Ultrasonics Sonochemistry 8 (2001) 175±181 www.elsevier.nl/locate/ultsonch Preliminary results on the eect of power ultrasound on nitrogen oxide and dioxide atmosphere in nitric acid solutions Ph. Moisy *, I. Bisel, F. Genvo, F. Rey-Gaurez, L. Venault, P. Blanc Commissariat aÁ l'EÂnergie Atomique (CEA/Valrh^o), DRCP/SCPS/LPCA, BP 17171, 30207 Bagnols-sur-CeÁze Cedex, France Abstract The eect of ultrasound (20 kHz, 3 W cm 2 ) on the kinetics of HNO2 and H2 O2 formation was investigated in a 1 M HNO3 medium for NO2 ±Ar and NO±Ar gas mixtures in various volume fractions (f NO2 < 1:7 vol% and f NO < 1:1 vol%, respectively). The H2 O2 formation rate measured in 1 M HNO3 in the presence of N2 H5 NO3 was observed to be much lower than that of HNO2 without N2 H5 NO3 , and was relatively independent of the NO2 or NO gas volume fractions in the argon atmosphere. The HNO2 formation rate increased under ultrasound, and was higher with NO than with NO2 . The induction period observed without ultrasound disappeared when ultrasound was applied. The ®rst step in the sonochemical mechanism of HNO2 formation in the presence of NO2 involves thermal decomposition of NO2 into NO within the cavitation bubble. In the second step of HNO2 formation, NO reacts either with HNO3 in the cavitation bubble, or with NO2 in the cavitation bubble or at the bubble/solution interface. Ó 2001 Elsevier Science B.V. All rights reserved. Keywords: Ultrasound; Nitrous acid; Nitrogen oxide; Nitrogen dioxide 1. Introduction Ultrasound has been successfully used over the last two decades in a wide range of applied research ®elds [1± 4], including organic synthesis and catalysis, preparation of structured materials, surface depassivation and electroanalysis, and environmental applications. Few reports, however, have discussed the advantages of ultrasound for converting chemically active gases for liquid-phase reactions: most published work concerning the eects of ultrasound according to the gas composition was carried out for fundamental research [5,6]. The investigations have focused primarily on the noble gases (He, Ne, Ar, Kr, Xe) or on the macro-constituents of air (O2 and N2 ) in aqueous media (generally water) when submitted to ultrasound. While the properties of gases under ultrasound are suitably represented by the ratio of their heat capacities c Cp =Cv and by their thermal conductivity C, those of the chemically active gases require a more complex approach [7,8]. Dierent isotopes have been used [5,6] during sonolysis of water to describe the role of the gaseous compounds O2 , H2 and * Corresponding author. Tel.: +33-466-791-611; fax: +33-466-796567. E-mail address: [email protected] (Ph. Moisy). N2 in the formation of H2 O2 , NO2 and NO3 in solution and of gaseous NO, NO2 and N2 O. Although the eect of N2 O during sonolysis of water has not been widely investigated [9], sonolysis has been observed to form N2 and O2 at a maximum rate for a N2 O volume fraction of about 15% in Ar; H2 O2 , NO2 and traces of NO3 tend to accumulate in solution according to a decomposition mechanism (Eqs. (1) and (2)) [9]: 2N2 O ! 2N2 O2 1 3N2 O H2 O ! 2HNO2 2N2 2 The absence of H2 formation and the decreasing rate of H2 O2 formation are justi®ed [9] by the fast kinetics of the reactions between OH or H and N2 O (Eqs. (3) and (4)): H N2 O ! N2 OH 3 OH N2 O ! 2NO H 4 The maximum rate obtained with the N2 O volume fraction f N2 O 15% is explained by the bubble temperature drop when the N2 O concentration increases in the argon [9]. To the best of our knowledge, the eect of ultrasound on NO and NO2 diluted in a noble gas has not been investigated. 1350-4177/01/$ - see front matter Ó 2001 Elsevier Science B.V. All rights reserved. PII: S 1 3 5 0 - 4 1 7 7 ( 0 1 ) 0 0 0 7 5 - X 176 Ph. Moisy et al. / Ultrasonics Sonochemistry 8 (2001) 175±181 The purpose of this preliminary study is to observe the eect of ultrasound on gaseous mixtures of argon and nitrogen oxides (NO and NO2 ) in a nitric acid medium. NO and NO2 transfers by sparging in nitric acid are known to result in the accumulation of HNO2 in solution. 2. Experimental All the chemical reactants were analysis grade as supplied by Prolabo and Merck, and were used without additional puri®cation. Deionized water (Milli-Q/RO System) was used to prepare the aqueous solutions. The gases and initial gaseous mixtures (Ar, Ar 15% NO, and Ar 5% NO2 ) were supplied by Air Products (Ar 55). The gaseous mixtures characterized by their volume percentage fraction (f(X)) were prepared from pure argon and the initial NOx ±Ar mixtures. The solubility of Ar and NO were estimated at 5.4 and 7.4 ml in 100 ml of water at 0°C [10]. The heat capacity ratios c Cp =Cv were 1.68 for Ar, 1.4 for NO and 1.3 for NO2 . The thermal conductivity values (C: 106 cal cm 1 K 1 s 1 ) were 39.1 for Ar, 56.2 for NO and 400.6 for NO2 [10]. The experiments were performed with a thermostatically controlled batch sonoreactor equipped with an 18 cm2 piezoelectric transducer supplied by a 20 kHz generator (VibraCell 600). The transducer was secured to the bottom of the glass sonoreactor by a watertight PTFE coupling ring. The solution volume subjected to ultrasound was 100 ml. The temperature in the reactor was measured by a thermocouple immersed approximately 3 cm below the surface. Preliminary tests showed that the solution temperature reached a constant value about 10 min after the sonolysis began. The temperature was maintained constant at 25°C for all the experiments by a thermo-cryostat (Huber Unistat Tango). Gas was supplied via a glass tube immersed in the solution, and tipped with glass frit capable of forming very ®ne gas bubbles at a rate of 140 ml min 1 . The solution was saturated with Ar about 30 min before initiating the sonolysis with appropriate gas. Preliminary tests con®rmed that the gas bubbling system considerably modi®ed the chemical kinetics of the system [4]. With a constant gas ¯ow rate and ultrasonic intensity, for example, the H2 O2 sonochemical formation rate in 1 M HNO3 in the presence of 0.1 M N2 H5 NO3 was about 5:4 0:1 lM min 1 when Ar was introduced through a ®ne glass tube ®xed at the surface of the solution, about 6:7 0:1 lM min 1 when the same ®ne glass tube was immersed in the solution, and about 7:5 0:2 lM min 1 with a glass tube ®tted with a glass frit tip and immersed in the solution. The gas was removed from the leaktight sonoreactor through a glass tube extending directly to the exterior. The use of a chemical trap in the reactor outlet line (sparging at a depth of about 10 cm of solution) considerably modi®ed the chemical kinetics, probably as a result of the pressure imposed in the sonoreactor by the solution head in the chemical trap. The acoustic power (W) transmitted to the system was measured by calorimetry [11]. The ultrasonic intensity (W cm 2 ) transmitted to the solution was calculated from the P =S ratio, where S is the transducer surface area (18 cm2 ). All the experiments were conducted at a constant intensity of 3 W cm 1 (P 54 W). Solution samples were taken during sonolysis without allowing air into the medium. The sample volumes were small, and can be considered negligible compared with the initial solution volume. The samples were analyzed immediately. HNO2 was monitored by initially stabilizing the samples (as NO2 ) after mixing with 1 M sodium hydroxide; the HNO2 concentration was determined by spectrophotometry (Shimadzu 3101 UVPC) by the Griess method (k 530 nm; e 42 000 cm 1 M 1 ) [12]. The H2 O2 concentration in the HNO3 medium in the presence of N2 H5 NO3 was determined by spectrophotometry by the Ti(IV) method in 0.5 M sulfuric acid (k 410 nm; e 600 cm 1 M 1 ) [12]. Under these conditions no interference was observed from nitrate ions for a 1 M nitric acid concentration in the sample. 3. Results 3.1. Sonolysis of NO2 ±Ar mixtures Fig. 1 shows the evolution of the HNO2 concentration in solution during sonolysis (I 3 W cm 2 ) of a 1 M nitric acid solution saturated by a gaseous mixture of argon and NO2 (0, 0.6, 0.9, 1.3 and 1.7 vol%). The HNO2 concentration in solution increased over time to a steady-state value due (as shown in a previous study [11,13]) to the identical rates of HNO2 formation and destruction. The slope of the linear HNO2 concentration variation in solution at t 0 is used (Eq. (5)) to estimate 2 the HNO2 formation rate xHNO meas . The results (Table 1) indicate that the kinetics of HNO2 formation increase with the NO2 volume fraction. 2 xHNO meas d HNO2 kfHNO2 dt 5 In order to take into account the rapid consumption of HNO2 by hydrogen peroxide (Eq. (6)) formed under ultrasound [11,13], the sonochemical H2 O2 formation 2 O2 rate xH meas was determined in the HNO3 medium in the presence of 0.1 M N2 H5 NO3 [14]. HNO2 H2 O2 ! HNO3 H2 O 6 Adding N2 H5 NO3 at an initial concentration of 0.1 M allowed H2 O2 to accumulate in solution, considering the rapid decomposition kinetics of HNO2 [15]. Under Ph. Moisy et al. / Ultrasonics Sonochemistry 8 (2001) 175±181 177 In order to discriminate between the eects of ultrasound and of simple sparging, the formation kinetics of HNO2 in 1 M HNO3 were observed under the same 2 conditions xHNO chem , but without ultrasound (Fig. 1b). Contrary to the results obtained with ultrasound, the kinetic law of HNO2 formation (Table 1) depended on the NO2 volume fraction. With a NO2 concentration above 1.3 vol%, the HNO2 formation kinetics estimated from the slope at t 0 were identical with those observed under ultrasound. With lower NO2 volume fractions (0.6 and 0.9 vol%) the rate of HNO2 formation in solution exhibited an initial induction phase, then accelerated. Regardless of the NO2 volume fraction, however, a steady-state HNO2 concentration was reached in solution. These results can than be used to calculate the total HNO2 concentration ([HNO2 ]T ) (Eq. (8)) and the HNO2 concentration formed under the eect of ultrasound alone ([HNO2 ]US ) (Eq. (9)). Fig. 1. (a) HNO2 concentration versus time in HNO3 (1 M; 25°C) with ultrasound (20 kHz; 3 W cm 2 ) under NO2 ±Ar atmosphere (140 ml min 1 ): (1) f NO2 1:7 vol%; (2) f NO2 1:3 vol%; (3) f NO2 0:9 vol%; (4) f NO2 0:6 vol%; (5) f NO2 0 vol% and (b) HNO2 concentration versus time in HNO3 (1 M; 25°C) without ultrasound under NO2 ±Ar atmosphere (140 ml min 1 ): (1) f NO2 1:7 vol%; (2) f NO2 1:3 vol%; (3) f NO2 0:9 vol%; (4) f NO2 0:6 vol%. these conditions, the H2 O2 concentration has been observed to increase in a linear manner with time, regardless of the NO2 volume fraction. The results (Table 1) can then be used (Eq. (7)) to calculate the total HNO2 2 formation rate xHNO for a given volume fraction: T H 2 O2 2 2 xHNO xHNO T meas xmeas 7 HNO2 T HNO2 meas H2 O2 meas 8 HNO2 US HNO2 T 9 HNO2 chem Fig. 2 shows the variation over time of the HNO2 concentration due to sonolysis of 1 M HNO3 with a NO2 volume fraction of 0.6% ([HNO2 ]meas ); the H2 O2 concentration obtained under identical sonochemical conditions in the presence of N2 H5 NO3 ([H2 O2 ]meas ); the HNO2 concentration obtained chemically by sparging 0.6 vol% NO2 without ultrasound ([HNO2 ]chem ); and the HNO2 concentration ([HNO2 ]US ) formed under the effect of ultrasound alone (calculated from Eq. (9)). This ®gure shows that the induction period observed during NO2 sparging without ultrasound is no longer observed with ultrasound, and that the HNO2 formation rate is higher with ultrasound. It is dicult to compare the steady-state HNO2 concentrations obtained with and without ultrasound, as the duration of the experiments was not sucient to reach a steady-state value without ultrasound. Moreover, H2 O2 was formed at a much lower rate than HNO2 with ultrasound. The variation of the HNO2 concentration formed with ultrasound alone (Eq. (9)) appears to be much greater than without ultrasound. Fig. 3 indicates the HNO2 concentration variation actually due to the eect of ultrasound alone (calculated Table 1 2 O2 Kinetic constants of formation of H2 O2 and HNO2 in HNO3 (1 M; 25°C) under NO2 ±Ar atmosphere (140 ml min 1 ) with ultrasound (xH meas and 2 , respectively) and without ultrasound (xHNO2 ) xHNO chem meas f(NO2 ) (% vol in Ar) 2 xHNO meas lmol l 0 0.6 0.9 1.3 1.7 7:7 0:4 65 3 59 2 120 5 165 5 1 min 1 ) 2 O2 xH meas lmol l 7:5 0:2 6:5 0:1 5:8 0:2 5:2 0:4 5:1 0:4 1 min 1 ) 2 xHNO chem l mol l 1 0 Induction period Induction period 110 2 140 3 min 1 ) 178 Ph. Moisy et al. / Ultrasonics Sonochemistry 8 (2001) 175±181 3.2. Sonolysis of NO±Ar mixtures Fig. 2. HNO2 concentration versus time in HNO3 (1 M; 25°C) under NO2 ±Ar atmosphere (f NO2 0:6 vol%; 140 ml min 1 ): (1) with ultrasound (20 kHz; 3 W cm 2 ); (2) without ultrasound; (3) under the eect of ultrasound alone, calculated from Eq. (9); (4) H2 O2 concentration versus time in HNO3 (1 M) N2 H5 NO3 (0.1 M) under NO2 ± Ar atmosphere (f NO2 0:6 vol%; 140 ml min 1 ). Fig. 4a shows the evolution of the HNO2 concentration during sonolysis (I 3 W cm 2 ) of a nitric acid solution (1 M) saturated with a gaseous mixture of argon and NO (0, 0.3, 0.6 and 1.1 vol%). As with the NO2 ±Ar mixtures, the linear HNO2 concentration variation at t 0 can be used to determine the HNO2 formation kinetics (Table 2). For 0.3 vol% NO, the HNO2 formation kinetics diered only slightly from those observed during sonolysis of HNO3 (1 M) under pure argon. A steady-state HNO2 concentration in solution was obtained for all three NO volume fractions. The H2 O2 concentration was monitored in 1 M HNO3 (in the presence of 0.1 M N2 H5 NO3 ) to determine the sonochemical formation kinetics of H2 O2 according to the NO volume fraction (Table 2). As with the NO2 ±Ar mixtures, the H2 O2 formation rate diminished very slightly with the NO volume fraction. Fig. 3. HNO2 concentration versus time in HNO3 (1 M; 25°C) under NO2 ±Ar atmosphere (140 ml min 1 ) with the eect of ultrasound alone, calculated from Eq. (9): (1) f NO2 1:7 vol%; (2) f NO2 1:3 vol%; (3) f NO2 0:9 vol%; (4) f NO2 0:6 vol%; (5) f NO2 0 vol%. from Eq. (9)) versus the NO2 volume fraction. The results show that for a volume fraction exceeding 1.3%, ultrasound does not enhance the kinetics of HNO2 formation in solution or the steady-state HNO2 concentration above the values obtained by simple gas sparging. The fact that the steady-state concentrations were approximately the same with or without ultrasound shows that the HNO2 decomposition rate is the same. For volume fractions below 1.3%, ultrasound has an appreciable eect and the HNO2 formation rate is signi®cantly higher than without ultrasound. It may be noted that the rates obtained were signi®cantly higher than measured during sonolysis (3 W cm 2 ) of a nitric acid solution (1 M) under pure argon atmosphere (Table 1). Fig. 4. (a) HNO2 concentration versus time in HNO3 (1 M; 25°C) with ultrasound (20 kHz; 3 W cm 2 ) under NO±Ar atmosphere (140 ml min 1 ): (1) f NO 1:1 vol%; (2) f NO 0:6 vol%; (3) f NO 0:3 vol%; (4) f NO 0 vol% and (b) HNO2 concentration versus time in HNO3 (1 M; 25°C) without ultrasound under NO±Ar atmosphere (140 ml min 1 ): (1) f NO 1:1 vol%; (2) f NO 0:6 vol%. Ph. Moisy et al. / Ultrasonics Sonochemistry 8 (2001) 175±181 179 Table 2 2 O2 Kinetic constants of formation of H2 O2 and HNO2 in HNO3 (1 M; 25°C) under NO±Ar atmosphere (140 ml min 1 ) with ultrasound (xH meas and 2 , respectively) and without ultrasound (xHNO2 ) xHNO chem meas f NO % vol in Ar 2 xHNO meas l mol l 0 0.3 0.6 1.1 7:7 0:4 72 93 9 125 7 1 min 1 Fig. 4b shows the evolution of the HNO2 concentration in 1 M HNO3 under NO±Ar atmosphere without ultrasound. In the case of a 1.1% volume fraction, the initial formation kinetics was determined from the linear HNO2 concentration variation over time. With lower volume fractions, however, the formation kinetics could not be accurately determined either because of the initial induction period (0.6 vol% NO) or the very low HNO2 accumulation rate (0.3 vol% NO). The calculated results (Table 2) show that without ultrasound the HNO2 formation kinetics are slower and the steady-state concentrations lower in the presence of NO than for NO2 . Fig. 5 shows the HNO2 concentration variation calculated from Eq. (9) ± i.e. actually formed under the eect of ultrasound alone ± versus the NO volume fraction: for 0, 0.6 and 1.1 vol% NO, ultrasound enhanced the HNO2 formation kinetics and the steadystate concentration in solution compared with the results obtained by simple sparging of the gas mixture. As with NO2 ±Ar mixtures, the rates obtained were signi®cantly higher than those measured during sonolysis (3 W cm 2 ) of a nitric acid solution (1 M) under pure argon atmosphere. An induction period was again observed with ultrasound for the 0.6% volume fraction. For the 0.3% volume fraction it is dicult to discuss the results for several reasons: (1) the low HNO2 concentration accumulated with ultrasound (on the same order of magnitude as with pure argon); (2) the H2 O2 accumu- Fig. 5. HNO2 concentration versus time in HNO3 (1 M; 25°C) under NO±Ar atmosphere (140 ml min 1 ) with the eect of ultrasound alone, calculated from Eq. (9): (1) f NO 1:1 vol%; (2) f NO 0:6 vol%; (3) f NO 0 vol%. 2 O2 xH meas lmol l 1 min 1 7:5 0:2 6:1 0:3 4:1 0:1 4:0 0:1 2 xHNO chem l mol l 1 min 1 0 Induction period Induction period 64 1 lation was comparable to that of HNO2 ; (3) the chemical accumulation of HNO2 by simple sparging was very low. Comparing the HNO2 concentrations versus the NO2 and NO volume fractions (Figs. 3 and 5) shows that with ultrasound the HNO2 concentration was much higher in the presence of NO than of NO2 , unlike the behavior observed without ultrasound. 4. Discussion Numerous parameters have already been identi®ed as important for controlling the eect of ultrasound; the speci®c heat ratio c, thermal conductivity C and gas solubility are particularly important in controlling the gaseous atmosphere. Considering the minor changes in the speci®c heat ratio c and the thermal conductivity C with NO and NO2 volume fractions well below 2% in argon, the eect of ultrasound is probably chemical in nature. It may thus be assumed that the temperature in the cavitation bubble and the ultrasonic intensity are similar to those obtained under pure argon. The problems encountered in determining the gas solubility under the eect of ultrasound, particularly for NO and NO2 make it impossible to predict the role of this parameter in the observed phenomenon, however, although these gases are poorly soluble in aqueous media, and the solubility diminishes as the temperature rises. The solubility of argon in water typically diminishes from 5.4 ml per 100 ml at 0°C to 4.5 ml at 25°C and 3.0 ml at 50°C. Moreover, it has been established [16] in the case of NO2 that the dimerization equilibrium results in the formation of N2 O4 (Eq. (10)), for which the solubility in the aqueous phase is too low to measure. This low solubility is generally attributed [17] to dismutation of N2 O4 into HNO2 and HNO3 (Eq. (11)). 2NO2 $ N2 O4 10 N2 O4 H2 O $ HNO2 HNO3 11 The equilibrium and kinetic constants are K 10 6:54 f 104 l mol 1 and k 10 4:5 108 l mol 1 s 1 at 25°C for the NO2 dimerization equilibrium [16], and K 11 f 3:33 1011 mol l 1 and k 11 1:7 1010 l mol 1 s 1 for the N2 O4 dismutation reaction [17]. NO2 is completely dimerized in the gaseous phase considering the high f equilibrium constant: K 10 6:84 atm 1 at 25°C [18]. 180 Ph. Moisy et al. / Ultrasonics Sonochemistry 8 (2001) 175±181 Considering the weakness of the N2 O4 bond, however, NO2 is probably monomeric in the hot cavitation bubble. Although it is dicult to predict the impact of the gas solubility on the ultrasonic eect, the temperature in the cavitation bubble and the ultrasonic intensity are thus probably the same as observed under argon atmosphere. It is currently acknowledged [7,8] that the two principal mechanisms accounting for the sonochemical phenomena observed in aqueous solution are a radical mechanisms involving the primary radicals OH and H , and a thermolysis mechanisms inside the cavitation bubble or at the bubble/solution interface. The fact that the HNO2 formation and decomposition kinetics are unchanged for NO2 volume fractions exceeding 1.3% in Ar with and without ultrasound (Fig. 3) shows that the mechanism probably consists in the generally accepted reactions (Eqs. (10) and (11)) for HNO2 formation, and Eq. (12) for its decomposition [11]. Another possible mechanism corresponds to the absorption of N2 O3 (Eq. (16)) formed from NO2 and NO (formed in the cavitation bubbles) to yield HNO2 (Eqs. (17) and (18)): NO NO2 $ N2 O3 16 N2 O3 H2 O $ 2HNO2 17 NO NO2 H2 O $ 2HNO2 18 The equilibrium constant of Eq. (16) and of the overall reaction (Eq. (18)), and the kinetic constants [23,24] at f 25°C are: K 16 5 104 l mol 1 , k 16 1:1 109 1 1 l mol s , and K 18 HNO2 2 1 107 l mol NONO2 1 dNO dNO2 k f H2 ONONO2 dt dt k b HNO2 2 12 19 In the case of lower NO2 volume fractions, however, ultrasound appears to accelerate the HNO2 formation rate (Fig. 3) ± probably due to thermolysis of NO2 in the cavitation bubble (Eq. (13)), where temperatures exceeding 1000°C are reached. NO2 is known to be totally decomposed at temperatures above 620°C [19]. where k f H2 O 106 l mol 1 s 1 and k b 9:51 l mol 1 s 1 . Considering the complexity of the equilibria involved, and of the redox chemistry of nitrogen, it is dicult to favor one mechanism over the other to account for the results obtained in NO2 ±Ar atmosphere. However, HNO3 reduction by NO in the cavitation bubble (Eq. (14)) appears the most likely mechanism to explain the results observed under NO atmosphere: NO2 is formed only by decomposition of HNO2 (just before the steady state), since the equilibrium constant (Eq. (20)) is very low [25] in 2 M HNO3 at 25°C (K 20 2HNO2 ! NO NO2 H2 O 2NO2 ! 2NO O2 13 Under these conditions ± small amounts of NO2 and NO (production in the cavitation bubbles), several probable mechanisms can account for the HNO2 formation kinetics with small NO2 volume fractions. One possible mechanism involves the reduction of HNO3 by the NO formed in the cavitation bubbles (Eq. (14)): 2NO HNO3 H2 O $ 3HNO3 14 The equilibrium constant has been estimated [17,18, 20] at about K 14 3:3 10 2 atm 2 mol 1 l 2 (ambient temperature). The kinetic law (Eq. (15)) established by Abel and Schmidt [17] indicates the existence of an autocatalytic phenomenon by nitrous acid: dHNO2 k f HNO2 H NO3 dt kb HNO2 4 2 PNO 15 where k f 1:6 l2 mol 2 min 1 and k b 46 l3 mol 3 min 1 . While this reaction is slow at room temperature, quantitative NO absorption has been observed at temperatures above 60°C [21]. Moreover, work by Knox and Reid [22] showed that a sustained high NO concentration shifts the equilibrium considerably toward the formation of HNO2 . Moreover, the volatility of undissociated nitric acid [11,13] is likely to allow HNO3 to accumulate in the cavitation bubbles, capable of reacting with NO. 3 PNO a H2 O a HNO 2 1:64 10 3 with the acidity. 2 PNO 8 atm2 mol NO 2HNO3 $ 3NO2 H2 O 1 l) and diminishes 20 The mechanisms of HNO3 reduction by NO formed in the cavitation bubbles (Eq. (14)) is capable of accounting for the induction phase (by an autocatalytic mechanism as per Eq. (15)) and for the higher steadystate HNO2 concentration following the rise in the NO concentration in the cavitation bubble compared with the result obtained without ultrasound. Given the similar steady-state HNO2 concentrations with and without ultrasound in NO2 atmosphere, and the increased steady-state concentration in NO atmosphere, oxidation of HNO2 (Eq. (21)) by the O2 formed according to Eq. (13) is probably negligible. No experimental study known to us has yet determined the kinetics of this reaction, and it is thus dicult to substantiate this hypothesis. 2HNO2 O2 $ 2HNO3 21 The main eect of ultrasound is thus probably the thermolysis of NO2 , leading to the formation of NO. Ph. Moisy et al. / Ultrasonics Sonochemistry 8 (2001) 175±181 The NO formed in the cavitation bubble can thus reduce the HNO3 contained in the bubble or at the bubble/solution interface to form nitrous acid. As this reaction is catalyzed by HNO2 , an induction period is observed at low HNO2 concentrations. Additional work will be required to con®rm the mechanism of HNO3 reduction by NO, and to assess its importance compared with the N2 O3 absorption mechanism. Moreover, in view of the slight drop in the rate of H2 O2 formation depending on the NO2 volume fraction (0±1.7 vol%) and of the NO volume fraction (0±1.1 vol%) in the argon, the scavenging power of NO2 and NO appears to be low with respect to the free radicals (OH and H ) released by homolytic decomposition of water and nitric acid (Eqs. (22)±(24)) [11]. H2 O ! OH H HNO3 ! OH NO2 HNO3 ! H NO3 22 23 24 It should also be noted (Fig. 2, Tables 1 and 2) that the order of magnitude of the H2 O2 formation rate is considerably lower than the HNO2 formation rate by the eect of ultrasound alone, as calculated from Eq. (9) under NO and NO2 atmosphere. It has also been observed during sonolysis of a nitric acid solution in the presence of hydrazinium nitrate (which acts as an HNO2 and NO2 scavenger) [14], that the H2 O2 formation rate is independent of the nitric acid concentration (1 < HNO3 < 6 M) and is signi®cantly lower than for HNO2 . For example, the H2 O2 formation rate was estimated at about 12 lM min 1 in a 6 M HNO3 medium, while the HNO2 formation rate under the same conditions is about 126 lM min 1 [14]. The HNO2 formation mechanism under NOx atmosphere involving the free radicals released by homolytic decomposition of water and nitric acid is probably a minor contributor. 5. Conclusion An investigation of the formation of HNO2 in a 1 M HNO3 medium for various NO±Ar and NO2 ±Ar gas mixtures with ultrasound revealed the following phenomena: (1) The rate of HNO2 formation was signi®cantly increased by ultrasound for NO and NO2 volume fractions below 1%. The induction period observed without ultrasound for such low NO2 volume fractions disappeared under the eect of ultrasound. (2) With ultrasound, the HNO2 formation rate was higher under NO±Ar than under NO2 ±Ar atmosphere, contrary to the behavior observed without ultrasound. 181 The rates increased with the NO and NO2 volume fractions diluted in the argon under these experimental conditions: f NO2 < 1:7 vol% and f NO < 1:1 vol%. (3) The ®rst step in the sonochemical (20 kHz) mechanism of HNO2 formation in HNO3 (1 M) under NO2 ±Ar atmosphere (<1 vol% NO2 ) involves thermal decomposition of NO2 into NO within the cavitation bubble. The second step appears to be similar to the phenomenon that occurs in NO±Ar atmosphere, and corresponds either to reduction of HNO3 by NO in the cavitation bubble, or to hydrolysis of N2 O3 (formed from NO and NO2 ) in the cavitation bubble or at the bubble/solution interface. References [1] J.L. Luche, Synthetic Organic Sonochemistry, Plenum Press, New York, 1998. [2] K.S. Suslick, M.M. Fang, T. Hyeon, M.M. Mdleleni, Sonochemistry and Sonoluminescence, series C, Vol. 524, NATO ASI Series, Kluwer, London, 1999, pp. 291±320. [3] Proceedings Second Conf. Appl. Power Ultrasound Phys. Chem. Process., Toulouse, France, 6±7 May, 1999. [4] Advances in Sonochemistry, JAI Press Inc., London, 1 (1990), 2 (1991), 3 (1993), 4 (1996), 5 (1999). [5] C. Von Sonntag, G. Mark, A. Tauber, H.P. Schuchmann, Advances in Sonochemistry, Vol. 5, JAI Press Inc., London, 1999, pp. 109±45. [6] A. Henglein, Advances in Sonochemistry, Vol. 3, JAI Press Inc., London, 1993, pp. 17±83. [7] T.J. Mason, The Uses of Ultrasound in Chemistry, Royal Society of Chemistry, Cambridge, 1990. [8] T.J. Mason, J.P. Lorimer, Sonochemistry: Theory, Applications and Uses of Ultrasound in Chemistry, Ellis Horwood Series, Ellis Horwood, Chichester, 1988. [9] E.J. Hart, A. Henglein, J. Phys. Chem. 90 (1986) 5992. [10] Air Liquide, Encyclopedie des gaz, Elsevier, Amsterdam, 1976 (in French). [11] L. Venault, Ph. Moisy, S.I. Nikitenko, C. Madic, Ultrason. Sonochem. 4 (1997) 195. [12] G. Charlot, Chimie Analytique Quantitative, Masson, Paris, 1974 (in French). [13] S.I. Nikitenko, Ph. Moisy, L. Venault, C. Madic, Ultrason. Sonochem. 7 (2000) 135. [14] L. Venault, Ph. Moisy, P. Blanc, C. Madic, Ultrason. Sonochem. (2001), in press. [15] J.R. Perrot, G. Stedman, N. Uysal, Dalton Trans. (1976) 2058. [16] M. Graetzel, S. Tanigushi, A. Henglein, Ber. Bunseng Chem. 74 (1970) 488. [17] E. Abel, H. Schmidt, Z. Phys. Chem. 136 (1928) 430. [18] M. Graetzel, A. Henglein, J. Lilie, G. Beck, Ber. Bunseng Chem. 73 (1969) 646. [19] J.W. Mellor, A Comprehensive Treatise on Inorganic and Theoretical Chemistry, Longman, Harlow, 1958. [20] M. Graetzel, A. Henglein, S. Tanigushi, Ber. Bunseng Chem. 74 (1970) 292. [21] E. Vialard, Ph.D. Thesis, Paris VI, 1979 (in French). [22] J. Knox, D.M. Reid, J. Soc. Chem. Ind. 38 (1919) 105. [23] A. Treinin, E. Hanon, J. Am. Chem. Soc. 92 (1970) 5821. [24] A. Maschka, Mh. Chem. 84 (1953) 853. [25] P. Pascal, Nouveau traite de chimie minerale, Masson, Paris, 1956 (in French).
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