Industrial reactor technology and operation
Calculation of catalytic reactors

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J4030 V2 Article

Industrial reactor technology and operation
Calculation of catalytic reactors

Author : Gérard HUSTACHE

Publication date: December 10, 1997 | Lire en français

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4. Industrial reactor technology and operation

4.1 Hydrodynamics

As the empty-barrel gas velocity increases (at constant gas composi-tion), the amount of SO 2 that presents itself to the catalyst per unit time increases and consequently the conversion percentage decreases.

In practice, the gas velocity in industrial reactors is between 0.3 and 0.5 Nm 3 .m –2 .s –1 [8] . Figure 10 shows the variation...

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