GB693390A - Process for preparing branched chain primary sulfate esters - Google Patents
Process for preparing branched chain primary sulfate estersInfo
- Publication number
- GB693390A GB693390A GB1397/51A GB139751A GB693390A GB 693390 A GB693390 A GB 693390A GB 1397/51 A GB1397/51 A GB 1397/51A GB 139751 A GB139751 A GB 139751A GB 693390 A GB693390 A GB 693390A
- Authority
- GB
- United Kingdom
- Prior art keywords
- tertiary
- ethylene
- primary
- diluent
- branched chain
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C17/00—Preparation of halogenated hydrocarbons
- C07C17/093—Preparation of halogenated hydrocarbons by replacement by halogens
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C303/00—Preparation of esters or amides of sulfuric acids; Preparation of sulfonic acids or of their esters, halides, anhydrides or amides
- C07C303/24—Preparation of esters or amides of sulfuric acids; Preparation of sulfonic acids or of their esters, halides, anhydrides or amides of esters of sulfuric acids
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Branched chain primary alkyl sulphates are obtained by reacting ethylene with a tertiary olefin in the presence of 80-100 weight per cent sulphuric acid at a temperature of -25 DEG C. to +80 DEG C. and at an ethylene partial pressure of 50-1000 p.s.i.g. The tertiary olefin may be aliphatic or alicyclic and may range from C4 to C30 or higher. The molar ratio of ethylene to tertiary olefine should preferably be greater than 50 : 1 but lower ratios may be employed when a tertiary olefine such as tetraisobutylene where the rate of self polymerization is negligible is employed. The reaction is preferably effected by adding the tertiary olefin to thn reactor containing the sulphuric acid and ethylene under the desired pressure and an inert hydrocarbon diluent is preferably employed. The diluent may be a saturated aliphatic or alicyclic hydrocarbon preferably a normal or iso-paraffin and when a branched chain hydrocarbon is employed as diluent it should preferably have the same carbon skeleton structure as the tertiary olefine. In a continuous type operation the tertiary olefine may be fed at the bottom of a reactor containing the sulphuric acid intermixed with the inert diluent and continuously withdrawing the tertiary olefine-free diluent from the top of the reactor. The primary sulphates produced by the process may be hydrolysed with water to give branched chain primary alcohols. Examples are given in which (1) isobutylene is reacted with ethylene using 95.5 weight per cent sulphuric acid at -15 DEG C. using n-heptane as p diluent to yield a primary sulphate ester which on hydrolysis with water yields 3,3-dimethyl-butanol-1; (2) a mixture of 2-methyl pentene-2 and 2-methylpentene-1 is similarly reacted with ethylene to give 3,3-dimethyl-hexanol-1; (3) a mixture of hexenes in which the ratio of tertiary/secondary olefins is about 3.5 : 1 yields hexyl ethanols, and (4) 1-methylcyclopentene yields a 2-alkylated ethanol in which the branching is an alicyclic radical. A Table is also given in which the production of various alkylated ethanols from the corresponding tertiary olefine and ethylene using 95-96 per cent sulphuric acid is described. The primary sulphate esters may be reacted with hydrogen halides such as HI, HBr2, HCl, HF to yield the corresponding halide, the reaction being effected by treating the primary sulphate ester with anhydrous hydrogen halide at 0 DEG to 100 DEG C. and preferably at 25 DEG to 50 DEG C. The primary sulphate esters also react with ammonia to form primary amines and on alcoholysis form other esters and mixed neutral sulphates whilst on heating the acid sulphate esters decompose to form alpha olefines. It is stated that the acetate derived from 3,3-dimethylbutanol and glacial acetic acid is useful as a lacquer solvent and that the di-octyl phthalate ester derived from phthalic anhydride and the branched chain alcohol of the invention can be employed as a plasticizer for polyvinyl chloride-type plastics.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US693390XA | 1950-04-27 | 1950-04-27 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB693390A true GB693390A (en) | 1953-07-01 |
Family
ID=22088299
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1397/51A Expired GB693390A (en) | 1950-04-27 | 1951-01-18 | Process for preparing branched chain primary sulfate esters |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB693390A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5977415A (en) * | 1998-08-20 | 1999-11-02 | The Nutrasweet Company | Preparation of 3, 3-dimethylbutyraldehyde from a tert-butyl cation precursor, vinyl chloride and an acidic catalyst |
WO2001002332A2 (en) * | 1999-07-02 | 2001-01-11 | The Nutrasweet Company | Process for the preparation of 3,3-dimethylbutanal |
-
1951
- 1951-01-18 GB GB1397/51A patent/GB693390A/en not_active Expired
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5977415A (en) * | 1998-08-20 | 1999-11-02 | The Nutrasweet Company | Preparation of 3, 3-dimethylbutyraldehyde from a tert-butyl cation precursor, vinyl chloride and an acidic catalyst |
WO2001002332A2 (en) * | 1999-07-02 | 2001-01-11 | The Nutrasweet Company | Process for the preparation of 3,3-dimethylbutanal |
WO2001002332A3 (en) * | 1999-07-02 | 2001-03-22 | Nutrasweet Co | Process for the preparation of 3,3-dimethylbutanal |
JP2003503471A (en) * | 1999-07-02 | 2003-01-28 | ザ・ニュートラスウィート・カンパニー | Method for producing 3,3-dimethylbutanol |
US6573409B1 (en) | 1999-07-02 | 2003-06-03 | The Nutrasweet Company | Process for the preparation of 3,3-dimethylbutanal |
US6803487B2 (en) | 1999-07-02 | 2004-10-12 | The Nutrasweet Company | Process for the preparation of 3,3-dimethylbutanal |
US7164049B2 (en) | 1999-07-02 | 2007-01-16 | The Nutrasweet Company | Process for the preparation of 3,3-dimethylbutanal |
US7348459B2 (en) | 1999-07-02 | 2008-03-25 | The Nutrasweet Company | Process for the preparation of 3,3-dimethylbutanal |
JP2011137026A (en) * | 1999-07-02 | 2011-07-14 | Nutrasweet Property Holdings Inc | Production method for 3,3-dimethylbutanal |
CN102249851A (en) * | 1999-07-02 | 2011-11-23 | 纳特拉斯维特公司 | Process for the preparation of 3,3-dimethylbutanal |
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