GB246526A - Process of esterification - Google Patents

Process of esterification

Info

Publication number
GB246526A
GB246526A GB2300/26A GB230026A GB246526A GB 246526 A GB246526 A GB 246526A GB 2300/26 A GB2300/26 A GB 2300/26A GB 230026 A GB230026 A GB 230026A GB 246526 A GB246526 A GB 246526A
Authority
GB
United Kingdom
Prior art keywords
alcohol
butyl
still
water
layer
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
GB2300/26A
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.)
US Industrial Alcohol Co
Original Assignee
US Industrial Alcohol Co
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 US Industrial Alcohol Co filed Critical US Industrial Alcohol Co
Publication of GB246526A publication Critical patent/GB246526A/en
Expired legal-status Critical Current

Links

Classifications

    • 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

Landscapes

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

Abstract

246,526. U.S. Industrial Alcohol Co., (Assignees of Arentz, F. B.). Jan. 26, 1925, [Convention date]. Esters.-In a process of esterification, a reaction mixture containing the acid and alcohol is distilled so as to produce, a constant boiling mixture which is condensed to form separate liquid layers, one of which contains a high percentage of water and is removed from the apparatus, while the entire layer containing the other constituents is returned to the renuxing column of the reaction vessel until no more water is evolved. The process is described for the preparation of normal butyl acetate, but may be used for the production of other esters, such as isobutyl acatate, amyl acetate, normal butyl tartrate, amyl phthalate, butyl phthalate, ,and amyl formate. In the preparation of butyl acetate, a mixture of butyl alcohol and concentrated or glacial acetic acid is heated with a small quantity of sulphuric acid as a catalyst in a still 1 surrounded by a heating jacket 2. The still is connected to a column 5, and dephlegmator 9, the condensates from which return to the still through pipes 7 and 12. After a substantial amount of ester has been formed, the mixture is slowly distilled, and the vapours are condensed in a condenser 14. The condensate passes to a separating chamber 18 fitted with a sight-glass 20, and separates into two layers 21, 22. The upper layer 21 consists mainly of butyl acetate and butyl alcohol and is returned to the column 5 through a pipe 23. The lower layer consists mainly of water and is removed by a pipe 24. When no more water separates out in the chamber 18, the contents of the still are neutralized with caustic soda and then rectified or otherwise treated to recover the ester. In making butyl tartrate, the vapours driven off from the still consist mainly of butyl alcohol and water, and separate into an upper alcohol layer, which is returned to the still, and a lower water layer. When the reaction is completed, the excess alcohol is removed by the vacuum distillation, and the crude ester is washed and rectified.
GB2300/26A 1925-01-26 1926-01-26 Process of esterification Expired GB246526A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US246526XA 1925-01-26 1925-01-26

Publications (1)

Publication Number Publication Date
GB246526A true GB246526A (en) 1927-04-26

Family

ID=21821701

Family Applications (1)

Application Number Title Priority Date Filing Date
GB2300/26A Expired GB246526A (en) 1925-01-26 1926-01-26 Process of esterification

Country Status (1)

Country Link
GB (1) GB246526A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE878348C (en) * 1942-11-21 1953-06-01 Basf Ag Process for the continuous production of carboxylic acid esters
WO1995017937A1 (en) * 1993-12-24 1995-07-06 Henkel Kommanditgesellschaft Auf Aktien Method of working up a reaction mixture by means of a column placed on the reaction vessel
US10337701B2 (en) 2014-05-21 2019-07-02 Signify Holding B.V. Decorative LED integrated luminaire
CN111408330A (en) * 2020-04-23 2020-07-14 山东润泽能源科技有限公司 Ester exchange equipment and method for producing DOTP (dioctyl phthalate) by PET (polyethylene terephthalate)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE878348C (en) * 1942-11-21 1953-06-01 Basf Ag Process for the continuous production of carboxylic acid esters
WO1995017937A1 (en) * 1993-12-24 1995-07-06 Henkel Kommanditgesellschaft Auf Aktien Method of working up a reaction mixture by means of a column placed on the reaction vessel
US10337701B2 (en) 2014-05-21 2019-07-02 Signify Holding B.V. Decorative LED integrated luminaire
CN111408330A (en) * 2020-04-23 2020-07-14 山东润泽能源科技有限公司 Ester exchange equipment and method for producing DOTP (dioctyl phthalate) by PET (polyethylene terephthalate)

Similar Documents

Publication Publication Date Title
GB246526A (en) Process of esterification
US2173124A (en) Manufacture of organic esters of higher alcohols and lower aliphatic acids
US1847597A (en) Treatment of crude pyroligneous acid
US1915002A (en) Process of obtaining fatty acids in anhydrous state from aqueous solutions
US2155625A (en) Production of organic esters
US2454734A (en) Distillation of acetone, ethanol, and butanol from aqueous solutions thereof
US2650249A (en) Process for treating methyl acetate
US1668380A (en) Continuous process for the dehydration of volatile fatty acids
US2290926A (en) Preparation of lactic acid
GB234458A (en) Improvements in the method for the continuous manufacture of esters of the fatty or the aromatic series
GB298137A (en) Improved process for concentrating acetic acid
US1733720A (en) Manufacture of alcohol
US1782963A (en) Manufacture of solvents
GB301523A (en) Improvements in the production of esters
US1931687A (en) Manufacture of aliphatic
US1696432A (en) Pbockess of cowcentbatihg-iowee
US1872029A (en) Manufacture of aliphatic anhydrides
US1884626A (en) Manufacture of aliphatic acid anhydrides
US1908508A (en) Process of dehydrating aqueous acetic acid with trichlorethylene
US2176655A (en) Continuous method of cracking hydrocarbon oil
GB301415A (en) Improvements in continuous process for the manufacture of acetic acid in the anhydrous state, from its aqueous solutions
US2143474A (en) Treatment of residual oils
GB418943A (en) Improvements in or relating to processes of making vinyl esters
US1836287A (en) Process for obtaining bornyl and isobornyl esters
US1663817A (en) Process for the manufacture of farnesol