Research Article

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

Table 2

(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)

601.292.1320.0270.001.840.80186.23
6001.292.1320.0270.001.840.886.24

(b)

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

61.2912.1320.026 1.8380.80386.14
601.2912.1320.0260.001.8380.80386.14

(c)   

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

4501.292.1320.027 1.840.886.24
9001.292.1320.027 1.840.886.24
18001.292.1320.027 1.840.886.24
900 1.29 2.132 0.027 1E   06 1.84 0.8 86.24
900 1.29 2.132 0.027 1E   06 1.84 0.8 86.24

(d)

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

2401.3132.1330.0270.0611.840.886.25
3601.2962.1320.0270.0161.840.886.24
7201.292.1320.027 1.840.886.24
240 1.313 2.133 0.027 0.061 1.84 0.8 86.25
240 1.313 2.133 0.027 0.061 1.84 0.8 86.25

(e)

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

4501.062.1270.0270.0022.4540.186115.1
9001.062.1270.0270.0012.4540.186115.1

(f)

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

2401.1172.1280.0270.1522.4540.186115.1
3601.0862.1270.0270.072.4540.186115.1