Research Article

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

Table 4

(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)

601.9092.1480.0270.000.192.459
6001.952.1490.0270.000.0792.5614

(b)

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

61.4482.136 0.027 1.4191.266.52
601.4472.1360.027 1.421.266.57

(c)

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

4501.5982.140.027 1.0191.62147.76
9001.6612.1420.027 0.8511.78939.89
18001.7222.1430.027 0.6871.95332.22
900 1.655 2.141 0.027 0.868 1.772 40.67
900 1.668 2.142 0.027 0.833 1.807 39.05

(d)

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

2401.4482.1360.027 1.4191.22166.52
3601.4482.1360.027 1.4191.22166.52
7201.4482.1360.027 1.4191.22166.52
240 1.448 2.136 0.027 4E   12 1.419 1.221 66.52
240 1.448 2.136 0.027 4E   12 1.419 1.221 66.52

(e)

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

4501.2142.130.0270.0002.0430.59795.75
9001.2512.1310.0270.0001.9430.69791.07

(f)

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

2401.1722.1290.0270.0712.2270.413104.4
3601.1632.1290.0270.0032.1820.458102.3