Get Chemical Engineering Dynamics: Modelling with PC Simulation PDF

By John Ingham

ISBN-10: 3527297766

ISBN-13: 9783527297764

During this e-book, the modelling of dynamic chemical engineering strategies is gifted in a hugely comprehensible manner utilizing the original blend of simplified primary conception and direct hands-on desktop simulation. the math is saved to a minimal, and but the approximately a hundred examples provided on a CD-ROM illustrate nearly each element of chemical engineering technological know-how. every one instance is defined intimately, together with the version equations. they're written within the smooth easy simulation language Berkeley Madonna, that are run on either home windows workstation and Power-Macintosh pcs. Madonna solves types comprising many usual differential equations utilizing extremely simple programming, together with arrays. it's so strong that the version parameters will be outlined as ''sliders'', which permit the influence in their switch at the version habit to be visible shortly. info can be integrated for curve becoming, and sensitivity or a number of runs should be played. the implications may be visible concurrently on multiple-graph home windows or through the use of overlays. the ensuing studying impression of this can be great. The examples should be different to slot any genuine state of affairs, and the advised routines offer sensible assistance. The large event of the authors, either in college educating and overseas classes, is mirrored during this well-balanced presentation, that's appropriate for the trainer, the scholar, the chemist or the engineer. This booklet offers a better knowing of the formula and use of mass and effort balances for chemical engineering, in a so much stimulating demeanour. This e-book is a moment version, that is a lot superior via the hot software program, and it is also a brand new part on organic procedure examples.

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Additional resources for Chemical Engineering Dynamics: Modelling with PC Simulation

Sample text

2 Formulation of Dynamic Models When the flow and inlet concentration vary with time, a solution is best obtained by numerical integration. 2 Case B. 15. Agitated tank for dissolving solids. For a batch system, with no inflow and no outflow, the total mass of the system remains constant. The solution to this problem, thus involves a liquid-phase component material balance for the soluble material, combined with an expression for the rate of mass transfer of the solid into the liquid. The component material balance is then ] [ Rate of accumulation Rate of transfer = of the solid of the material in the solvent to the solvent 1 giving where, VL is the volume of the liquid, CL is the concentration of the component in the liquid, kL is the liquid phase mass transfer coefficient, A is the total interfacial area for mass transfer and CL* is the equilibrium value.

For an open system with energy exchange across its boundaries, as shown in Fig. 1 . I 7, the energy balance can be written as Rate of of energy Rate of Rate of Rate of Rate of work done by the 28 1 Basic Concepts Here, E is the total energy of the system, Ei is the energy per mole of component i, Ni is the molar flow rate of component i, Q is the rate of energy input to the system due transfer and S is the total number of components (reactants and inerts). 17. A continuous reactor showing only the energy-related variables.

15. Agitated tank for dissolving solids. For a batch system, with no inflow and no outflow, the total mass of the system remains constant. The solution to this problem, thus involves a liquid-phase component material balance for the soluble material, combined with an expression for the rate of mass transfer of the solid into the liquid. The component material balance is then ] [ Rate of accumulation Rate of transfer = of the solid of the material in the solvent to the solvent 1 giving where, VL is the volume of the liquid, CL is the concentration of the component in the liquid, kL is the liquid phase mass transfer coefficient, A is the total interfacial area for mass transfer and CL* is the equilibrium value.

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Chemical Engineering Dynamics: Modelling with PC Simulation by John Ingham


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