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Sonochemical processes

Ultrasound can thus be used to enhance kinetics, flow, and mass and heat transfer. The overall results are that organic synthetic reactions show increased rate (sometimes even from hours to minutes, up to 25 times faster), and/or increased yield (tens of percentages, sometimes even starting from 0% yield in nonsonicated conditions). In multiphase systems, gas-liquid and solid-liquid mass transfer has been observed to increase by 5- and 20-fold, respectively [35]. Membrane fluxes have been enhanced by up to a factor of 8 [56]. Despite these results, use of acoustics, and ultrasound in particular, in chemical industry is mainly limited to the fields of cleaning and decontamination [55]. One of the main barriers to industrial application of sonochemical processes is control and scale-up of ultrasound concepts into operable processes. Therefore, a better understanding is required of the relation between a cavitation coUapse and chemical reactivity, as weU as a better understanding and reproducibility of the influence of various design and operational parameters on the cavitation process. Also, rehable mathematical models and scale-up procedures need to be developed [35, 54, 55]. [Pg.298]

Okitsu K, Yue A, Tanabe S, Matsumoto H (2002) Formation of palladium nanoclusters on Y-zeolite via a sonochemical process and conventional methods. Bull Chem Soc Jpn 75 449 155... [Pg.150]

Novel single, double and triple doped ZnA O M and ZnGa204 M (where M = Dy3+, Tb3+, Eu3+ and Mn2+) nanophosphors were also synthesized through a simple sonochemical process [42]. [Pg.201]

Yadav RS, Mishra P, Mishra R, Kumar M, Pandey AC (2010) Growth mechanism and optical property of CdS nanoparticles synthesised using amino-acid histidine as chelating agent under sonochemical process. Ultrason Sonochem 17 116-122... [Pg.211]

SL thermometry) exhibiting a strong dependence on thermal conductivity, the more spatially and temporally averaged temperature (from the MRR method), which is more representative for sonochemical processes, does not show such dependence. It is probable that it is actually the water vapour content within the bubble not the gas itself that dictates the bubble temperature. [Pg.371]

CuPB NPs produced by the sonochemical process may have an excess of negative charge above that available by K dissociation. [Pg.191]

Romanian scientists compared one-electron transfer reactions from triphenylmethyl or 2-methyl benzoyl chloride to nitrobenzene in thermal (210°C) conditions and on ultrasonic stimulation at 50°C (lancu et al. 1992, Vinatoru et al. 1994, Chivu et al. 2006). In the first step, the chloride cation-radical and the nitrobenzene anion-radicals are formed. In the thermal and acoustic variants, the reactions lead to the same set of products with one important exception The thermal reaction results in the formation of HCl, whereas ultrasonic stimulation results in CI2 evolution. At present, it is difficult to elucidate the mechanisms behind these two reactions. As an important conclusion, the sonochemical process goes through the inner-sphere electron transfer. The outer-sphere electron transfer mechanism is operative in the thermally induced process. [Pg.281]

The reaction with monomethyl malonate in acetic acid, which does not occur at 0-10°C, proceeds smoothly when sonication is applied (Allegretti et al. 1993). From cyclohexene, only the cis ring fusion in bicyclic lactone is observed the product is formed at 80% yield for 15 min at 10°C. The overall transformation, in brief, is shown in Scheme 6.16. The stereoselectivity of the sonochemical process probably reflects the enhanced reaction rate, which does not allow equilibration processes to take place. [Pg.331]

An investigation of the Wittig-Horner reaction taking place under sonochemical irradiation and catalyzed by the activated Ba(OH)2 showed that the process could be markedly improved. The sonochemical process increased the reaction rate over... [Pg.292]

However, this commonly accepted theory is incomplete and applies with much difficulty to systems involving nonvolatile substances. The most relevant example is metals. For a heterogeneous system, only the mechanical effects of sonic waves govern the sonochemical processes. Such an effect as agitation, or cleaning of a solid surface, has a mechanical nature. Thus, ultrasound transforms potassium into its dispersed form. This transformation accelerates electron transfer from the metal to the organic acceptor see Chapter 2. Of course, ultrasonic waves interact with the metal by their cavitational effects. [Pg.278]

The stereoselectivity of the sonochemical process probably reflects the enhanced reaction rate, which does not allow equilibration processes to take place. [Pg.409]

Ultrasonic irradiation of aqueous solutions of the chlorophenols was carried out with a Vibra Cell Model VC-250 direct immersion ultrasonic horn (Sonics Materials Newtown, CT) operated at a frequency of 20 kHz with a constant power output of 50 W (the actual insonation power at the solution was 49.5 W, and the power density was 52.1 W/cm2). Reactions were done in a glass sonication cell (4.4 cm i.d. by 10 cm), similar to the one described by Suslick (1988). The temporal course of the sonochemical processes was monitored by HPLC. [Pg.450]

For all these reasons, most of the acoustical energy involved in generating the cavities and in their collapse is ultimately spent in decomposing water into H2 and 02. This is the main factor affecting sonochemical efficiency (i.e., the ratio between the rate of the reaction of interest and the applied power density, W/L). In order to improve the efficiency of a sonochemical process, chemical or physical modifications can be introduced into the system, which may reduce this loss (see Sec. IV.G). The efficiency can also be affected by the presence of other chemicals in the solution, which may react with the radicals, thus reducing the number of reactive species available to the target molecules. A preprocess might be conceived to separate some of these unwanted chemicals from the solution prior to sonochemical treatment. [Pg.214]

B. Role of Higher Ultrasonic Frequencies in the Scale-Up of Sonochemical Processes... [Pg.221]

A scale-up of a sonochemical process is usually required in order to treat commercially viable quantities of a solution. It is now becoming apparent that higher ultrasonic frequencies present perhaps the best way to scale up a process. The energy required to cavitate water is provided by the transducer in the form of mechanical waves. How does this energy ultimately dissociate the water molecule and produce chemical reactions Fig. 5 shows that for the lower ultrasonic frequencies (i.e., 20 kHz), the water itself cannot support... [Pg.221]

Sonochemistry is the research area in which molecules undergo chemical reaction due to the application of powerful ultrasound radiation (20 KHz-10 MHz) [4]. The physical phenomenon responsible for the sonochemical process is acoustic cavitation. Let us first address the question of how 20 kHz radiation can rupture chemical bonds (the question is also related to 1 MHz radiation), and try to explain the role of a few parameters in determining the yield of a sonochemical reaction, and then describe the unique products obtained when ultrasound radiation is used in materials science. [Pg.114]


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See also in sourсe #XX -- [ Pg.225 ]




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