Normal heptane is dehydrocyclicized to toluene and hydrogen in a continuous vapor-phase reaction: C7H16 → C6H5CH3 + 4 H2 Pure heptane at 400°C is fed to the reactor at a rate of 100 mol/s. The reactor...


Normal heptane is dehydrocyclicized to toluene and hydrogen in a continuous vapor-phase
reaction:
C7H16 → C6H5CH3 + 4 H2
Pure heptane at 400°C is fed to the reactor at a rate of 100 mol/s. The reactor operates
isothermally at 400°C and the reaction goes to completion. Data: The average heat capacity of nheptane between 25°C and 400°C is 0.2427 kJ/(mol°C). Calculate the required heat transfer to or
from the reactor in kJ/s. What is the heat of the heptane dehydrocyclization reaction at 400°C and
1 atm?


C, (NO)=29.5x10-3 +0.8188x10-s T -0.2925x10-8T2+0.3653x10-12T3<br>[kJ/molK]<br>AHE (kJ/mol)<br>NH3<br>-46.19<br>NO<br>90.37<br>C, (kJ/molK)<br>34.31 x10-3+ 5.469x10-ST+0.3661x10-8T2-11x10-12T3<br>29.1 x10-3+ 1.158x10-5T-0.6076x10-8T2+1.311 x10-12T3<br>29 x10-3+ 0.2199x10-ST+0.5723x10-8T2-2.871 x10-12T3<br>AHº (kJ/mol)<br>CH4<br>T(°C)<br>T(°C)<br>T(°C)<br>T(°C)<br>T(°C)<br>T(°C)<br>T(°C)<br>T(°C)<br>T(°C)<br>-74.85<br>02<br>N2<br>НСНО<br>-115.9<br>34.28 x10-3+ 4.268x10-5T-8.694x10-12T3<br>CO2<br>-393.5<br>36.11x10-3 + 4.233x10-5T-2.887x10-8T2<br>H20(v)<br>-241.83<br>33.46 x10-34 0.6880x10-ST+0.7604x10-8T2-3.593x10-12T3<br>C2H5OH<br>-235.31<br>61.34 x10-3+ 15.72x10-ST-8.749x10-8T²+19.83x10-12T3<br>CH3CHO<br>-166.2<br>0.05048+ 1.326X104T-8.050x10$T²+2.380 x10-11T³<br>H2<br>28.84x10-3+0.00765x10-5T+0.3288x10-8T2-0.8698x10-12T3<br>C7H16<br>-187.8<br>0.2427<br>C6HSCH3<br>50<br>94.18 x10-3+ 38x10-5T-27.86x10-8T2+8.033x10-12T3<br>T(°C) |<br>(C2H5)20(1)<br>-272.8<br>0.08945+ 40.33x10-5T-2.244x10-7T2 T(°C)_<br>C2H4<br>52.28<br>40.75 x10-3+ 11.47x10-5T-6.891x10-8T2+17.66x10-12T3<br>C2H40<br>-51<br>-4.69+0.2061T-9.995X10-ST²<br>(J/molK)<br>T(K)<br>H20(1)<br>-285.84<br>Heat of vaporization of diethylether =26.05 kJ/mol<br>Table B.8 Specific Enthalpies of Selected Gases: SI Units<br>À(kJ/mol)<br>Reference state: Gas, Pret = 1 atm, Tref = 25°C<br>Air<br>co<br>CO:<br>H;O<br>-0.72<br>-0.73<br>-0.73<br>-0.72<br>-0.73<br>-0.92<br>-0.84<br>25<br>0.00<br>0.00<br>0.00<br>0.00<br>0.00<br>0.00<br>0.00<br>2.19<br>2.19<br>2.16<br>2.54<br>6.01<br>9.57<br>13.23<br>100<br>2.24<br>2.19<br>2.90<br>200<br>5.15<br>5.31<br>8.47<br>5.13<br>5.06<br>5.16<br>7.08<br>300<br>8.17<br>8.12<br>7.96<br>8.17<br>11.58<br>400<br>11.24<br>11.72<br>11.15<br>10.89<br>11.25<br>16.35<br>500<br>14.37<br>15.03<br>14.24<br>13.83<br>14.38<br>21.34<br>17.01<br>600<br>17.55<br>18.41<br>17.39<br>16.81<br>17.57<br>26.53<br>20.91<br>20.59<br>23.86<br>27.19<br>30.56<br>19.81<br>22.85<br>700<br>20.80<br>21.86<br>20.82<br>31.88<br>24.92<br>29.05<br>33.32<br>37.69<br>800<br>24.10<br>25.35<br>24.13<br>37.36<br>900<br>27.46<br>25.93<br>28.89<br>32.47<br>27.49<br>42.94<br>1000<br>30.86<br>29.04<br>30.91<br>48.60<br>1100<br>34.31<br>36.07<br>33.99<br>32.19<br>34.37<br>54.33<br>42.18<br>35.39<br>37.81<br>41.34<br>1200<br>39.70<br>37.46<br>37.87<br>60.14<br>46.78<br>1300<br>43.38<br>47.07<br>40.97<br>38.62<br>41.40<br>65.98<br>51.47<br>56.25<br>61.09<br>1400<br>44.89<br>44.51<br>41.90<br>44.95<br>71.89<br>1500<br>48.45<br>50.77<br>48.06<br>45.22<br>48.51<br>77.84<br>

Extracted text: C, (NO)=29.5x10-3 +0.8188x10-s T -0.2925x10-8T2+0.3653x10-12T3 [kJ/molK] AHE (kJ/mol) NH3 -46.19 NO 90.37 C, (kJ/molK) 34.31 x10-3+ 5.469x10-ST+0.3661x10-8T2-11x10-12T3 29.1 x10-3+ 1.158x10-5T-0.6076x10-8T2+1.311 x10-12T3 29 x10-3+ 0.2199x10-ST+0.5723x10-8T2-2.871 x10-12T3 AHº (kJ/mol) CH4 T(°C) T(°C) T(°C) T(°C) T(°C) T(°C) T(°C) T(°C) T(°C) -74.85 02 N2 НСНО -115.9 34.28 x10-3+ 4.268x10-5T-8.694x10-12T3 CO2 -393.5 36.11x10-3 + 4.233x10-5T-2.887x10-8T2 H20(v) -241.83 33.46 x10-34 0.6880x10-ST+0.7604x10-8T2-3.593x10-12T3 C2H5OH -235.31 61.34 x10-3+ 15.72x10-ST-8.749x10-8T²+19.83x10-12T3 CH3CHO -166.2 0.05048+ 1.326X104T-8.050x10$T²+2.380 x10-11T³ H2 28.84x10-3+0.00765x10-5T+0.3288x10-8T2-0.8698x10-12T3 C7H16 -187.8 0.2427 C6HSCH3 50 94.18 x10-3+ 38x10-5T-27.86x10-8T2+8.033x10-12T3 T(°C) | (C2H5)20(1) -272.8 0.08945+ 40.33x10-5T-2.244x10-7T2 T(°C)_ C2H4 52.28 40.75 x10-3+ 11.47x10-5T-6.891x10-8T2+17.66x10-12T3 C2H40 -51 -4.69+0.2061T-9.995X10-ST² (J/molK) T(K) H20(1) -285.84 Heat of vaporization of diethylether =26.05 kJ/mol Table B.8 Specific Enthalpies of Selected Gases: SI Units À(kJ/mol) Reference state: Gas, Pret = 1 atm, Tref = 25°C Air co CO: H;O -0.72 -0.73 -0.73 -0.72 -0.73 -0.92 -0.84 25 0.00 0.00 0.00 0.00 0.00 0.00 0.00 2.19 2.19 2.16 2.54 6.01 9.57 13.23 100 2.24 2.19 2.90 200 5.15 5.31 8.47 5.13 5.06 5.16 7.08 300 8.17 8.12 7.96 8.17 11.58 400 11.24 11.72 11.15 10.89 11.25 16.35 500 14.37 15.03 14.24 13.83 14.38 21.34 17.01 600 17.55 18.41 17.39 16.81 17.57 26.53 20.91 20.59 23.86 27.19 30.56 19.81 22.85 700 20.80 21.86 20.82 31.88 24.92 29.05 33.32 37.69 800 24.10 25.35 24.13 37.36 900 27.46 25.93 28.89 32.47 27.49 42.94 1000 30.86 29.04 30.91 48.60 1100 34.31 36.07 33.99 32.19 34.37 54.33 42.18 35.39 37.81 41.34 1200 39.70 37.46 37.87 60.14 46.78 1300 43.38 47.07 40.97 38.62 41.40 65.98 51.47 56.25 61.09 1400 44.89 44.51 41.90 44.95 71.89 1500 48.45 50.77 48.06 45.22 48.51 77.84
Jun 11, 2022
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