GB778451A - Improvements in or relating to the manufacture of hydrazine - Google Patents
Improvements in or relating to the manufacture of hydrazineInfo
- Publication number
- GB778451A GB778451A GB1707354A GB1707354A GB778451A GB 778451 A GB778451 A GB 778451A GB 1707354 A GB1707354 A GB 1707354A GB 1707354 A GB1707354 A GB 1707354A GB 778451 A GB778451 A GB 778451A
- Authority
- GB
- United Kingdom
- Prior art keywords
- ammonia
- reaction
- reaction zone
- employed
- hydrazine
- 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
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B21/00—Nitrogen; Compounds thereof
- C01B21/082—Compounds containing nitrogen and non-metals and optionally metals
- C01B21/16—Hydrazine; Salts thereof
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
In the production hydrazine by a two stage reaction of sodium hypochlorite with ammonia as aqueous medium, sufficient ammonia is initially employed to produce chloramine in an intermediate reaction zone, e.g. at a temperature less than 15 DEG C., the amount of ammonia emplayed being less than one-tenth of the total ammonia employed in the reaction, whereafter the intermediate reaction product is passed without back mixing to the final reaction zone, in the presence of a negative catalyst, after admixture with gaseous ammonia at elevated pressure to provide a molar ratio of ammonia to chloramine of 15-45 : 1 and to heat the reaction mixture to 120-150 DEG C., the reaction period in the final reaction zone being limited to 3-30 sec. The solution may be heated, if necessary, by means of a heat exchanger after introduction of the gaseous ammonia. A pressure of 200-400 p.s.i.g., preferably 300 p.s.i.g., may be maintained in the final reaction zone which may be in the form of a tubular reactor having a length to diameter ratio of 15-18 to 1. After completion of the reaction ammonia is flashed off and returned to the process. Hydrazine is recovered from the liquid remaining in known manner. As catalyst 0.066-0.33 gm. of fish glue or gelatin per litre may be employed. Specifications 22957/07 and 139/08 [both in Class I] are referred to.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1707354A GB778451A (en) | 1954-06-10 | 1954-06-10 | Improvements in or relating to the manufacture of hydrazine |
FR1107572D FR1107572A (en) | 1954-06-10 | 1954-06-17 | Improvement in the manufacture of hydrazine |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1707354A GB778451A (en) | 1954-06-10 | 1954-06-10 | Improvements in or relating to the manufacture of hydrazine |
Publications (1)
Publication Number | Publication Date |
---|---|
GB778451A true GB778451A (en) | 1957-07-10 |
Family
ID=10088772
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1707354A Expired GB778451A (en) | 1954-06-10 | 1954-06-10 | Improvements in or relating to the manufacture of hydrazine |
Country Status (2)
Country | Link |
---|---|
FR (1) | FR1107572A (en) |
GB (1) | GB778451A (en) |
-
1954
- 1954-06-10 GB GB1707354A patent/GB778451A/en not_active Expired
- 1954-06-17 FR FR1107572D patent/FR1107572A/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
FR1107572A (en) | 1956-01-03 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
ES319142A1 (en) | Procedure and apparatus for the production of peracytic acid. (Machine-translation by Google Translate, not legally binding) | |
GB840945A (en) | úÝ, úÝ-dioxydiphenols as coupling components in diazotype materials | |
GB778451A (en) | Improvements in or relating to the manufacture of hydrazine | |
GB392845A (en) | Improvements in or relating to the production of hydrazine | |
GB879441A (en) | Improved injectable iron preparations | |
GB757449A (en) | Process for fractionating starch | |
GB885575A (en) | Improvements in or relating to amino-guanidine preparation | |
GB946014A (en) | Production of dichlorobutadiene | |
GB785346A (en) | Process for the manufacture of isonicotinyl hydrazide | |
GB947842A (en) | Improved process for the preparation of nitrocyclohexane | |
GB785108A (en) | Manufacture of hexahydrobenzylamine | |
GB423286A (en) | Process of manufacturing starch products | |
GB735779A (en) | Production of ethylene diamine | |
GB705799A (en) | Guanidine sulphamate | |
GB939905A (en) | A process for preparing a penillic acid and salts thereof | |
GB652328A (en) | Preparation of iodoanthanthrones | |
GB191212845A (en) | Improvements in the Manufacture of Sulphate of Ammonia. | |
GB895681A (en) | Improvements in the preparation of glycolonitrile | |
GB722074A (en) | Improvements in or relating to the preparation of metaaminophenol | |
GB1108965A (en) | Continuous production of mucochloric acid | |
GB306575A (en) | Process for the manufacture of ortho-cyanaryl-thioglycollic acids and intermediate products | |
GB779506A (en) | Production of sulphuric acid | |
GB649123A (en) | Improvements in or relating to the production of trichloracetic acid | |
GB874070A (en) | Process for the production of n -sulphanilyl-n-butyl urea | |
GB1001881A (en) | Process for modifying calcium carbonate |