 A US498567 A US 498567A US 49856774 A US49856774 A US 49856774A US 3923848 A US3923848 A US 3923848A
Authority
US
United States
Prior art keywords
olefins
oxidation
chromosulfuric acid
molecular weight
carbon atoms
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 - Lifetime
Application number
US498567A
Other languages
English (en)
Inventor
Hans Schmidt
Werner Strabberger
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.)
Hoechst AG
Original Assignee
Hoechst AG
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 claimed from DE19732342823 external-priority patent/DE2342823C3/de
Application filed by Hoechst AG filed Critical Hoechst AG
Application granted granted Critical
Publication of US3923848A publication Critical patent/US3923848A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/16Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation

Definitions

  • the present invention provides a process for preparing saturated, high molecular weight, aliphatic monocarboxylic acids by oxidizing a-olefms having from 16 to 70 carbon atoms in the molecule or mixtures of such a-olefins in the molten state by means of aqueous chromosulfuric acid, which comprises adding to the molten olefins or mixtures of olefins prior to oxidizing of from 2 to 15% by weight, calculated on the olefins, of aliphatic monoor dialcohols having from to 40 carbon atoms in the molecule-optionally in the form of their fatty acid esters and then oxidizing with aqueous chromosulfuric acid.
  • the proportion of neutral matter in the oxidation products may be reduced by 10 to 50% or even more.
  • Suitable starting materials for the chromosulfuric acid oxidation according to the invention are for example a-olefins having more than carbon atoms in the molecule, for example l-hexadecene, l-octadecene and l-eicosene or a-olefins having up to about 70 carbon atoms, which may be prepared by oligomerizing ethylene. Commercial mixtures of a-olefins having from 22 to 28 or from 24 to 48 carbon atoms are preferably used.
  • aliphatic alcohols are saturated monoalcohols having from 10 to 40 carbon atoms, preferably straight chain primary alcohols, as for example decyl alcohol, dodecyl alcohol, tetradecyl alcohol, cctyl alcohol and especially stearyl alcohol and behenyl alcohol, moreover glycoland polyglycol monoalkyl ethers having higher alkyl groups, such as the etheralcohol glycol-monostearyl ether.
  • Synthetic monoalcohols for example those, prepared according to the known polyethylene synthesis with Ziegler catalysts followed by oxidative hydrolysis of the aluminium trialkyls are also suitable.
  • Aliphatic dialcohols having from 10 to 40 carbon atoms for example a,w-diols, such as l, l0-decane-diol or 1,19mondecane-diol, and optionally polyalkylene glycols are also suitable; it should be taken into consideration however that dicarboxylic acids are generally formed in the oxidation of diols, so that the use of diols is not recommended, if the acids resulting from the oxidation shall be free from dicarboxylic acids.
  • Esters of higher monoalcohols or diols with fatty acids having 2,3 or from 16 to 40 carbon atoms for example stearyl acetate, stearyl stearate and esters of the montanic acid are also suitable. They are first saponified under the oxidation conditions, so that their efficiency finally is based on the presence of the basic alcohols.
  • the aliphatic monoalcohols or diols are added to the molten a-olefin or a-olefin mixture to be oxidized in an amount of from 2 to 15, preferably of from 4 to 10 by weight, calculated on the olefins.
  • the oxidation is carried out in known manner.
  • Chromosulfuric acid containing per liter from 50 to 140 g of CrO preferably from to 120 g and from 300 to 650 g, preferably from 400 to 550 g of H 80 is used as oxidizing agent.
  • the oxidation temperature is in the range of from 60 to 180C, preferably of from to 120C.
  • the quantity of oxidizing agent required is from to 250 preferably from to 200 of CrO calculated on the weight of the olefin-alcohol mixture to be oxidized.
  • the oxidation is preferably carried out as follows:
  • the molten olefin-alcohol mixture is introduced into the chromosulfuric acid heated to the desired oxidation temperature by small amounts or continuously and the mixture is vigorously stirred during the whole reaction. It is also possible to add the oxidizing agent to the molten mass of the product to be oxidized. According to a preferred method the reaction is carried out in a multiple-stage process, while separating the depleted oxidant after each step.
  • the oxidation times are generally in the range of from 4 to 8 hours.
  • the high molecular weight, aliphatic carboxylic acids or carboxylic acid mixtures obtained having a relatively low content of neural matter are colourless and thermostable and are especially suitable for preparing waxlike esters, partial esters and amides, which may be used as lubricants in the plastics processing and in the preparation of floor waxes and polishing pastes.
  • synthelic alcohol according to Ziegler, having 24 carbon atoms "aarnonadecane diol molecule, or their fatty acid esters, and then oxidizing with the aqueous chromosulfuric acid at a temperature of 60 to 180C.
  • aqueous chromosulfuric acid used is a chromosulfuric acid containing per liter of from 50 to g of CrO and from 300 to 650 g of H 50

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
US498567A 1973-08-24 1974-08-19 Process for preparing high molecular weight aliphatic carboxylic acids by chromosulfuric acid oxidation of {60 -olefins Expired - Lifetime US3923848A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE19732342823 DE2342823C3 (de) 1973-08-24 Verfahren zur Herstellung höhermolekularer, aliphatischer Monocarbonsäuren

Publications (1)

Publication Number Publication Date
US3923848A true US3923848A (en) 1975-12-02

Family

ID=5890635

Family Applications (1)

Application Number Title Priority Date Filing Date
US498567A Expired - Lifetime US3923848A (en) 1973-08-24 1974-08-19 Process for preparing high molecular weight aliphatic carboxylic acids by chromosulfuric acid oxidation of {60 -olefins

Country Status (7)

Country Link
US (1) US3923848A (fr)
JP (1) JPS5076017A (fr)
BE (1) BE819199A (fr)
CA (1) CA1028354A (fr)
FR (1) FR2241527B1 (fr)
GB (1) GB1452571A (fr)
NL (1) NL7411058A (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4029682A (en) * 1974-12-23 1977-06-14 Emery Industries, Inc. Soaps and ester-soaps of α-olefin derived high molecular weight acids

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102013007638B4 (de) * 2013-05-06 2019-04-25 Kahl GmbH & Co. KG Verfahren zur Herstellung eines Säurewachses

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2450858A (en) * 1944-01-20 1948-10-05 J D Fitzpatrick Method of oxidizing unsaturated fatty bodies
US2470515A (en) * 1946-07-05 1949-05-17 Emery Industries Inc Plasticized prolamines
US2644837A (en) * 1951-04-27 1953-07-07 Du Pont Oxidation of olefinic compounds
US3692810A (en) * 1971-02-22 1972-09-19 Continental Oil Co Catalytic oxidation of olefins to yield carboxylic acids

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2450858A (en) * 1944-01-20 1948-10-05 J D Fitzpatrick Method of oxidizing unsaturated fatty bodies
US2470515A (en) * 1946-07-05 1949-05-17 Emery Industries Inc Plasticized prolamines
US2644837A (en) * 1951-04-27 1953-07-07 Du Pont Oxidation of olefinic compounds
US3692810A (en) * 1971-02-22 1972-09-19 Continental Oil Co Catalytic oxidation of olefins to yield carboxylic acids

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4029682A (en) * 1974-12-23 1977-06-14 Emery Industries, Inc. Soaps and ester-soaps of α-olefin derived high molecular weight acids

Also Published As

Publication number Publication date
DE2342823B2 (de) 1976-01-15
JPS5076017A (fr) 1975-06-21
GB1452571A (en) 1976-10-13
CA1028354A (fr) 1978-03-21
FR2241527A1 (fr) 1975-03-21
FR2241527B1 (fr) 1979-01-05
DE2342823A1 (de) 1975-03-20
NL7411058A (nl) 1975-02-26
BE819199A (fr) 1975-02-26

Similar Documents

Publication Publication Date Title
US3756999A (en) Sprocess for the preparation of oxidation products of ethylene polymer
EP0010809B1 (fr) Composition de cire pouvant remplacer entièrement ou partiellement la cire de carnauba ou la cire montan
DE69213435T2 (de) Herstellung von alkoholen
US2182617A (en) Polymerization of olefins
US3923848A (en) Process for preparing high molecular weight aliphatic carboxylic acids by chromosulfuric acid oxidation of {60 -olefins
US3899476A (en) Process for making a methacrylic acid adduct of linoleic acid and product
US2766267A (en) Organic acids from oxygen-bearing organic compounds
US3576881A (en) Preparation of modified oxo catalyst and process relating thereto
US2962513A (en) Manufacture of organoaluminum compounds
US3950365A (en) Method for purification of fatty acid mixtures
JPS6225682B2 (fr)
EP0505807B1 (fr) Procédé d'épuration d'oléfines
US3542857A (en) Production of vic-glycol esters
US2360393A (en) Alcoholysis catalysts
US3005846A (en) Production of acids and esters
US3299110A (en) Condensation of carboxylic acids and olefins to produce esters
US3816489A (en) Increasing the selectivity and yield in the production of carboxylic acids
CA1066832A (fr) Produit de l'oxydation mixte de cires vegetales et autres
US3104271A (en) Olefin dimerization
DE4422777A1 (de) Verfahren für die Herstellung von Adipinsäure oder Pentensäure
US2628938A (en) Production of greases using reaction products of alpha-hydroxy fatty acids
US3053883A (en) Use of metal salts to promote esterification
US3974194A (en) Method of separating cobalt catalyst from a liquid polyol ester product
EP0445859B1 (fr) Procédé pour la préparation du sec-butylacrylate
US3185745A (en) Olefin dimerization