By Timothy C. Frank

ISBN-10: 0071511385

ISBN-13: 9780071511384

Now in its 8th version, Perry's Chemical Engineers' instruction manual bargains unmatched, up to date assurance of all elements of chemical engineering. For the 1st time, person sections can be found for buy. you can now obtain merely the content material you would like for a fragment of the cost of the full quantity. Streamline your examine, pinpoint really good details, and save cash through ordering unmarried sections of this definitive chemical engineering reference today.
First released in 1934, Perry's Chemical Engineers' instruction manual has built generations of engineers and chemists with a professional resource of chemical engineering info and information. Now up-to-date to mirror the most recent know-how and methods of the hot millennium, the 8th variation of this vintage advisor offers unsurpassed assurance of each element of chemical engineering-from primary ideas to chemical procedures and kit to new machine applications.
Filled with over seven hundred designated illustrations, the 8th variation of Perry's Chemical Engineers' guide features:
*Comprehensive tables and charts for unit conversion
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*New to this variation: the most recent advances in distillation, liquid-liquid extraction, reactor modeling, organic strategies, biochemical and membrane separation techniques, and chemical plant safeguard practices with twist of fate case histories

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Additional info for Perry's Chemical Engineers' Handbook. Section 15

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561–567 (1978)]. Although the NRTL or UNIQUAC equations generally are recommended for nonionic systems, a number of alternative approaches have been introduced. Some include explicit terms for association of molecules in solution, and these may have advantages depending upon the application. An example is the statistical associating fluid theory (SAFT) equation of state introduced by Chapman et al. [Ind. Eng. Chem. , 29(8), pp. 1709–1721 (1990)]. SAFT approximates molecules as chains of spheres and uses statistical mechanics to calculate the energy of the mixture [Müller and Gubbins, Ind.

48(2), pp. 194–200 (2002)]. These methods minimize the need for data; however, the computational effort and specialized expertise required to use them generally are higher, and the accuracy of the results may not be known. An important method gaining increasing application in the chemical industry is the conductorlike screening model (COSMO) introduced by Klamt and colleagues [Klamt, J. Phys. Chem. 99, p. , 172, pp. , 48(2), pp. 369–385 (2002); and Klamt, From Quantum Chemistry to Fluid Phase Thermodynamics and Drug Design (Elsevier, 2005)].

79. 80. 81. 82. 83. 84. 85. Buchanan, Ind. Eng. , 44, p. 2449 (1952). Griswold, Chew, and Klecka, Ind. Eng. , 42, p. 1246 (1950). Johnson and Bliss, Trans. Am. Inst. Chem. , 42, p. 331 (1946). , 94, pp. 267–280 (1994). Church and Briggs, J. Chem. Eng. Data, 9, p. 207 (1964). Baker, Phys. , 59, p. 1182 (1955). Conway and Phillips, Ind. Eng. , 46, p. 1474 (1954). Hixon and Bockelmann, Trans. Am. Inst. Chem. , 38, p. 891 (1942). Hirata and Hirose, Kagalau Kogaku, 27, p. 407 (1963). , J. Chem. Eng.

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Perry's Chemical Engineers' Handbook. Section 15 by Timothy C. Frank


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