By James N. Tilton
Now in its 8th variation, Perry's Chemical Engineers' instruction manual bargains unequalled, updated assurance of all features of chemical engineering. For the 1st time, person sections can be found for buy. you can now obtain purely the content material you wish for a fragment of the cost of the complete quantity. Streamline your learn, pinpoint really expert details, and save cash by way of ordering unmarried sections of this definitive chemical engineering reference this day. First released in 1934, Perry's Chemical Engineers' instruction manual has outfitted generations of engineers and chemists with a professional resource of chemical engineering info and knowledge. Now up-to-date to mirror the newest expertise and techniques of the hot millennium, the 8th version of this vintage advisor presents unsurpassed insurance of each point of chemical engineering-from primary rules to chemical procedures and kit to new machine functions. packed with over seven-hundred precise illustrations, the 8th variation of Perry's Chemical Engineers' instruction manual gains: *Comprehensive tables and charts for unit conversion *A significantly accelerated part on actual and chemical information *New to this version: the most recent advances in distillation, liquid-liquid extraction, reactor modeling, organic strategies, biochemical and membrane separation methods, and chemical plant safeguard practices with coincidence case histories
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Additional resources for Perry's Chemical Engineers' Handbook 8 E Section 6:Fluid and Particle Dynamics
Because the Navier-Stokes equations are first-order in pressure and second-order in velocity, their solution requires one pressure boundary condition and two velocity boundary conditions (for each velocity component) to completely specify the solution. The no slip condition, which requires that the fluid velocity equal the velocity of any bounding solid surface, occurs in most problems. Specification of velocity is a type of boundary condition sometimes called a Dirichlet condition. Often boundary conditions involve stresses, and thus velocity gradients, rather than the velocities themselves.
Viscoelastic fluids exhibit elastic recovery from deformation when stress is removed. Polymeric liquids comprise the largest group of fluids in this class. A property of viscoelastic fluids is the relaxation time, which is a measure of the time required for elastic effects to decay. Viscoelastic effects may be important with sudden changes in rates of deformation, as in flow startup and stop, rapidly oscillating flows, or as a fluid passes through sudden expansions or contractions where accelerations occur.
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Perry's Chemical Engineers' Handbook 8 E Section 6:Fluid and Particle Dynamics by James N. Tilton