Method for separating and purifying byproduct isopropyl hydrazine produced in preparation of hydrazine hydrate from ketazine
A technology of ketazine hydrazine hydrate and isopropylhydrazine, which is applied in the field of separation and purification of by-products of ketazine hydrazine hydrate, can solve the problems of cumbersome operation process, many steps in the preparation method, and high parameter requirements, so as to improve economic benefits, effect of problem solving
Patent Information
- Authority / Receiving Office
- CN · China
- Current Assignee / Owner
- Publication Date
- 2019-12-31
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Figure 1
Abstract
Description
technical field
[0001] The invention relates to a method for separating and purifying a by-product of ketazine hydrazine hydrate, in particular to a method for separating and purifying isopropylhydrazine, a by-product of ketazine hydrazine hydrate. Background technique
[0002] Hydrazine hydrate, also known as: hydrazine hydrate, chemical formula is N 2 h 4 ·H 2 O, a strong reducing agent, is an important chemical raw material, and is also a raw material for medicine, pesticides, dyes, foaming agents, developers, and antioxidants; it is used for deoxidizing boiler water, producing high-purity metals, and synthesizing and reducing organic compounds. , separation of rare elements, and also used in the manufacture of rocket fuel and explosives. With the advancement of technology and the development of society, the application fields of hydrazine hydrate are constantly expanding in recent years. The production methods of hydrazine hydrate mainly include Raschig method, urea m...
Examples
Embodiment 1
[0029] Add 500 kg of a solution containing 10.30% isopropylhydrazine into the distillation still, heat to carry out distillation, control the temperature of the still still at 100-105°C, control the distillation temperature at 95-98°C, and the concentration of isopropylhydrazine after distillation is 78.25% , standing for stratification, standing for 0.5h, there is an obvious phase interface, the stratification is over, add the oil phase to the extraction kettle, add 300kg ether for extraction three times each time, combine the extracts into the distillation kettle, distill out the ether, and collect at 750mmHg 49.95kg of isopropylhydrazine was obtained from the fraction at 106-108°C, the content of which was analyzed to be 95.52%, and the calculated yield was 92.64%.
Embodiment 2
[0031]Add 500 kg of a solution containing 10.05% isopropylhydrazine into the still, heat to carry out distillation, control the temperature of the still still at 100-108°C, control the distillation temperature at 95-100°C, and the concentration of isopropylhydrazine after distillation is 80.5% , standing for stratification, standing for 1h, there is an obvious phase interface, the stratification is over, add the oil phase to the extraction kettle, add 350kg ether for extraction three times each time, combine the extracts into the distillation kettle, distill out the ether, and collect at 750mmHg 46.96kg of isopropylhydrazine was obtained from the fraction at 106-108°C, the content of which was analyzed to be 98.84%, and the calculated yield was 94.55%.
Embodiment 3
[0033] Add 500 kg of a solution containing 11.3% isopropylhydrazine into the distillation still, heat to carry out distillation, control the temperature of the still still at 101-108°C, control the distillation temperature at 95-100°C, and the concentration of isopropylhydrazine after distillation is 81.62% , standing for stratification, standing for 0.5h, there is an obvious phase interface, the stratification is over, add the oil phase to the extraction kettle, add 300kg ether for extraction three times each time, combine the extracts into the distillation kettle, distill out the ether, and collect at 750mmHg 53.0kg of isopropylhydrazine was obtained from the fraction at 106-108°C, the content of which was analyzed to be 98.50%, and the calculated yield was 92.39%.
