Methods for preparing halogenated ethanol and ethylene oxide by dry gas
A technology of ethylene oxide and haloethanol, which is applied in the introduction of hydroxyl and halogen preparation, bulk chemical production, organic chemistry, etc., can solve the problems of environmental pollution, difficult treatment, and large water consumption.
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0097] A method for preparing haloethanol from dry gas, the method may further comprise the steps:
[0098] (1) Haloalcoholization: Add 70wt% concentration of hydrogen peroxide H 2 o 2 Aqueous solution, 35wt% concentration of HCl solution (hydrochloric acid) and dry gas (the volume content of ethylene is 33.9vol%), at a temperature of 45 ℃, carry out chlorohydrinization reaction, wherein 70wt% concentration of hydrogen peroxide H 2 o 2 , 35wt% concentration of HCl solution and the flow rate of dry gas should make H 2 o 2 The volume ratio of HCl to dry gas is about 1.1:1.5:1. Chlorohydrin is obtained.
Embodiment 2
[0103] A method for preparing haloethanol from dry gas, the method may further comprise the steps:
[0104] 1) Haloalcoholization: add tungstic acid catalyst, 35wt% concentration of hydrogen peroxide H in the tower reactor 2 o 2 , HCl solution (hydrochloric acid) and dry gas of 20wt% concentration, carry out chlorohydrinization reaction at the temperature of 35 ℃, wherein the mass ratio of tungstic acid catalyst and dry gas is 0.05:1, the hydrogen peroxide H of 35wt% concentration 2 o 2 , 20wt% concentration of HCl solution and the addition of dry gas should make H 2 o 2 The volume ratio of HCl to dry gas is about 2:3:1. Chlorohydrin is obtained.
Embodiment 3
[0112] A method for preparing ethylene oxide from dry gas, the method may further comprise the steps:
[0113] (1) Haloalcoholization: add tungstic acid catalyst, 35wt% concentration of hydrogen peroxide H in the tower reactor 2 o 2 , HCl solution (hydrochloric acid) of 20wt% concentration and dry gas, carry out chlorohydrinization reaction at the temperature of 35 ℃, wherein the hydrogen peroxide H of 35wt% concentration 2 o 2 , 20wt% concentration of HCl solution and dry alkene three flow should make H 2 o 2 The volume ratio of HCl to dry gas is about 1.1:1.5:1. Chlorohydrin is obtained.
[0114] (2) Saponification: carry out saponification reaction with the chloroethanol obtained in step (1) and sodium hydroxide, obtain ethylene oxide organic phase and sodium chloride solution. The saponification reaction is carried out in a steel tower reactor, and the upper part is designed as a sieve tray tower. Steam enters from the bottom of the tower to blow out the crude ethyl...
PUM
Abstract
Description
Claims
Application Information
- R&D Engineer
- R&D Manager
- IP Professional
- Industry Leading Data Capabilities
- Powerful AI technology
- Patent DNA Extraction
Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic, Popular Technical Reports.
© 2024 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap|About US| Contact US: help@patsnap.com