For example 2-5, when two CSTRs and one PFR are used, and all conditions are the same, what is the worst arrangement, and at that time, what is the size of each reactor?

 

 

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Example 2-5 An Adiabatic Liquid-Phase Isomerization The isomerization of butane n-C,H10 2 i-C,H10 was carried out adiabatically in the liquid phase. The data for this reversible react are given in Table E2-5.1. (Example 11.3 shows how the data in Table E2-5.1 w generated.) TABLE E2-5.1 RAW DATA 0.0 0.2 0.4 0.6 0.65 -TA(kmol/m3 - h) 39 53 59 38 25 Don't worry how we got this data or why the (1/-rA) looks the way it does; we v see how to construct this table in Chapter 11, Example 11-3. It is real data fo real reaction carried out adiabatically, and the reactor scheme shown below Figure E2-5.1 is used. Example 2-5 An Adiabatic Liquid-Phase Isomerization The isomerization of butane n-C,H10 2 i-C,H10 was carried out adiabatically in the liquid phase. The data for this reversible react are given in Table E2-5.1. (Example 11.3 shows how the data in Table E2-5.1 w generated.) TABLE E2-5.1 RAW DATA 0.0 0.2 0.4 0.6 0.65 -TA(kmol/m3 - h) 39 53 59 38 25 Don't worry how we got this data or why the (1/-rA) looks the way it does; we v see how to construct this table in Chapter 11, Example 11-3. It is real data fo real reaction carried out adiabatically, and the reactor scheme shown below Figure E2-5.1 is used.

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Example 25 Given data Molay floo yat nbutane FAO 50 kmo... View the full answer