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Chapter 2: Conversion and Reactor Sizing
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R2.2 Space Times, τ, for a Number of Industrial Reactors
Table R2.2-1 Typical Space Time for Industrial Reactors1
Reactor Type | Mean Residence Time Range | Production Capacity |
Batch | 15 minutes to 20 hours | Few kg/day to 100,000 tons/year |
CSTR | 10 minutes to 4 hours | 10 to 3,000,000 tons/year |
Tubular | 0.5 seconds to 1 hour | 50 to 5,000,000 tons/year |
Table R2.2-2 Sample Industrial Space Times2
Reaction | Reactor | Temperature | Pressure atm | Space Times |
(1) | C2H6 → C2H4 + H2 | PFR† | 860°C | 2 | 1 s |
(2) | CH3CH2OH + HCH3COOH → CH3CH2COOCH3 + H2O | CSTR | 100°C | 1 | 2 h |
(3) | catalytic cracking | PBR | 490°C | 20 | 1 s < τ < 400 s |
(4) | C6H5CH2CH3 → C6H5CH=CH2 + H2 | PBR | 600°C | 1 | 0.2 s |
(5) | CO + H2O → CO2 + H2 | PBR | 300°C | 26 | 4.5 s |
(6) | C6H6 + HNO3 → C6H5NO2 + H2O | CSTR | 50°C | 1 | 20 min |
† The reactor is tubular but the flow may or may not be ideal plug flow. |
1Tramboue, Landeghem, and Wauquier, Chemical Reactors, p. 154, (Paris: Editions Technip, 1988; Houston: Gulf Publishing Company, 1988).
2Walas, S.M. Chemical Reactor Data, Chemical Engineering, 79 (October 14, 1985).