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Cavitation pressure

Description of liquid Limiting cavitation pressures at approx. 81° F. (in atmospheres) ... [Pg.30]

EFFECT OF SURFACE REFLECTION ACOUSTIC THEORY NO CAVITATION PRESSURE... [Pg.99]

Locally variable cooling temperature profiles can be established most easily with liquid heat transfer media that do not vaporize in the intended operating range. In order to avoid cavitation, pressurized water should be used only up to ca. 220 °C heat transfer oils cover the temperature range up to 300 °C, while above this temperature salt melts are now used exclusively in reaction technology [4], The temperature ranges of possible heat transfer media arc compared in Figure 17. [Pg.436]

In homogeneous liquid systems, sonochemical effects generally occur either inside the collapsing bubble, — where extreme conditions are produced — at the interface between the cavity and the bulk liquid —where the conditions are far less extreme — or in the bulk liquid immediately surrounding the bubble — where mechanical effects prevail. The inverse relationship proven between ultrasonically induced acceleration rate and the temperature in hydrolysis reactions under specific conditions has been ascribed to an increase in frequency of collisions between molecules caused by the rise in cavitation pressure gradient and temperature [92-94], and to a decrease in solvent vapour pressure with a fall in temperature in the system. This relationship entails a multivariate optimization of the target system, with special emphasis on the solvent when a mixed one is used [95-97]. Such a commonplace hydrolysis reaction as that of polysaccharides for the subsequent determination of their sugar composition, whether both catalysed or uncatalysed, has never been implemented under US assistance despite its wide industrial use [98]. [Pg.249]

The liquid passes through a throttling valve, orifice plate or any other mechanical constriction (Figure 3.12a). If the pressure in vena contractu falls below the cavitation pressure (usually the vapor pressure of the medium), millions of microcavities will be generated. Those cavities will subsequently collapse as the liquid jet expands and pressure recovers. [Pg.242]

The vapour nucleation takes place in water under negative pressures (tension) from -20 to -30 MPa while the minimum on the spinodale curve is arranges near -200 MPa. Skripov (1972, tabl. 15) observed similar situations for liquid water, mercury and chloroform, where the cavitation pressure is 5-7 times smaller than predicted by the theory of homogeneous nucleation for the spinodale pressure minimum. For benzol, vinegar acid, aniline and CCI4 the same ratio is 1.5-2 only. [Pg.312]

Minimal values Th-Tn for different samples are between 12 and 20°C. It is mean, that nucleation of vapour phase never observed before overcooling inclusion on 10°C (or smaller) below L-V equilibrium. At average slops of water isochors as 1.5-1.6 MPa per 1°C, it corresponds to nucleation pressures from -20 to -30 MPa. Last values are very similar to cavitation pressures, estimated by other methods (see review Herbert et. al., 2006). By other words, in some fluid inclusions formation of vapour phase begin at the same pressure (rate of tension) as in capillaries, optic or other cells, but in other inclusions with same water density the cavitation take place at much higher tension (larger values of Th-Tn). [Pg.315]

Insonation at 800 kHz should produce more hydroxyl radicals than 25 kHz at the same power, but lessened cavitation pressure effects. However, given the different geometries and cell configurations employed at the different frequencies, the significance of the shift requires corroboration before mechanistic conclusions are drawn. An effort has recently been made by Petrier to correlate sonoelectro-chemical parameters at both 20 kHz and 500 kHz by using a reactor of well-defined characteristics.34... [Pg.277]

Figure 4. Cavitation pressure as a fimction of temperature for two scenarios for water reentrant spinodal scenario (a) and liquid-liquid critical point scenario (b). These scenarios predict a different temperature behavior for the liquid-vapor spinodal (dotted curve), eitha- with a minimum (a. based on extrapolation of positive pressure data [40]), or monotonic (b. based on molecular dynamics simulations with theTIPSP potential [41]). The solid curve shows the prediction of CNT based on the bulk surface tension of water it becomes unphysical when it goes beyond the liquid-vapor spinodal. The dashed curve is the DPT prediction [40] that correctly remains above the spinodal, and reflects its temperature dependence. Figure 4. Cavitation pressure as a fimction of temperature for two scenarios for water reentrant spinodal scenario (a) and liquid-liquid critical point scenario (b). These scenarios predict a different temperature behavior for the liquid-vapor spinodal (dotted curve), eitha- with a minimum (a. based on extrapolation of positive pressure data [40]), or monotonic (b. based on molecular dynamics simulations with theTIPSP potential [41]). The solid curve shows the prediction of CNT based on the bulk surface tension of water it becomes unphysical when it goes beyond the liquid-vapor spinodal. The dashed curve is the DPT prediction [40] that correctly remains above the spinodal, and reflects its temperature dependence.
The cavitation pressure has been calibrated by three methods. The flrst uses a commercial piezoelectric needle hydrophone placed at the focus. This method has a limited accuracy (13% uncertainty in the hydrophone gain), and moreover, as the needle is fragile, it can be used only at low amplitude, so that an extrapolation to... [Pg.58]

Figure 7 compares the results obtained for the cavitation pressure with different methods, excluding the one using water inclusions in quartz. Note that usually only the cavitation pressure reported is the most negative that could be observed with... [Pg.66]

Figure 7. Comparison of the cavitation pressure of water as a function of temperature obtained with different techniques a Berthelot-Bourdon tubes (solid triangle up [70], solid triangle down [27]) metal Berthelot tube with pressure transducer (open diamond [74]) z tube centrifuge (x [46]) shock wave (box plus [89]) acoustic (black bullet [47], black solid square [48], open bullet [52]) and MVLE (solid diamond [ 15 ]). An arrow means that cavitation was not observed. Reproduced with permission from Ref. [90]. Figure 7. Comparison of the cavitation pressure of water as a function of temperature obtained with different techniques a Berthelot-Bourdon tubes (solid triangle up [70], solid triangle down [27]) metal Berthelot tube with pressure transducer (open diamond [74]) z tube centrifuge (x [46]) shock wave (box plus [89]) acoustic (black bullet [47], black solid square [48], open bullet [52]) and MVLE (solid diamond [ 15 ]). An arrow means that cavitation was not observed. Reproduced with permission from Ref. [90].
Figure 8. Comparison of the cavitation pressure (top) and density (bottom) of water as a function of temperature obtained with acoustic method and water inclusions in quartz used as Berthelot tubes. The symbols represent acoustic method with calibration by static pressure method (open diamonds [43] and solid diamonds [52]), acoustic method with fiber optic probe hydrophone (solid bullets [51]), water Inclusions In quartz (open squares [45]). In the lower panel, cavitation of an inclusion during melting is also included (black filled square [92]) and light and dark arrows indicate isothermal and isochorlc paths, respectively. Solid lines are the binodals. Lower panel reproduced with permission from Ref. [52]. Figure 8. Comparison of the cavitation pressure (top) and density (bottom) of water as a function of temperature obtained with acoustic method and water inclusions in quartz used as Berthelot tubes. The symbols represent acoustic method with calibration by static pressure method (open diamonds [43] and solid diamonds [52]), acoustic method with fiber optic probe hydrophone (solid bullets [51]), water Inclusions In quartz (open squares [45]). In the lower panel, cavitation of an inclusion during melting is also included (black filled square [92]) and light and dark arrows indicate isothermal and isochorlc paths, respectively. Solid lines are the binodals. Lower panel reproduced with permission from Ref. [52].
Oil supply pressure = 0.0517 MPa (gauge) Cavitation pressure -0.175 MPa (gauge)... [Pg.358]

Transfer of a cavitating element to a full film element occurs when equation [4] predicts an oil volume equal to or exceeding the element volume Vo(j,i) Vg(j,i). The reverse transfer may occur during the film pressure relaxation process, when a sub-cavitation pressure is computed for a full film element. By means of the above processes, cavitation zones may expand or contract in any direction according to the prevailing conditions as the dynamic cycle proceeds. [Pg.359]

Liquid CO2 from a storage tank is subcooled or prepressurized by means of an inline pump (avoiding cavitations), pressurized and heated up to extraction conditions. [Pg.182]

Fisher uses a similar equation to the Equation 2.18 to describe cavitation pressure drop ... [Pg.46]


See other pages where Cavitation pressure is mentioned: [Pg.299]    [Pg.84]    [Pg.37]    [Pg.49]    [Pg.50]    [Pg.101]    [Pg.277]    [Pg.321]    [Pg.310]    [Pg.305]    [Pg.235]    [Pg.235]    [Pg.58]    [Pg.60]    [Pg.72]    [Pg.75]    [Pg.77]    [Pg.358]    [Pg.360]    [Pg.360]    [Pg.361]    [Pg.361]    [Pg.473]    [Pg.477]    [Pg.41]    [Pg.502]   
See also in sourсe #XX -- [ Pg.44 ]




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