Question

A nonisothermal batch reactor can be described by the following equations: - (-10/(T+273)) dC dt dT = 1000 el-10/(T+273) C –A nonisothermal batch reactor can be described by the following equations: - (-10/(T+273)) dC dt dT = 1000 el-10/(T+273) C –

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Answer #1

\frac{dC}{dt} = f(t_i,C_i)= -e^{(-10/(T_i+273))}C_i

Ci+1 = C; + slope * h

Slope = f(t_{i + 1/2},C_{i+1/2})

t_{i+1/2}= t_i + *h/2

C_{i+1/2}= C_i + f(t_i,C_i)*h/2

at t =0, Ci = 1.5 , ti=0 and Ti = 17.8 deg C

Now, sample calculation is shown for i = 1 ,

t_{i+1/2}= t_i + *h/2 = 0+0.1/2 = 0.05

f(t_i,C_i)= -e^{(-10/(T_i+273))}C_i = -e^{(-10/(17.8+273))}*1.5 = -1.449

C_{i+1/2}= C_i + f(t_i,C_i)*h/2 = 1.5 +(-1.449)*0.1/2 = 1.428

Slope = f(t_{i + 1/2},C_{i+1/2}) = -e^{-10/(Ti+273)}*C_{i+1/2}=-e^{-10/(17.8+273)}*1.428=-1.379

C_{i+1}= C_i + slope*h = 1.5 +(-1.379)*(0.1)= 1.362

\frac{dT}{dt} = f(t,T)= 1000e^{(-10/(T+273))}C -7.89(T-20)

f(t_i,T_i)= 1000e^{(-10/(T_i+273))}C_i -7.89(T_i-20)= 1000e^{(-10/(17.8+273))}*1.5 -7.89(17.8-20) = 1446.6

T_{i+1/2}= T_i + f(t_i,T_i)*h/2 = 17.8 +(1446.6)*0.1/2 = 91.13

Slope = f(t_{i+1/2},T_{i+1/2})= 1000e^{(-10/(T_{i+1/2}+273))}C_i -7.89(T_{i+1/2}-20)= 1000e^{(-10/(91.13+273))}*1.5 -7.89(91.13-20) =898.1

T_{i+1}= T_i + slope*h = 17.8 +(898.1)*(0.1)= 107.6

Similarly we can calculate for other value of i

time (t) t i + 0.5 C i + 0.5 slope Conc (Ci) T i + 0.5 slope Temp (T)
min f(t i ,C i ) f(t i + 1,C i + 1) gmol/L f(t i ,T i ) f(t i + 1,T i + 1) T
0 1.5 17.8
0.1 0.05 1.449295 1.427535 -1.379279776 1.362072 1466.653 91.13265 898.1301 107.613
0.2 0.15 1.326752 1.295734 -1.262134404 1.235859 635.4851 139.3873 387.4748 146.3605
0.3 0.25 1.206737 1.175522 -1.147822007 1.121076 209.7528 156.8481 127.7076 159.1313
0.4 0.35 1.095431 1.066305 -1.041912651 1.016885 -2.31429 159.0155 -1.40809 158.9904
0.5 0.45 0.993616 0.967204 -0.94507199 0.922378 -103.019 153.8395 -62.6553 152.7249
0.6 0.55 0.900964 0.87733 -0.856961948 0.836682 -146.235 145.4132 -88.9152 143.8334
0.7 0.65 0.816848 0.795839 -0.776974004 0.758984 -160.197 135.8235 -97.3833 134.0951
0.8 0.75 0.740568 0.721956 -0.704437655 0.688541 -159.643 126.1129 -97.0273 124.3923
0.9 0.85 0.67143 0.654969 -0.638693014 0.624671 -152.225 116.7811 -92.5022 115.1421
1 0.95 0.608783 0.594232 -0.57911799 0.566759 -141.888 108.0477 -86.2053 106.5216
1.1 1.05 0.552021 0.539158 -0.52513767 0.514246 -130.634 99.98986 -79.3537 98.58621
1.2 1.15 0.500591 0.489216 -0.476226096 0.466623 -119.454 92.6135 -72.5495 91.33126
1.3 1.25 0.45399 0.443924 -0.431904684 0.423433 -108.814 85.89056 -66.0758 84.72368
1.4 1.35 0.41176 0.402845 -0.391739239 0.384259 -98.9102 79.77817 -60.0514 78.71854
1.5 1.45 0.373487 0.365584 -0.355336462 0.348725 -89.8019 74.22844 -54.5123 73.2673
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