Research Article

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

Table 9

(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)

601.762.1440.0270.000.5882.05227.5
6001.8922.1470.0270.000.2342.40611.0

(b)

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

61.2162.13 0.027 2.0370.695.5
601.2162.130.0270.0002.0370.695.5

(c)

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

4501.3182.1330.027 1.7650.87582.7
9001.3662.1240.027 1.6381.00276.8
18001.4232.1360.027 1.4851.15569.6
900 1.359 2.134 0.027 8E   06 1.656 0.984 77.6
900 1.374 2.667 0.027 1E   05 1.615 1.025 75.7

(d)

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

2401.2182.130.0270.0292.060.5896.55
3601.2162.130.0270.0082.0440.59695.8
7201.2162.130.027 2.0380.60295.51
240 1.218 2.13 0.027 0.029 2.06 0.58 96.55
240 1.218 2.13 0.027 0.029 2.06 0.58 96.55

(e)

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

4501.0782.1270.0270.0032.4080.232112.9
9001.092.1270.0270.0022.3760.264111.4

(f)

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

2401.0762.1270.0270.0872.4980.142117.1
3601.0652.1270.0270.0462.4860.154116.6