By Lyle F. Albright
This can be a vector PDF reproduction. Grayscale, 1930 pages. first-class caliber, with bookmarks and renumbered pages.
From basics to plant operations, Professor Albright’s guide is an intensive but succinct advisor to daily equipment and calculations utilized in chemical engineering functions. Leaders from an excellent range of specialties offer a transparent evaluate of uncomplicated details, together with illustrative case examples and references to additional info for extra complicated learn. They talk about crucial rules, calculations, and key matters reminiscent of response engineering, strategy keep watch over and layout, waste disposal, and electrochemical and biochemical engineering. the ultimate chapters hide patents, highbrow estate, communications, and moral concerns which are so much appropriate to engineers.
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Additional info for Albright's Chemical Engineering Handbook
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  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.
Albright's Chemical Engineering Handbook by Lyle F. Albright