Separation Process Principles- 2n - Seader &amp; Henley - Solutions Manual

# For example when the pressure is 70 atm fig 1 in the

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Unformatted text preview: e interface rc and time t, differentiate Eq. (2) with respect to r and evaluate the differential at r = rc. This gives: − c A0 − c Ab dc A = (3) dr r = rc rc rc 1 − rs The rate of diffusion at r = rc is given by Fick's first law, e.g. Eq. (3-66): dN A dc A − = 4πrc2 De (4) dt dr r = rc 1− Exercise 11.26 (continued) Analysis: (continued) Where, N A is the amount of A diffused. Combining Eqs. (3) and (4): ( d N A 4πrc De c A0 − cAb = dt r 1− c rs By material balance for the solute in the core: ) (5) dN A ρA d 4 3 4πrc2ρ A drc =− πrc = − dt M A dt 3 M A dt where: (6) ρ A = initial mass of solute per unit volume of solid particle M A = molecular weight of solute Combining Eqs. (5) and (6): −ρ A 1 1 2 − rc drc = De c A0 − c Ab dt M A rc rs Integrating Eq. (7) and applying the boundary condition: ρ A rs2 t= 6 De M A c A0 − c Ab (7) rc = rs at t = 0 gives: r 1− 3 c rs 2 r +2 c rs 3 (8) For complete extraction, rs = 0, and Eq. (8) becomes: t= ρ A rs2 6 De M A c A0 − c Ab (9) Equations (5) and (9) indicate that both the rate of extraction and time for extraction depend on the effective diffusivity of the solute in the particle, which must be measured experimentally. Exercise 11.27 Subject: Supercritical extraction of a slurry of 0.002 kmol/h of solid β-carotene in 0.20 kmol/h of water with a solvent of recycle carbon dioxide in a single-stage contactor operating in the supercritical region to extract 99% of the carotene. Given: Design of a supercritical extractor using the Group-Contribution EOS of SkjoldJorgensen, at 353 K and 1013 bar, as shown in Fig. 1 of the cited article by Cygnarowicz and Seider. Find: Design of a similar extractor using the Peng-Robinson EOS with the Wang-Sandler mixing rules. Analysis: In the Cygnarowicz and Seider (C-S) article, the solubility of the carotene in water is neglected and a fit of experiment data for the solubility of carotene in CO2 is given in Fig. 2 of the C-S article. Thus, it was only necessary here to model a single-stage flash of CO2 and water. An initial run was made with the Aspen Plus program with the FLASH2 model under the following conditions, based on the PR EOS with the Wang-Sandler mixing rules (PRWS): Feed of 0.2 kmol/h of water. Solvent of 0.8004 kmol of CO2 and 0.0081 kmol/h of water. Single-stage extraction at 353 K and 1013 bar. The result of the flash was only a single phase containing both the feed and the solvent. Thus, use of the PR EOS with Wang-Sandler mixing rule did not give the required two equilibrium phases shown in the C-S article. When the extraction pressure was reduced to 101.3 bar (100 atm), the following results, which are close to the C-S results, were obtained: kmol/h: Component Feed Solvent C O2 Water Total: 0.0 0.2 0.2 0.8004 0.0081 0.8085 Raffinat e 0.0275 0.1950 0.2225 Extract 0.7729 0.0131 0.7860 However, at this much lower pressure, Fig. 2 of the C-S article shows that the mole fraction of carotene in the extract is an unacceptable 4 x 10-8 instead of t...
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