Research Article

Kinetics and Product Selectivity (Yield) of Second Order Competitive Consecutive Reactions in Fed-Batch Reactor and Plug Flow Reactor

Table 5

(a) Reactor-1 (Fed-Batch, Scheme , Part 1). (b) Reactor-2 (Plug Flow, Scheme , Part 1). (c) Reactor-1 (Fed-Batch, Scheme , Part 2). (d) Reactor-2 (Plug Flow, Scheme , Part 2). (e) Reactor-1 (Fed-Batch, Scheme , Part 3). (f) Reactor-2 (Plug Flow, Scheme , Part 3).
(a)

(s) (m3) (k mol) (k mol) (k mol) (k mol) (kg)

601.9272.1480.0270.000.1412.4997
6001.9612.1490.0270.000.052.592

(b)

(s) (m3) (k mol) (k mol) (k mol) (k mol) (kg)

61.3132.133 0.027 1.7780.983.34
601.3132.6670.027 1.7780.983.34

(c)

(s) (m3) (k mol) (k mol) (k mol) (k mol) (kg)

4501.5622.1390.0270.001.1131.52752.19
9001.6542.1410.027 0.8691.77140.75
18001.7332.1430.027 0.6581.98230.85
900 1.646 2.141 0.027 1E   12 0.868 1.75 41.71
900 1.662 2.142 0.027 1E   10 0.848 1.792 39.74

(d)

(s) (m3) (k mol) (k mol) (k mol) (k mol) (kg)

2401.3132.1330.0270.001.7780.86283.34
3601.3132.1330.0270.001.7780.86283.34
7201.3132.1330.027 1.7780.86283.34
240 1.313 2.133 0.027 0.00 1.778 0.862 83.34
240 1.313 2.133 0.027 0.00 1.778 0.862 83.34

(e)

(s) (m3) (k mol) (k mol) (k mol) (k mol) (kg)

4501.2032.130.027 2.0710.56997.1
9001.2652.1320.027 1.9070.73389.4

(f)

(s) (m3) (k mol) (k mol) (k mol) (k mol) (kg)

2402.9972.1280.0270.0212.3040.336108
3601.1242.128 0.0270.002.2840.356107