By James O. Maloney

ISBN-10: 0071511245

ISBN-13: 9780071511247

Now in its 8th variation, Perry's Chemical Engineers' guide bargains unequalled, updated insurance of all elements of chemical engineering. For the 1st time, person sections can be found for buy. you can now obtain purely the content material you would like for a fragment of the cost of the whole quantity. Streamline your study, pinpoint really good details, and economize through ordering unmarried sections of this definitive chemical engineering reference this present day.

First released in 1934, Perry's Chemical Engineers' guide has built generations of engineers and chemists with knowledgeable resource of chemical engineering details and information. Now up-to-date to mirror the most recent know-how and methods of the recent millennium, the 8th variation of this vintage advisor presents unsurpassed insurance of each point of chemical engineering-from basic ideas to chemical methods and kit to new machine functions.

choked with over seven hundred unique illustrations, the 8th variation of Perry's Chemical Engineers' guide features:

*Comprehensive tables and charts for unit conversion

*A drastically extended part on actual and chemical facts

*New to this version: the newest advances in distillation, liquid-liquid extraction, reactor modeling, organic tactics, biochemical and membrane separation procedures, and chemical plant safeguard practices with coincidence case histories

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Extra resources for Perry's chemical Engineer's handbook, Section 1

Example text

Perhaps the most familiar technique is the capillary-flow method. The working principle is the Hagen-Poiseuille relationship between the flow rate through a tube of fixed diameter, the pressure drop, and the viscosity. In practice, because the capillary diameter appears to the fourth power in the working equation and is difficult to determine accurately, capillary viscometers are usually calibrated with reference fluids such as water or reference oils that are available from viscometer manufacturers and some national laboratories.

Such an average usually somewhat overpredicts the mixture value, and more complex mixing rules have been proposed [15] that give better quantitative results. For high-temperature liquids, compressed gases, and other systems at intermediate densities, a corresponding-states treatment is preferable. 2, and is available in the same NIST databases [9, 59]. Reference-quality correlations exist for the thermal conductivity of a few well-measured fluids such as water. 4. An additional complication in describing the thermal conductivity at intermediate densities is its divergence to infinity in the critical region.

Values of Henry’s constant kH for solute-solvent pairs may be derived from experimental solubility data. If the solvent is a mixture of liquids, methods exist [15, 36] for estimating kH in the mixture from its value in each component of the solvent. 10) and provides the pure-component endpoints that anchor the mixture calculations. The second most important factor is the binary interaction parameters, which must be fitted to reliable binary data or estimated with a reliable method. Some activity-coefficient models also require molar volumes of the pure components.

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Perry's chemical Engineer's handbook, Section 1 by James O. Maloney


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