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The catalyst test apparatus is shown in Fig. 1.
The setup for catalyst test is shown in Fig. 1.
The simulation results are compared with the Pt catalyst test results.
With parallel testing in multi-tubular catalyst test units there are even greater possibilities.
The catalyst test conditions are: 70 bar, H2/CO ratio = 2, GHSV = 3,000 h−1, internal calibration 5 vol% N2 in syngas stream.
The catalyst test conditions are: 70 bar, H2/CO ratio = 2, GHSV = 3,000 h−1 Open image in new window Fig. 5 The catalyst performance of 1.6 % K 3.5 % Co 40%% Mo2C/Al2O3 B2O3 catalyst for syngas to alcohol.
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The information from catalyst testing should be scalable.
This enables parallel catalyst testing, which enhances the number of catalysts tested significantly and reduces the time for kinetic studies.
A differential packed-bed reactor microfabricated in silicon is presented for heterogeneous gas phase catalyst testing.
The paper presents the coupled results on reactor structure modelling and the catalyst testing.
The catalyst tests employed a fixed bed reactor system, connected with gas chromatography system (online GC, off line GC/MS).
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