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Second solution method: Separation of variables and use of partial fractions. dy y(y Integration gives ln y 1 ln y ln j y y 1 j x c*. 1) ( 1 y 1 1 ) dy y dx.

(2.30)



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has been divided into a series of blocks running parallel to the ridge crest which have been assigned magnetization vectors which are either in the direction of the ambient geomagnetic eld or in the reversed direction. The interpretation shows that the observed anomalies are simulated by a model in which the intensities of the magnetization vary, and that relatively high values of some 10 A m 1 are required to produce the necessary contrasts.

XOR row 1 with rows 3 and 4 of S1(7, 11) 0 1 0 1 0 1 1 0 0 1 B1C B0 1 0 1 1C B C B C B1C B0 0 1 0 1C B C B C @1A @0 0 0 0 0A 0 0 0 1 0 1 | {z }





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where We = c N2 D3 / is the ratio of inertial (disruptive) to surface (cohesive) forces. This expression is the well-known Weber number theory, which has been derived and validated by Chen and Middleman (1967), among others. Their substantial data set for a Rushton turbine covered a broad range of physical properties and tank size and is shown in Figure 12-8. The data are best t by eq. (12-22) with C2 = 0.053. Equations (12-21) and (12-22) show that dispersed phase systems created by turbulent ow scale-up by maintaining constant max ; or for practical industrial purposes, by constant P/V. Large Weber numbers result in small drops, and vice versa. These expressions are valid for dilute, noncoalescing systems of low d . It turns out that many stabilized or noncoalescing industrial systems with > 0.05 can also be scaled by the constant P/V criterion. Example 12-1. It is proposed to recover a fermentation product by solvent extraction. The broth has a viscosity of c = 0.3 Pa s (300 cP). While the broth is viscous, the drop phase is not. The bulk or mixture viscosity is = 0.0386 Pa s (38.6 cP). The interfacial tension is = 0.003 N/m (3.0 dyn/cm). The broth has density c = 1000 kg/m3 (1.0 g/cm3 ), but the bulk or mixture density is 1100 kg/m3 (1.1 g/cm3 ). The vessel volume is 3.54 m3 (750 gal). The vessel has a diameter T = 1.524 m (5.0 ft) and is equipped with an RDT with D/T = 0.4. Laboratory studies have shown that acceptable extraction results are obtained if the mean drop size is d32 = 50 m. Determine the required impeller speed and power draw.

The minimized LTS for this abstracted port, called APORT, consists of only four states and is depicted in Figure 10.8.

4.0x 1014

anonymous FTP so the users can drop off files ) or omitting security patches ( Did we apply that security patch to our IIS server that stopped the buffer overflow bug that allows arbitrary file downloads ) can break the trust model. If anonymous FTP is misconfigured or if the Web server is compromised, the property file could be overwritten. Hackers could download the property file and run password crackers offline to gain access to the backend server. Trust boundaries have to be well defined in the three-tier chain of information flow. Every time a user crosses a boundary, he or she must first authenticate to the server across the boundary. Within the confines of a boundary, all architecture elements should be protected in a uniform manner. Access granularity is equally important. It would make little sense to finely separate user communities into roles at the Web server only to allow all the roles equivalent access to the backend database.

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