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Application of staged O2 feeding in the oxidative dehydrogenation of ethylbenzene to styrene over Al2O3 and P2O5/SiO2 catalysts

Paper ID Volume ID Publish Year Pages File Format Full-Text
39780 45835 2014 11 PDF Available
Title
Application of staged O2 feeding in the oxidative dehydrogenation of ethylbenzene to styrene over Al2O3 and P2O5/SiO2 catalysts
Abstract

•Staged feeding is very advantageous in the ODH reaction of EB to ST.•Conversion of EB and ST selectivity are a function of the overall O2 to EB molar feed ratio.•Maintaining a low (local) O2 partial pressures is essential for high ST selectivity.•The lower partial pressure of O2 and EB will result in a lower catalyst activity.

Drastic improvements in styrene yield and selectivity were achieved in the oxidative dehydrogenation of ethylbenzene by staged feeding of O2. Six isothermal packed bed reactors were used in series with intermediate feeding of O2, while all EB was fed to the first reactor, diluted with helium or CO2 (1:5 molar ratio), resulting in total O2:EB molar feed ratios of 0.2–0.6. The two catalyst samples, γ-Al2O3 and 5P/SiO2, that were applied both benefitted from this operation mode. The ethylbenzene conversion per stage and the selectivity to styrene were significantly improved. The production of COX was effectively reduced, while the selectivity to other side products remained unchanged. Compared with co-feeding at a total O2:EB molar feed ratio of 0.6, by staged feeding the EB conversion (+15% points for both catalysts), ST selectivity (+4% points for both samples) and O2 (ST) selectivity (+9% points for γ-Al2O3 and +17% points for 5P/SiO2) all improved. The ethylbenzene conversion over 5P/SiO2 can be increased from 18% to 70% by increasing the number of reactors from 1 to 6 with each reactor a total amount of O2 of 0.1 without the loss of ST selectivity (93%). For 5P/SiO2 a higher temperature (500 °C vs. 450 °C for Al2O3) is required. Essentially more catalyst (5P/SiO2) was required to achieve full O2 conversion in each reactor. Staged feeding of O2 does not eliminate the existing issues of the catalyst stability both in time-on stream and as a function of the number of catalyst regenerations (5P/SiO2), or the relatively moderate performance (relatively low styrene selectivity for γ-Al2O3).

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Keywords
Oxidative dehydrogenation; Ethylbenzene; Styrene; Staged feeding; Selectivity; Alumina; Phosphorous; Silica; Catalyst coking; Catalyst stability
First Page Preview
Application of staged O2 feeding in the oxidative dehydrogenation of ethylbenzene to styrene over Al2O3 and P2O5/SiO2 catalysts
Publisher
Database: Elsevier - ScienceDirect
Journal: Applied Catalysis A: General - Volume 476, 22 April 2014, Pages 204–214
Authors
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Subjects
Physical Sciences and Engineering Chemical Engineering Catalysis