Byproduct comprehensive utilization method in diethyl hydroxylamine production

A technology for diethylhydroxylamine and by-products is applied in the field of comprehensive utilization of by-products in the production of diethylhydroxylamine, which can solve the problems of increased energy consumption, complex process, environmental pollution, etc., and achieves the reduction of environmental pollution, the simple production process, The effect of improving economic efficiency

Inactive Publication Date: 2017-01-25
JINING KENDRAY CHEM TECH CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] This process will produce by-product ethylene. For every ton of triethylamine converted, about 0.28 tons of by-product ethylene will be produced along with the formation of diethylhydroxylamine. At present, the main treatment methods for this by-product ethylene are as follows: ( 1) Due to the small output of diethylhydroxylamine produced by domestic manufacturers, the by-product ethylene is not recycled and is generally discharged directly, causing greater environmental pollution; (2) In recent years, due to the increasingly stringent national environmental protection, the existing diethylhydroxylamine Hydroxylamine manufacturers began to use the method of ethylene gas discharge torch combustion for treatment
Although this method can reduce the environmental pollution caused by direct discharge, on the one hand, this method needs to increase additional high energy consumption, and on the other hand, it wastes a large amount of ethylene, which increases the cost of diethylhydroxylamine and reduces the competitiveness of diethylhydroxylamine; (3) Industrially, ethylene can be recovered by deep condensation, which is complex in process, high in energy consumption and uneconomical

Method used

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  • Byproduct comprehensive utilization method in diethyl hydroxylamine production

Examples

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Effect test

Embodiment 1

[0019] Example 1: The 2000L enamel reaction kettle I2 and the 2000L enamel reaction kettle II3 respectively contained 1800kg of bromine, and the 2000L enamel reaction kettle III4 contained 1400kg of water. Set the temperature of Reactor I2 and Reactor II3 to 25°C, and the temperature of Reactor III4 to 10°C. Vacuum tail gas ethylene 1 in the decompression cracking section of diethylhydroxylamine passes through reactor I2, reactor II3 and reactor III4 at a speed of 65Kg / h. After reacting for 32 hours, the color of the reaction solution becomes colorless, and the reaction ends, and the obtained product II Ethyl bromide is subjected to subsequent separation and storage.

Embodiment 2

[0020] Example 2: The 2000L enamel reaction kettle I2 and the 2000L enamel reaction kettle II3 respectively contained 1800kg of bromine, and the 2000L enamel reaction kettle III4 contained 1400kg of water. Set the temperature of Reactor I2 and Reactor II3 to be 45°C, and the temperature of Reactor III4 to be 15°C. Vacuum tail gas ethylene 1 in the decompression cracking section of diethylhydroxylamine passes through reactor I2, reactor II3 and reactor III4 at a speed of 65Kg / h. After 20 hours of reaction, the color of the reaction solution becomes colorless, and the reaction ends, and the obtained product II Ethyl bromide is subjected to subsequent separation and storage.

Embodiment 3

[0021] Example 3: 1500kg of bromine and 1500kg of carbon tetrachloride were contained in 2000L enamel reactor I2 and 2000L enamel reactor II3 respectively, and 1400kg of water was contained in 2000L enamel reactor III4. Set the temperature of Reactor I2 and Reactor II3 to 50°C, and the temperature of Reactor III4 to 20°C. Vacuum tail gas ethylene 1 in the decompression cracking section of diethylhydroxylamine passes through reactor I2, reactor II3 and reactor III4 at a speed of 65Kg / h. After 15 hours of reaction, the color of the reaction solution becomes colorless, and the reaction ends, and the obtained product II Ethyl bromide is subjected to subsequent separation and storage.

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Abstract

The invention relates to a byproduct comprehensive utilization method in diethyl hydroxylamine production. The method comprises the following steps: pyrolysis and rectification purification are carried out on the raw material triethylamine under the action of a catalyst to obtain diethyl hydroxylamine, the diethyl hydroxylamine reduced pressure pyrolysis section generates a vacuum exhaust ethylene, and the vacuum exhaust ethylene sequentially passes through a reaction kettle I, a reaction kettle II and a reaction kettle III, wherein the reaction kettle I and reaction kettle II are filled with bromine water, the bromination reaction temperatures in the reaction kettle I and reaction kettle II are 10-80 DEG C, the reaction kettle III is filled with water, and the holding temperature of the reaction kettle III is 5-50 DEG C; and after the vacuum exhaust ethylene is subjected to absorption reaction in the reaction kettle I and reaction kettle II, the ethylene inside is converted into 1,2-dibromoethane, and the unreacted vacuum exhaust ethylene is subjected to water sealing through the reaction kettle III and sent to a torch to be combusted. The method provided by the invention has the advantages of simple production technique, mild reaction and low energy consumption, can effectively lower the production cost, enhances the economic benefits and reduces the environmental pollution.

Description

technical field [0001] The present invention relates to a method for comprehensive utilization of by-products of chemical products, in particular to a method for comprehensive utilization of by-products in the production of diethylhydroxylamine. Background technique [0002] Diethylhydroxylamine is mainly used in the production, storage and polymerization of conjugated olefins such as styrene, divinylbenzene, butadiene, isoprene, methyl methacrylate and acrylonitrile As a polymerization inhibitor, it can also be used in the production of non-standard monomers and other monomers containing active bonds. As a polymerization inhibitor, diethylhydroxylamine has a high polymerization inhibition effect, and the polymerization inhibition efficiency is not affected by temperature changes. The polymerization inhibition efficiency of hydroxylamine is twice that of tert-butanediol. It not only has high polymerization inhibition efficiency in the liquid phase, but also has good polymer...

Claims

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Application Information

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IPC IPC(8): C07C17/02C07C19/075
Inventor 陈军民宋芬陈培根
Owner JINING KENDRAY CHEM TECH CO LTD
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