Journal of Crystal Growth North-Holland 126 (1993) 493-498 10U'"><0' CRVSTAL GROWTH Ca1cium oxalate monohydrate precipitation investigation by thermometric method O. Sohnel, A. Costa-Bauzá 1 and V. Velich lnstitute of Chemical Technology, Department of lnorganic Processes, Nám. Legií 565, 532 lO Pardubice, Czechoslouakia Received 27 March 1992; manuscript received in final form 9 October 1992 Calcium oxalate monohydrate (COM) precipitation from diluted solutions of 100 mol m -3 ionic strength at 25°C was studied by an isoperibolic reaction twin calorimeter. The molar reaction enthalpy was determined as - 17.5 kJ mol-l. Results achieved with a pure system were highly reproducible. Citrate, pyrophosphate and phytate retard COM precipitation that is manifested mainly by an induction period appearance and a decrease of the initial precipitation rateo Effect of the studied impurities on individual precipitation experiments carried out under identical conditions was to so me extent "random", i.e. the reaction extent reached at arbitrary time considerably differed for individual experiments. Impurity effectiveness in retarding spontaneous precipitation < phytate. increases in succession citrate < pyrophosphate 1. Introduction Preeipitation kineties of ealcium oxalate monohydrate (hereafter COM) were studied using a wide variety of experimental methods based on evolution of erystal size distribution [1], deerease of ealcium eoneentration in solution [2], development of the systems optieal turbidity [3], linear displaeement of erystal faee [4], eonsumption of reaetants by the system [5] and others. Most of these methods follow a quantity diffieult to determine with reasonable aeeuraey. Furthermore the quantity is often indireetly related to the erystal growth and henee ealibration, usually nonlinear and of limited preeision, must be introdueed. Therefore, reliability of these results is somewhat restrieted. Thermometrie methods, espeeially those involving eompensation of eomplementary heat effeets assoeiated with dilution, stirring, heat losses, ete., measure the heat evolved on reaetion and this quantity is direetly, lineariy and unequivo- 1 Permanent address: Department of Chemistry, University the Balearic Islands, 07 071 Palma de Mallorca, Spain. 0022-0248/93/$06.00 © 1993 - Elsevier Science Publishers of eally related to the mass of solid preeipitated from the system. Moreover, measurement of temperature on whieh a ealorimetry is based is very aeeurate and sensitive. Sinee an isoperibolie reaetion twin ealorimeter satisfies all requirements given above, it represents a sensitive and reliable teehnique for studying the kineties of preeipitation. This teehnique has already demonstrated its value in studying homogeneous reaetion kineties [6,7] and also a limited applieation to heterogeneous reaetions [8]. This eontribution reports on results aehieved using an isoperibolie reaetion twin ealorimeter and studying ealcium oxalate monohydrate preeipitation from diluted solutions. Speeial attention is given to the effeet of impurities, speeifieally phytie aeid, sodium pyrophosphate and eitrate, on the preeipitation kineties of COMo 2. Experimental procedure The isoperibolie reaetion twin ealorimeter used in the study of COM preeipitation from solutions of CaClz and NaZCZ04 is shown in fig. 1. Reae- B.V. All rights reserved 494 O. Sohnel et al. / COM precipitation investigation by thermometric method vessels were different, liquid in the reference vessel had to be cooled or heated as appropriate. After equilibrating temperature of both vessels, i.e. a strictIy horizontal line on a plotter was recorded, precipitation was initiated by adding an identical volume of oxalate solution to both ves- :,.' ' '" . -== ..... ---- . ,. . ~.. '" ' .. ,. . '.., ' .• , -- ~. ~----- '1 ." ~ ". , z . ~--;:1- ". ---=--"":. J•• , , .~ ' - ----------_--:...---:..-----, , ------------. -' . - - Fig. 1. Cross section of isoperibolic reaction twin calorimeter. (1) reaction or reference vessel; (2) insulating body of calorimeter; (3) water jacket; (4) insulating cover; (5) syringe; (6) stirrer. tion and reference vessels (1) are situated in a therma11y insulating block of polystyrene foam which is placed inside a water jacket (3) thraugh which water of constant temperature is circulated. The water jacket is surraunded by a block of foam polystyrene (2), representing the body of the calorimeter. A vertica11y movable thermal insulating cover (4) contains mechanica11y coupled syringes (5), thermistors and stirrers (6). Thermistors are connected to a differential resistance bridge with an amplifier and its voltage output is recorded as a function of time by a compensating recorder. The reaction and reference vessels of 200 mI volume, each containing 100 mi of reference and calcium containing solution, respectively, were kept in a constant temperature water bath prior to each experiment for at least 30 mino Then they were quickly transferred into the calorimeter body, the cover tightIy closed, stirred and the bridge output recording begun. If a recorded line was inclined fram the base, ie. temperature in seis thraugh syringes. The temperature development in the reaction vessel was recorded for appraximately 10 min and then the experiment was terminated. Then a calibration determining the heat capacity of the reaction mixture, i.e. the heat required for a defined increase in the output voltage, was performed. This calibration enabled conversion to take place of the experimental voltage versus time curves, so-caBed progress curves, into the time development of heat evolved at precipitation. The reaction vessel, corresponding thermistor and stirrer were carefu11y cleaned in order to remove a11 adhered salid particles of COM, and then dried. Construction of an isoperibolic reaction twin calorimeter and the way of performing experiments were fu11y described in refs. [9,10]. Each experiment under certain reaction conditions was repeated several times. The result was a family of pragress curves corresponding to the same experimental conditions. 100 mi of the reference solution placed in the reference vessel always represented a solution of NH4CI of ionic strength 100 mol m-3. 100 mi of the reactant solution placed in the reaction vessel contained the required amount of 100 mol m-3 CaClz stock solution and an appropriate amount of NH4CI for adjusting the total solution ionic strength to 100 mol m -3. If the influence of admixtures was studied, the same amount of admixture, specifica11y phytic acid, sodium pyraphosphate or sodium citrate, was added to the solution in the reference and the reaction vessels. Then an appropriate volume, 2 to 5 mi, of 100 mol m -3 stock solution of sodium oxalate for achieving the stoichiometric conditions in the reaction vessel was added thraugh syringes to start the reaction. AlI experiments were performed at 25°C. The used chemicals of Analar grade were dissolved in distilIed water and the resulting solutions were filtered through a membrane filter O. Sohnel et al. / COM precipitation investigation by thermometric 495 method types of reactions. A model of a bimolecular autocatalytic reaction, A + B = 2B, with different initial concentrations of reactants, i.e. IV) T 2 mV 1 1 - exp [ - kt (b + a) 1 + a exp [W - kt ( b Os 100s (t) Fig. 2. Family of the progress, i.e. voltage versus time, curves for COM precipitation carried out at initial COM concentration of 2.439 mol m -3, 25°C and 1 = 100 mol m -3. before use. The same stock solutions were used for experiments carried out under identical conditions in order to eliminate any deviation caused by a possible difference in the composition of independentiy prepared stock solutions. 3. Results Two series of experiments were performed: the first series at different initial concentrations of COM without the presence of admixtures and the second series with solutions of the same initial concentration of COM, but containing different amounts of an admixture, specifically phytate, pyrophosphate or citrate. In both cases, the ionic strength of the reacting solution was adjusted to 100 mol m-3 with NH4Cl. A typical family of progress curves obtained from independent experiments with apure system, i.e. without an admixture present, performed at identical conditions, are shown in fig. 2. These experiments were well reproducible as to the precipitation rate and the reaction extent measured by the reaction enthalpy released at any selected time. However, for experiments carried out at low supersaturations (c¡ < 1.9 mol m -3), such reproducibilty was lost and individual progre ss curves differed substantially. These progress curves were fitted by a computer to give kinetic expressions corresponding to different ] + a) ]/ b ' (1) where ¡lU and ¡lUoo are the output voltages at time t and at infinity, respectively, a and b are the initial concentrations of the reactants and k is the kinetic constant, describes best the actual shape of the experimental curves. The total reaction enthalpy evolved on reaction completion, ¡lHoo, from the employed volume of reaction mixture was evaluated using eq. (1). The arithmetic average of individual values from independent experiments for each initial supersaturation studied, are given in table 1. The amount of solid, ns, precipitated from the actual volume of reaction mixture, determined as the difference between the initial and equilibrium total concentration of COM under experimental conditions, i.e. 25°C and 1= 100 mol m - 3, is also given in table 1. The latter concentration was calculated from the thermodynamic solubility product of COM, Ksp = 2.00 X 10-3 molz m-6 [11], valid for 1 = 100 mol m -3 and the thermodynamic association constant for ionic pairs of CaCZ04, K = 1.537 mol m-3 [12], as ceq = 0.123 mol m -3. The respective activity coefficient y:¡: = 0.3714 was calculated from the Davies extension of the Debye-Hlickel theory [13]. The last column in table 1 gives the molar reaction enthalpy, i.e. the change of enthalpy accompanying formation of 1 mol of COM, from ¡lit, Table 1 COM precipitation solution at different 1.961 2.439 2.913 3.846 4.762 at 25°C, 1 = 100 mol m -3 from initial concentration - ¡jHoo ns X 104 (mol) (J) - ¡jHoo/ns (kJ mol- 1) 1.874 2.373 2.873 3.872 4.871 3.38 4.00 4.78 6.98 8.74 18.0 16.9 16.6 18.0 17.9 ns represents the number of COM moles precipitated reaction completion in the respective experiment. pure at 496 (v!! O. Sohnel et al. / COM precipitation investigation by thermometric (iii) the average slope of the progress curve 10 s after induction period termination, mlO, and (iv) the difference between the maximum and minimum value of reaction enthalpy observed at a respective set of experiments after 100 s of reaction duration: iJ.IllOo T ZmV 1 8 = I HlOo(max) Os method 100s HlOo(min) l. (3) diluted aqueous solutions of CaClz and NaZCZ04 at 25°C and 1 = 100 mol m-3. The second series of experiments was designed for studying the admixture influence on COM precipitation. These experiments were performed with reaction mixture of initial concentration c¡ = 2.439 mol m -3 COM at 25°C and varying amount of impurity. A typical family of progress curves determined in individual experiments carried out under identical conditions are shown in fig. 3. Each family of progress curves were characterized by (i) the average induction period, i.e. time elapsed between the solution mixing and the onset of heat evolution, (ii) the arithmetic mean of determined values of reaction enthalpy evolved after 100 s from the induction period termination, are also quoted in table 2. The corresponding values for the reference state, i.e. characterization of progress curves produced by apure system of the same supersaturation, is also given in table 2. In all experiments crystals of characteristic COM shape were formed. 3. Discussion An isoperibolic reaction twin calorimeter proved to be a suitable and sensitive technique for studying spontaneous COM precipitation. Reproducibility of experimental progress curves determined for COM precipitation without impuri- Table 2 = 2.439 (2) These values are given in table 2. The standard deviation corresponding to each calculated value of iJ.HlOo, defined as (ti Fig. 3. Family of the progress (voltage versus time) curves for COM precipitation carried out at initial COM concentration of 2.439 mol m-3, 25°C, 1 = 100 mol m -3 and 0.732 mol m-3 sodium citrate. m 2.57 2.35 o0.66 1.86 2.08 1.50 2.77 2.59 0.050 2.73 0.066 3.74 0.133 0.065 0.067 .19 0.49 0.85 4.015 6.6 6.3 8.6 1.04 12 5I c 4.88 9.76 1.14 232.68 0.028 .69 0.56 81.95 1.28 1.61 0.44 4.01 0.083 0.035 0.046 .16 .13 0.79 o0.33 0.52 0.66 7.85 1254N 0.67 0.037 2.65 0.044 2.5 0.61 0.73 6.4 X 102(JS-I) 0.142 2.2 7.65 (J) a9.4 t20.8 100 I2.72 L1 (s) ¡¡lOa (J) COM precipitation at 2SOC, 1 = 100 mol m -3 and c¡ Impurity - mol m -3 in presence of impurities O. Sohnel et al. / COM precipitation ties was satisfactory (see fig. 2) if initial supersaturation exceeded a certain minimum value. Fig. 2 presents a family of very similar progress curves obtained in independent experiments carried out under identical conditions for apure system. The rather small difference 8 given on the first line in table 2 for systems without impurity confirms the close similarity of independent progress curves determined under identical conditions. The supersaturation range within which a precipitating system can be investigated by this method is limited. The lower limit is given by the requirement that a reasonable reaction extent must be reached within maximum 20 min beyond which the calorimeter is not thermally stable. The upper limit of supersaturation is determined by the promptness of the equipment response to a temperature change; if the heat evolution rate exceeds the response, any reliable kinetic curve cannot be obtained. The molar enthalpy of reaction + CaClz + HzO NazCz04 ~ CaCZ04• HzO(s) + 2 NaCl, carried out in dilute solutions of ionic strength 100 mol m -3, is given in table 1 as i1¡t,/ns, and is independent of solution initial supersaturation within the studied concentration range. The average molar reaction enthalpy was c~lculated from values quoted in table 1 as i1Hr = -17.5 kJ mol-I. The reaction enthalpy can also be determined from the standard formation enthalpies of products and reactants according to i1Hor= Lv¡Ho¡- Lv¡Ho¡, (4) p where p and r denote products and reactants. Inserting appropriate formation enthalpies, NazCzO/dil) - 1299.2 [14], CaClidil) - 873.2 [14], NaCl - 406.3 [14], Hz0(t') - 286.2 kJ mol-I [14] for 18°C and 1 atm and CaCZ04' HzO(s) 1673.6 kJ mol-I [15] valid for 25°C and 1 atm into Formation (4) yields i1Hor = -27.6 kJ mol-I. enthalpies denoted by (dil) apply to substances dissolved in infinitely diluted solutions, (t') and (s) correspond to liquid and solid state, respectively. investigation by thermometric method 497 The experimental average reaction enthalpy ( - 17.5 kJ mol- 1) is of a similar value as the quantity calculated from eq. (4) ( - 27.6 kJ mol-I). The calculated value is, however, to some extent unreliable due to the difference in reference temperature of the formation enthalpies (l8°C) and of the experiments (25°C) and al so due to uncertainty in the reported values of formation enthalpies. The formation enthalpies cannot even be brought to a common temperature, since the required heat capacities are not available. Taking into account these uncertainties, the correspondence between experimental and calculated values of reaction enthalpies can be considered as acceptable. A mathematical model of the autocatalytic reaction fits the experimental data well and also gives realistic values of the initial concentration of the reactants. Calculated and actual initial concentration of reactants compare well. These facts, howeverencouraging, cannot be overestimated since the model in question applies strictly to homogeneous reactions [8], whereas in our case a heterogeneous reaction takes place. Therefore, this model was used only for estimating the total reaction heat enthalpy, in which case it provided reliable results. Further conclusions inferred from close correspondence of mathematical model and experiment, mainly a dominating role of secondary nucleation under employedexperimental conditions, could not be considered as sufficiently safe. The studied impurities - phytate, pyrophosphate and citrate - induce induction period at COM precipitation (see table 2). This effect is generally more pronounced at higher concentration of impurity. The effectiveness of the impurity, estimated according to the concentration resulting in a similar duration of tind, increases in the succession citrate < pyrophosphate < phytate. The initial precipitation rate, a measure of which is mlO, is lowered by the studied impurities compared to the rate in apure system and decreases with increasing impurity concentration. The effectiveness of impurity in influencing the precipitation rate follows the same succession as given above. An interesting conclusion can be inferred from 498 O. Sohnel et al. / COM precipitation the observed spread of progress curves, expressed as 8 and u in table 2, determined from independent experiments carried out under identical conditions when precipitation takes place in the presence of impurities. This spread means that in independent, but identical, experiments, a different reaction extent is reached after the same time has elapsed from the reaction start-up. The same effect is illustrated in fig. 3 by dissimilar shape and height of individual progress curves. It contrasts with experiments in apure system where the reaction extent is similar at any time. Such behaviour indicates somewhat "random" influence of impurities on spontaneous precipitation. An acceptable explanation of this observation cannot be suggested at presento 4. Conclusions An isoperibolic twin reaction calorimeter represents a convenient and reliable technique for studying spontaneous crystallization of sparingly soluble substances. The resulting progre ss curves of precipitation, i.e. time dependence of heat evolved due to precipitation, are highly reproducible. Precipitation of COM from diluted aqueous solution is retarded by the studied impurities, compared to apure system. The effectiveness of impurities in influencing precipitation increases in the succession citrate < pyrophosphate < phytate. The studied impurities affect sponta- investigation by thermometric method neous precipitation of COM carried out under the same conditions in a "random" way, that is, independently performed experiments are influenced to a different degree by the same amount of an identical impurity. References [1] Lj. Brecevic, o. Skrtié and J. Garside, J. Crystal Growth 74 (1986) 399. [2] F. Grases and A. Costa-Bauzá, Clin. Chem. Enzym. Commun. 3 (1991) 319. [3] O. Skrtié and N. Filipovié-Vincekovié, J. Crystal Growth 88 (1988) 313. [4] J.O. OeLong and O. Briedis, J. Crystal Growth 71 (1985) 689. [5] M.E. Sheehan and G.H. Nancollas, lnvest. Urol. 17 (1980) 446. [6] V. Velich and F. Stehlík, J. Thermal Anal. 24 (1982) 299. [7] V. Velich and V. Olask, Oyes and Pigments 6 (1985) 445. [8] V. Velich, M. Jánosová and H. Malíková, Oyes and Pigments 12 (1990) 63. [9] V. Velich, F. Oittrich, J. Timar and Z. Kraus, Chem.Listy 79 (1985) 661. [10] V. Velich, P. Petr and R. Severa, Chem.Lísty 84 (1990) 202. [11] G.H. Nancollas and G.L. Gardner, J. Crystal Growth 21 (1974) 267. [12] B. Tomazié and G.H. Nancollas, J.Crystal Growth 46 (1979) 355. [13] G.H. Nancollas, lnteractions in Electrolyte Solutions (Elsevier, Amsterdam, 1966) [14] International Critical Tables, Vol. V (McGraw-HiIl, New York, 1929) p. 197. [15] Landolt-Bornstein, Zahlenwerte und Funktionen, 6. Auflage, 11. Band, 4. Teil (Springer, Berlín, 1961).
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