GB771640A - Improvements in or relating to production of isopropyl nitrate - Google Patents
Improvements in or relating to production of isopropyl nitrateInfo
- Publication number
- GB771640A GB771640A GB18886/55A GB1888655A GB771640A GB 771640 A GB771640 A GB 771640A GB 18886/55 A GB18886/55 A GB 18886/55A GB 1888655 A GB1888655 A GB 1888655A GB 771640 A GB771640 A GB 771640A
- Authority
- GB
- United Kingdom
- Prior art keywords
- tower
- isopropyl
- isopropyl nitrate
- reaction
- recovered
- 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
- 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
Isopropyl nitrate is produced by reacting isopropyl alcohol with aqueous nitric acid in the presence of urea in a cyclic system comprising a packed tower, circulating the reaction mixture through said tower by means of a pump, continuously introducing reaction components into the circulation conduit where also the heat required for the process is supplied, continuously discharging isopropyl nitrate and water formed in a gaseous state from the system, and continuously withdrawing liquid from the system to maintain a substantially constant volume of liquid in the system, and recovering the isopropyl nitrate so produced. The reaction components are preferably added separately on the suction side of the pump, while the heat required for the process is supplied on the pressure side, from a heat-exchanger. Preferably the circulation rate is such that the contents of the tower are changed 50-100 times per hour. The temperature is suitably maintained below the boiling-point of the reaction mixture. The vapours from the reaction tower are condensed and from the lower of the two layers so formed the ester is recovered. Unreacted isopropyl alcohol may be recovered from both layers and recycled to the process. A detailed example is given which also describes suitable apparatus. Specification 696,489 is referred to.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SE771640X | 1954-07-02 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB771640A true GB771640A (en) | 1957-04-03 |
Family
ID=20333371
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB18886/55A Expired GB771640A (en) | 1954-07-02 | 1955-06-30 | Improvements in or relating to production of isopropyl nitrate |
Country Status (2)
Country | Link |
---|---|
DE (1) | DE1046007B (en) |
GB (1) | GB771640A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102557953A (en) * | 2011-12-29 | 2012-07-11 | 北京理工大学 | Method for preparing alkyl straight chain hydrocarbon monohydric alcohol nitrate ester with 4-10 carbon atoms |
CN102557954A (en) * | 2011-12-30 | 2012-07-11 | 北京理工大学 | Preparation method for methylnitrate |
CN102816033A (en) * | 2012-09-11 | 2012-12-12 | 北京理工大学 | Carbinol nitrate full-simulation explosive mimics |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2294849A (en) * | 1938-08-20 | 1942-09-01 | Sharples Chemicals Inc | Manufacture of nitric acid esters |
BE504749A (en) * | 1950-07-24 |
-
1955
- 1955-06-28 DE DEA22963A patent/DE1046007B/en active Pending
- 1955-06-30 GB GB18886/55A patent/GB771640A/en not_active Expired
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102557953A (en) * | 2011-12-29 | 2012-07-11 | 北京理工大学 | Method for preparing alkyl straight chain hydrocarbon monohydric alcohol nitrate ester with 4-10 carbon atoms |
CN102557953B (en) * | 2011-12-29 | 2013-11-06 | 北京理工大学 | Method for preparing alkyl straight chain hydrocarbon monohydric alcohol nitrate ester with 4-10 carbon atoms |
CN102557954A (en) * | 2011-12-30 | 2012-07-11 | 北京理工大学 | Preparation method for methylnitrate |
CN102557954B (en) * | 2011-12-30 | 2013-12-04 | 北京理工大学 | Preparation method for methylnitrate |
CN102816033A (en) * | 2012-09-11 | 2012-12-12 | 北京理工大学 | Carbinol nitrate full-simulation explosive mimics |
Also Published As
Publication number | Publication date |
---|---|
DE1046007B (en) | 1958-12-11 |
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