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Jean-Paul Duroudier's Adsorption-Dryers for Divided Solids PDF

By Jean-Paul Duroudier

ISBN-10: 008101774X

ISBN-13: 9780081017746

ISBN-10: 1785481797

ISBN-13: 9781785481796

Adsorption-Dryers for Divided Solids, a part of the business gear for Chemical Engineering set, presents sensible functions and exact wisdom on worldwide examine, offering an in-depth examine of quite a few facets in the box of chemical engineering.

This quantity discusses the main of adsorption of gaseous impurities, sensible info on adsorption, ion alternate and chromatography, the speculation of drying, and the speculation of imbibition. the writer additionally presents tools wanted for knowing the gear utilized in utilized thermodynamics within the wish of encouraging scholars and engineers to construct their very own courses. Chapters are complemented with appendices which supply more information and linked references.

  • Provides key features of fluid-solid equilibriums
  • Includes a realistic use of adsorbents that may be utilized
  • Covers specific circumstances in chromatography
  • Presents common tools for calculations on dryers

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Extra info for Adsorption-Dryers for Divided Solids

Example text

One possible solution is, in advance, to adsorb the product A to the solid in a very small quantity before carrying out the adsorption-pushing operation. 2. 1. Rectangular injection – brief injection Over a time period tp, we introduce the volume V0 of fluid at a constant concentration c0 (or, better put, at a constant composition). Now consider the Dirac distribution (generally known as brief injection). To do so, consider a number ε as small as possible, and a volume of fluid V0. We can choose a volume V such that: V − V0 < ε According to Dirac, we can choose a concentration c0 such that for c>c0, we have: c × V − V0 = M M is expressed in kg or kmol.

These three volumes are, together, equal to the total volume injected: v B c A = ( v B − v A ) c Aobs + K 'A (1 − ε ) v c c A + ε v c c A where cAobs is the concentration of A in the effluent during the fixation of B, and K 'A is the equilibrium coefficient of A in the presence of B. We deduce: ' c Aobs v B − K A (1 − ε ) vc − εvc = cA vB − vA It is only when KA = K 'A that cAobs = cA, meaning that the concentration cA of the feed is equal to the concentration cAobs of the volume vB – vA. Otherwise, all the terms involved in that relation can be found directly by measuring, except for K 'A , which we can then obtain by using the above relation.

The reduced plate height is: h = H / dp dp: diameter of the particles: m. s-1; D: diffusivity of the marker in the fluid. 42 Adsorption – Dryers for Divided Solids Unfortunately, in evaluating the coefficients A, B and D, we must draw on experience. 4. Height equivalent to a theoretical plate [KNO 77] This concept is inspired by liquid–gas exchange in a packed column. However, this analogy is misleading if we are looking at a chromatography column. Indeed, for a feed in the form of a Dirac pulse, we know that the concentration profile of the liquid at the output is a bell curve whose standard deviation σ is given by the following relation, which is the definition of the TPEH.

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Adsorption-Dryers for Divided Solids by Jean-Paul Duroudier


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