Fundamentals of Chemical Engineering Thermodynamics (MindTap Course List)
Fundamentals of Chemical Engineering Thermodynamics (MindTap Course List)
15th Edition
ISBN: 9781285968360
Author: DAHM
Publisher: Cengage
Question
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Chapter 8.5, Problem 3E

(A)

Interpretation Introduction

Interpretation:

The boiling points of n-hexane using the Antoine equation.

Concept Introduction:

The Antoine equation is,

log10(Psat)=ABT+C

Here, Antoine coefficients are A, B, and C, vapor pressure is Psat, and temperature is T.

(B)

Interpretation Introduction

Interpretation:

The boiling points of n-hexane using the Clausius-Clapeyron equation.

Concept Introduction:

The Clausius-Clapeyron equation is,

ln(P2satP1sat)=ΔH_vapR(1T21T1)

Here, gas constant is R, temperature at state 1 and 2 is T1andT2 respectively, vapor pressure at state 1 and 2 is P1satandP2sat respectively, and change in molar enthalpy from vaporization is ΔH_vap.

(C)

Interpretation Introduction

Interpretation:

The boiling points of n-hexane using the shortcut equation.

Concept Introduction:

The shortcut vapor pressure equation is,

log10Prsat=73(ω+1)(11Tr)Tr=[1Tclog(PsatPc)(ω+1)Tc(37)]1

Here, reduced temperature is Tr, critical temperature is Tc, critical pressure is Pc, acentric factor is ω, and reduced pressure at saturated point is Prsat.

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7) You are tasked with separating two proteins by ion exchange chromatography on a 30 cm long column with an inner diameter of 2 cm. The resin has a diameter of 100 μm and a void fraction of 0.3, and your mobile phase flows through the column at a rate of Q = 5 cm³/min. The Van Deemter coefficients A, B, and C have been determined to be 0.0228 cm, 0.0036 cm²/min, and 0.00053 min, respectively, for both proteins. Protein A elutes from the column with an average retention time of 27 min and standard deviation of 0.8 min. Protein B elutes from the column. with an average retention time of 33.8 min and standard deviation of 1.0. a) How many theoretical plates does the column contain? b) What flow rate (Q) will give you the maximum resolution? c) What is the minimum height of a theoretical plate for the system?
1 5) You are asked to design a moving bed adsorption process using two columns (see the figure below). Your feed contains 100 mg/L protein and flows through both columns at 4 m³/h. Fresh resin enters the bottom of both columns (resin does not flow from the bottom column to the top column). The maximum resin flow rate that your pumps can comfortably handle is 120 kg resin/h. Experimental data suggest that the adsorption equilibrium can be modeled as qi=4ci where qi is in g protein/kg resin and c; is in g protein/L broth. (Pay attention with units!) a) What is the lowest concentration of proteins that you could get in the effluent from column 1 (indicated by the *) in mg/L? (Hint: set up a mass balance) 0.25 , * 1 2 b) What should be the flow rate of resin (in kg/h) into the second column (B2) if your overall process needs to remove 99% of the protein?
6) Instead of moving bed adsorption, you decide to try fixed bed adsorption with a different resin for removal of your protein. Your column is 25 cm long with an inner diameter of 5 cm. The resin packed in the column has a density of 1.5 g/cm³ and a void fraction of 0.25. Equilibrium data suggests that the protein binding to the column follows a Langmuir isotherm with an Stot = 6.25 g protein/kg resin and Keq = 2.58 L broth/g protein. The feed contains 100 mg/L protein and flows through the column at 500 mL/h. The calculated binding capacity of the column under these conditions is 945 mg protein. a) After 17.7 h, you detect an unacceptable level of protein in the column effluent. What is the length of unused bed? b) After deciding that this process will work well for separation, you need to scale up to a 1 m long column with the same diameter. If all else but length of the column is held constant, how long will you be able to run the column before breakthrough?
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