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Anita Kova Kralj
Faculty of Chemistry and Chemical Engineering, University of Maribor, Smetanova 17, Maribor, Slovenia
Received December 13, 2006; Accepted April 4, 2007Abstract:The hydrolysis of acetic anhydride to acetic acid was studied by measuring the conductivity. The
measurements were based on the conductivity of a weak electrolyte. The reaction kinetics when producing ace-
tic acid (CH 3COOH) from acetic anhydride ((CH
3 CO) 2O) and water (H
2O) was checked in a stirred batch re-
actor under different temperatures (T 1 = 20 o C, T 2 = 23 oC and T
3 = 26 o C): (CH 3 CO) 2 O + H 2O 侟2 CH
3 COOHThe course of the reaction was followed by measuring a weak electrolyte conductivity, in our case, acetic
acid. The kinetic parameters of acetic acid production (activation energy, reaction rate constant, rate order)
were determined. Experimental data agrees quite well with the data in the literature.Keywords:hydrolysis of the acetic anhydride, production of the acetic acid, kinetics, reaction rate constant,
activation energy, rate order, conductivityIntroduction
1) Quite a few studies have been reported in literature on the kinetics of acetic anhydride hydrolysis. Eldridge and Piret [1] obtained the pseudo-first-order reaction rate constant using a batch reactor. In order to determine the acetic anhydride concentration, samples from the reactor were withdrawn into tarred flasks containing 15佢20 times the quantity of saturated aniline-water required to react with the sample. Since the anhydride rapidly acety- lates the aniline, producing acetanilide and acetic acid, the samples were then titrated to determine the concen- tration of acetic acid. In another study, Shatyski and Hanesian [2] determined the kinetics of the above re- action by using temperature-time data obtained under adiabatic conditions in a batch reactor. The use of in-situ FTIR spectroscopy for following the hydrolysis of acetic anhydride reaction has been demonstrated [3]. The analy- sis of the batch reactor data showed that the hydrolysis of acetic anhydride is a pseudo-first order reaction. The rate constants were calculated from the batch data using both integral and differential methods of analysis. In this paper the kinetics of the hydrolysis of acetic an-To whom all correspondence should be addressed.
(e-mail: anita.kovac@uni-mb.si) hydride to acetic acid were studied by measuring the conductivity.Conductivity
Further insight into the nature of molecular motion can be obtained by studying the motion of ions in solution, for ions can be dragged through the solvent by the appli- cation of a potential difference between two electrodes immersed in the sample. The fundamental measurement used to study the motion of ions is that of the electrical resistance, R, of the sol- ution [4]. The conductance, G, of a solution is the inverse of its resistance R: G = 1/R. As resistance is expressed in ohms, 儅, the conductance of a sample is expressed as -1 . The reciprocal ohm used to be called the mho, but its official designation is now the siemens, S, and 1S = 1 -1 . The conductance of a sample decreases with its length l and increases with its cross-sectional area A. We therefore write: (1) where 儗is the conductivity. With the conductance inAnita Kova Kralj632
siemens and the dimensions in meters, it follows that theSI units of 儗are siemens per metre (S m
1 The conductivity of a solution depends on the number of ions present, and it is normal to introduce the molar conductivity, , which is defined as: (2) where c is the molar concentration of the added electrolyte. The SI unit of molar conductivity is siemens metre-squared per mole (S m 2 mol -1 The molar conductivity is found to vary according to the concentration. One reason for this variation is that the number of ions in the solution might not be proportional to the concentration of the electrolyte. For instance, the concentration of ions in a solution of a weak acid de- pends on the concentration of the acid in a complicated way, and doubling the concentration of the acid added does not double the number of ions. Secondly, because ions interact strongly with one another, the conductivity of a solution is not exactly proportional to the number of ions present. The concentration dependence of molar conductivities indicates that there are two classes of electrolyte. The characteristic of a strong electrolyte is that its molar conductivity depends only slightly on the molar concentration. The characteristic of a weak elec- trolyte is that its molar conductivity is normal at concen- trations close to zero, but falls sharply to low values as the concentration increases.Weak Electrolytes
Weak electrolytes are not fully ionised in solution [4]. They include weak Bronsted acids and bases, such as CH 3COOH and NH
3 . The marked concentration depend- ence of their molar conductivities arises from the dis- placement of the equilibrium:HA(aq) + H
2O(l) 侟H
3 O (aq) + A (aq) towards products at low molar concentrations. The conductivity depends on the number of ions in the solution, and therefore on the degree of ionisation, 儎, of the electrolyte; when referring to weak acids, we speak of the degree of deprotonation. It is defined so that, for the acid HA at a molar concentration c, at equilibrium: [H 3 O ] = 儎c [A] = 儎c [HA] = (1-儎)c If we ignore activity coefficients, the acidity constant, K a , is approximately: (3) The acid is fully deprotonated at infinite dilution, and its molar conductivity is then . Because only a frac- tion 儎is actually present as ions in the actual solution, the measured molar conductivity is given by: (4) For the weak electrolyte the 儎is nearly 0 and for the strong electrolyte the 儎draws near to 1. The concentration, c, is calculated from the eq. 3: (5) The degree of ionisation, 儎, is calculated from the eq.4 by considering eqs. 2 and 5:
(6)Reaction Rate
For a constant-volume batch reactor [3], the rate of ap- pearance of reactant A (acetic anhydride), r A , is given by: (7) where r A can be expressed as: (8) where k is the reaction rate constant, n and m are the re- action orders with respect to species A (acetic anhydride) and B (water), respectively. Since water is in excess, c B remains essentially unchaged during the course of the re- action: (9) where k' is a pseudo rate constant (10) The concentration of B remains constant at volume ratioV (Ac:H
2O) = 1:10 [5], but we use the volume ratio 1:25.
Checking the Kinetics of Acetic Acid Production by Measuring the Conductivity633 Table 1. The Kinetics Parameters from the LiteratureRate constant,
k/min -1T = 20
oC0.0924
T = 25
oC0.1580
T = 35
oC0.2752
Activation energy, E
a/(kJ/mol) 50.2Order of reaction Pseudo-first order
k, is a function of reaction temperature and is given by the Arrhenius equation: (11) where k 0 is a pre-exponential factor, E a is the activation energy for the reaction, and T is the absolute tempera- ture. The reaction order and rate constant can be determined by the integral method of analysis. In this method, the rate expression is guessed and the differential equation used to model the batch system is integrated. If the as- sumed order is correct, the appropriate plot (determined from the integration) of concentration-time data should be linear.For the first-order case where
, integration of equation 7 yields: (12) where c A is acetic anhydride concentration and c A0 is ini- tial acetic anhydride concentration. The differential method can also be used to analyse the rate data. In this method, the reaction rate at each con- centration is determined by differentiating concentration versus time data. By combining the mole balance (eq. 7) with the rate law (eq. 9), we obtain: (13) Taking the logarithm of both sides of eq. 13 gives: (14)The slope of a plot of
is the reaction order.Kinetics Parameter
The hydrolysis of acetic anhydride ((CH
3 CO) 2O) to ace-
tic acid (CH 3COOH ) takes place:
Figure 1. The apparatus - stirred batch reactor.
(CH 3 CO) 2 O + H 2O 侟2 CH
3 COOH, AB C r H 298= - 56 kJ/mol (15) The final reaction product is a harmless acetic acid sol- ution in water with degree of conversion, X A = 98 %. The reaction is carried out in a batch reactor over three different temperatures (T 1 = 20 o C, T 2 = 23 o
C and T
3 26o C). The kinetics parameters from the literature [3] are in