Title : Oxidative dehydrogenation of 4-vinylcyclohexene to styrene in a two section reactor on metal-containing zeolites
Abstract:
This abstract presents the results of the oxidative dehydrogenation of 4-vinylcyclohexene in a two-section reactor in the presence of g-Al2O3 (1st section) and Fe-Zr-Gd-La/HNa-ZSM-5 (2nd section).
For the study, we used Fe-Zr-M-O/HNa- ZSM-5 (M-alkali or rare earth elements) catalytic systems prepared according to the method.
We previously established that in the temperature range of 250-320°C the main reaction products are conjugated dienes formed as a result of the migration of double bonds. The migration of double bonds in the substrate molecule in this temperature range is thermodynamically more favorable which leads to a sharp increase in the content of 3-ethylidenecyclohexene and ethylcyclohexadiene-1,3 isomers (52-57%).
In order to find experimental confirmation of these assumptions about possible reaction routes and obtain comparative results, the experiments on the dehydrogenation of 4-VCH were carried out in the two-section reactor with a section-by-section supply of oxygen. In the first section, 4-VCH was isomerized over g-Al2O3 or Ga2O3/HNa-ZSM-5 at a temperature of 350-375°C; and in the second section, dehydrogenation of the forming isomerate over Fe-Zr-Gd-La/HNa-ZSM-5 in the temperature range of 400-450°C.
The obtained results are presented in a table and it is seen that at a temperature of 350/420-375°C/450°C and a molar ratio of 4-VCH:CO2:O2=1:4-5:0.05-0.1 the yield of ethylbenzene and styrene increases to 69.0-72.0%. The selectivity of the reaction as a result of reducing the degree of destructive oxidation, cracking and other side reactions of 4-VCH increases from 75.0-77.0 to 86.8-87.2%. Thus, the use of the two-section reactor helps to increase the yield of target products in the temperature range of 350-450°C.