GB731438A - Improvements in or relating to manufacture of amyl nitrate - Google Patents
Improvements in or relating to manufacture of amyl nitrateInfo
- Publication number
- GB731438A GB731438A GB1675152A GB1675152A GB731438A GB 731438 A GB731438 A GB 731438A GB 1675152 A GB1675152 A GB 1675152A GB 1675152 A GB1675152 A GB 1675152A GB 731438 A GB731438 A GB 731438A
- Authority
- GB
- United Kingdom
- Prior art keywords
- per cent
- weight
- mixture
- alcohols
- acid
- 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
- C07C203/00—Esters of nitric or nitrous acid
- C07C203/02—Esters of nitric acid
- C07C203/04—Esters of nitric acid having nitrate groups bound to acyclic carbon atoms
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C201/00—Preparation of esters of nitric or nitrous acid or of compounds containing nitro or nitroso groups bound to a carbon skeleton
- C07C201/02—Preparation of esters of nitric acid
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
A process for the nitration of amyl alcohols consisting essentially of between 80 to 100 per cent by weight of isomeric primary alcohols, of not more than 20 weight per cent isomeric secondary amyl alcohols and not more than 1 weight per cent tertiary amyl alcohol comprises reacting said amyl alcohols directly with a nitration mixture consisting essentially of nitric and sulphuric acids, the nitric acid in said mixture being at least 20 per cent by weight and the water in said mixture being not more than 14 per cent by weight, the amount of nitric acid in said mixture being at least equal to and not more than 13 per cent in excess of the stoichiometric requirement to substantially completely esterify said amyl alcohols, and the ratio by weight of water to sulphuric acid in the final esterification mixture being not more than 0.35. The process may be carried out batchwise or continuously. The reaction product is allowed to separate into two phases in a settling chamber or continuous centrifugation, and solvent extraction or distillation may be employed. The product is preferably washed with soda and percolated through a tower containing a solid adsorbent such as "Filtrol" (Registered Trade Mark) or silica gel. In examples a mixture consisting mainly of primary amyl alcohols with small amounts of secondary alcohols, diamyl ether and water and mixtures consisting of nitric acid, sulphuric acid and water are introduced into an agitated body of reaction liquid in a stainless steel vessel with an overflow leading to a series of separators, the second equipped with a line for the addition of soda ash solution. Various compositions of acid are employed and the feed ratio of acid to alcohol is varied p including both conditions in accordance with the invention and for comparison.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US170264A US2618650A (en) | 1950-06-24 | 1950-06-24 | Manufacture of amyl nitrate |
GB1675152A GB731438A (en) | 1952-07-03 | 1952-07-03 | Improvements in or relating to manufacture of amyl nitrate |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1675152A GB731438A (en) | 1952-07-03 | 1952-07-03 | Improvements in or relating to manufacture of amyl nitrate |
Publications (1)
Publication Number | Publication Date |
---|---|
GB731438A true GB731438A (en) | 1955-06-08 |
Family
ID=10083000
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1675152A Expired GB731438A (en) | 1950-06-24 | 1952-07-03 | Improvements in or relating to manufacture of amyl nitrate |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB731438A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20150031909A1 (en) * | 2012-12-04 | 2015-01-29 | Shandong Libaode Chemical Co., Ltd. | Safe method for producing alkyl nitrate |
CZ305494B6 (en) * | 2014-03-07 | 2015-10-29 | Synthesia, A.S. | Continuous process for preparing alkyl nitrates having 5 to 10 carbon atoms in a molecule |
CN110746306A (en) * | 2019-10-31 | 2020-02-04 | 山东益丰生化环保股份有限公司 | Preparation method of cetane number improver |
-
1952
- 1952-07-03 GB GB1675152A patent/GB731438A/en not_active Expired
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20150031909A1 (en) * | 2012-12-04 | 2015-01-29 | Shandong Libaode Chemical Co., Ltd. | Safe method for producing alkyl nitrate |
US9365488B2 (en) * | 2012-12-04 | 2016-06-14 | Shandong Libaode Chemical Co., Ltd. | Safe method for producing alkyl nitrate |
CZ305494B6 (en) * | 2014-03-07 | 2015-10-29 | Synthesia, A.S. | Continuous process for preparing alkyl nitrates having 5 to 10 carbon atoms in a molecule |
CN110746306A (en) * | 2019-10-31 | 2020-02-04 | 山东益丰生化环保股份有限公司 | Preparation method of cetane number improver |
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