Research Article

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

Table 10

(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)

601.0192.1250.0270.002.5640.077120.2
6000.9942.1250.0270.002.63 123.3

(b)

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

61.4192.135 0.027 1.4971.170.15
601.4192.1350.027 1.4971.170.15

(c)

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

4501.3022.1330.027 1.8070.83384.7
9001.252.1310.027 1.9460.69491.2
18001.1922.130.027 2.1010.53998.5
900 1.254 2.131 0.027 4E   15 1.936 0.704 90.7
900 1.246 2.131 0.027 4E   15 1.957 0.683 91.7

(d)

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

2401.7712.1440.0270.4080.9651.67545.25
3601.5442.1390.0270.0881.2511.38958.6
7201.4252.1360.0270.0011.4821.15869.49
240 1.771 2.144 0.027 0.408 0.965 1.675 45.25
240 1.771 2.144 0.027 0.408 0.965 1.675 45.25

(e)

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

4501.042.6670.027 2.5060.134117.5
9001.0342.1260.027 2.5230.117118.3

(f)

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

2401.42.1350.0270.6242.170.47101.7
3601.1912.130.0270.2022.3070.333108.1