The platform will undergo maintenance on Sep 14 at about 7:45 AM EST and will be unavailable for approximately 2 hours.
1979
DOI: 10.1021/i260071a012
|View full text |Cite
|
Sign up to set email alerts
|

Synthesis of Epichlorohydrin by Elimination of Hydrogen Chloride from Chlorohydrins. 1. Kinetic Aspects of the Process

Abstract: The reactions involved in epichlorohydrin industrial production have been studied. The reactions can be divided into two groups: ring closure (dehydrochlorination) and ring opening (epoxide hydrolysis). Two analytical techniques, potentiometry and gas chromatography, have been employed in order to follow the time evolution of the reagents. The kinetic parameters of the reactions have been determined and a kinetic model of the overall system is offered.

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
1
1
1

Citation Types

1
59
0
1

Year Published

2004
2004
2023
2023

Publication Types

Select...
6
1

Relationship

0
7

Authors

Journals

citations
Cited by 39 publications
(61 citation statements)
references
References 1 publication
(2 reference statements)
1
59
0
1
Order By: Relevance
“…This is manifested in the 1,3-DCH/2,3-DCH ratio, which is 30 -50 in the GTE process, but only about 3:1 in the incumbent process. The value of improved 1,3-regioselectivity is that 1,3-DCH undergoes cyclization with base to form epichlorohydrin about 300 times faster than does 2,3-DCH [12]. This translates into smaller process equipment and/or shorter residence times.…”
Section: Resultsmentioning
confidence: 99%
“…This is manifested in the 1,3-DCH/2,3-DCH ratio, which is 30 -50 in the GTE process, but only about 3:1 in the incumbent process. The value of improved 1,3-regioselectivity is that 1,3-DCH undergoes cyclization with base to form epichlorohydrin about 300 times faster than does 2,3-DCH [12]. This translates into smaller process equipment and/or shorter residence times.…”
Section: Resultsmentioning
confidence: 99%
“…The following modeling assumptions are made in this paper: [3,4,14,16] (1) the concentration of HAC is constant due to its catalytic function in the reaction system, (2) the concentration of HCl is constant and can be obtained according to its saturation in the organic phase due to its weak/difficult dissolution ability in the organic phase, (3) the concentration of H 2 O is constant due to its surplus in the reaction system, and (4) the quasi-stationary-state assumption is applied. Therefore, according to the reaction steps shown in Scheme 2, the mass balance equations can be worked out.…”
Section: Kinetic Modelmentioning
confidence: 99%
“…1,3-Dichloro-2-propanol (1,3-DCP) is an intermediate for the production of epichlorohydrin (ECH, 1-chloro-2,3-epoypropane) [1], which is an important intermediate for the chemical industry [1][2][3]. Recently, a direct process to prepare 1,3-DCP consisting of the chlorination of glycerol (GLY) with hydrochloric acid (HCl) was developed [2,3], and the process has been widely applied in the industry.…”
Section: Introductionmentioning
confidence: 99%
See 1 more Smart Citation
“…Details on some of the reaction kinetics of this type of reaction system can be found in Carra, Santacesaria, and Morbidelli (1979). However, the model presented in Carra et al (1979) requires many parameters, such as reaction rates, to be determined when applied to practical systems so that only qualitative information is taken in this paper.…”
Section: Description Of the Processmentioning
confidence: 99%