The ARSST adiabatic bomb calorimeter reactor can also be used to determine the reaction orders. The hydrolysis of acetic anhydride to form acetic acid was carried out adiabatically

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The rate law is postulated to be of the form
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The following temperature time data were obtained for two different critical concentrations of acetic anhydride under adiabatic operation. The heating rate was 2 °C/min.
CA0 = 6.7 M, CB0 = 0.2 M
t (min) | 0.0 | 2.0 | 4.3 | 6.2 | 8.1 | 10.2 | 12.0 | 13.0 | 13.5 | 13.6 | 13.7 | 13.8 | 14 |
T(k) | 299 | 303 | 309 | 314 | 321 | 329 | 344 | 361 | 386 | 403 | 439 | 438 | 435 |

Data from Undergraduate Laboratory, University of Michigan.
(a) Assume ACP = 0 and show for complete conversion, X = 1, the difference between the final temperature, 7}, and the initial temperature, 7n,

(b) Show that the concentration of A can be written as

and CB as

and -rA as

(c) Show that the unsteady energy balance can be written as

(d) Assume first order in A and in B and that 0 g = 3 then show

(e) Rearrange Equation (P9-10.6) in the form

(f) Plot the data to obtain the activation energy and the specific reaction rate
(g) Find the heat of reaction. Additional information:
Chemical | Density (g/nil) | Heat capacity (J/g’°C) ‘ | MW | Heat capacity (J/mob°C) |
Acetic anhydride | 1.0800 | 1.860 | 102 | 189.7 |
Water | 1.0000 | 4.187 | 18 | 75.4 |
Glass cell (bomb) | 0.1474 | 0.837 |
| 0.84 J/g/°C |
Total volume 10 ml with
Water 3.638 g
Acetic anhydride 6.871 g
(MSCP = 28.012 J/°C andφ = 1.004 and msCps = φ MsCps)
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