80 jo a hw 19-4_dc6c0... → →: Tisomerization of butane n-C,H10 i-C,H10 was carried out adiabatically in the liquid phase. The data for this reversible reaction are given in Table E2-5.1. (Example 11.3...

80<br>jo a hw 19-4_dc6c0...<br>→ →:<br>Tisomerization of butane<br>n-C,H10 i-C,H10<br>was carried out adiabatically in the liquid phase. The data for this reversible reaction<br>are given in Table E2-5.1. (Example 11.3 shows how the data in Table E2-5.1 were<br>generated.)<br>TABLE E2-5.1<br>RAw DATA<br>X<br>0.0<br>0.2<br>0.4<br>0.6<br>0.65<br>-r,(kmol/m h)<br>39<br>53<br>59<br>38<br>25<br>X, = 0.2<br>X2 = 0.6<br>V2<br>FAI<br>X = 0.65<br>Figure E2-5.1 Reactors in series.<br>Calculate the volume of each of the reactors for an entering molar flow rate of<br>n-butane of 50 kmol/hr.<br>Sol<br>ically and graphically<br>

Extracted text: 80 jo a hw 19-4_dc6c0... → →: Tisomerization of butane n-C,H10 i-C,H10 was carried out adiabatically in the liquid phase. The data for this reversible reaction are given in Table E2-5.1. (Example 11.3 shows how the data in Table E2-5.1 were generated.) TABLE E2-5.1 RAw DATA X 0.0 0.2 0.4 0.6 0.65 -r,(kmol/m h) 39 53 59 38 25 X, = 0.2 X2 = 0.6 V2 FAI X = 0.65 Figure E2-5.1 Reactors in series. Calculate the volume of each of the reactors for an entering molar flow rate of n-butane of 50 kmol/hr. Sol ically and graphically

Jun 10, 2022

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80 jo a hw 19-4_dc6c0... → →: Tisomerization of butane n-C,H10 i-C,H10 was carried out adiabatically in the liquid phase. The data for this reversible reaction are given in Table E2-5.1. (Example 11.3...

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