Dynamic Model for Mass Transfer of Solutes in Cucumber Fermentation

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Dynamic Model for Mass Transfer of Solutes in Cucumber Fermentation Fredrico V. Passos, Richard M. Felder , Henry P. Fleming, Roger F. McFeeters, David F. Ollis Presented by MD. WALIUL ISLAM Oklahoma State University Spring 2012 Course: Diffusional Mass Transport

Transcript of Dynamic Model for Mass Transfer of Solutes in Cucumber Fermentation

Page 1: Dynamic Model for Mass Transfer of Solutes in Cucumber Fermentation

Dynamic Model for Mass Transfer of Solutes in Cucumber Fermentation

Fredrico V. Passos, Richard M. Felder , Henry P. Fleming, Roger F. McFeeters, David F. Ollis

Presented by MD. WALIUL ISLAMOklahoma State UniversitySpring 2012Course: Diffusional Mass Transport

Page 2: Dynamic Model for Mass Transfer of Solutes in Cucumber Fermentation

“A mathematical model for transfer of solutes between whole cucumbers and brine in cucumber fermentation.”

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Objective of the StudyTo measure rates of solute movement into and out of non-fermenting brined pickling cucumbers to formulate a transport model.

To determine the controlling mechanism of solute transport.

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Experimental Procedure

Fruits were brined in glass jar containing 40% cucumber and 60% brine by weightAcetic Acid, Lactic Acid, Ethanol & Sodium metabisulfite were also addedSO2 with trace amount was added to avoid growth of microorganismBrined cucumbers were held @ 30°C for 6days

(CONT’D)

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Experimental Procedure (Cont’d)

The jars containing the material were continuously purged with N2 to prevent bloater formation.2 ml samples were taken periodically (3-12 hr) from brineNaCl concentrations were determined by titration with standard AgNO3Concentration of all other solutes were determined using HPLC

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Transport Model Development

)( bcb

tb CChV

KAdtdC

K= Overall Permeabilityh=Thickness of Vegetable Skin (Membrane)At= Total Skin Surface AreaVb= Brine VolumeCb= Concentration of Solute in BrineCc=Concentration of Solute at Inner Surface of Vegetable Skin

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Similarities with Fick’s First LawJA= -D

dzdC

So we see, the main driving force for mass transfer is concentration

gradient

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Fasina et al.(2002) suggested the following equation

)exp(0

ktCCCCeq

eq

The above equation provided a good fit to their data

Transient Mass Transfer

to represent the movement of solutes

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Rate of solute permeation into or out of the cucumber

Jf(mol/s)=kfAt(Cb-Cx)

kf = film diffusivityAt =External Cucumber Surface AreaCb= Concentration of Solute in BrineCx =Solute concentration @the interface between the fluid boundary layer and the exterior cucumber surface

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The flux through the skinJs=(1/h)(pstAs+pecAe)

(Cx-Cc)Pst= Permeability of solute through stomataPec=Permeability of solute through epidermal cellCc=Concentration of Solute at Inner Surface of Vegetable Skinh=Thickness of Vegetable Skin (Membrane)Ast=Cross sectional area of stomata (1st diffusion channel)Aec=Cross sectional area of epidermal cell (2nd diffusion channel)

Note Pec=Henry’s law solubility of solute * Diffusivity of solute

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FinallyJf=Js=J whereJ=KAt(Cb-Cc)

ecests

t

f pApAhA

kK

11And

kf, pst and pec are transport coefficients

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Plot of measured and Predicted concentrations (Cb,i/Cb0,i) vs. Time for Acetic acid (a) and Lactic acid (b) at different circulation rates.

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Plot of measured and Predicted concentrations (Cb,i/Cb0,i) vs. Time for Acetic acid (a) and Lactic acid (b) at different cucumber sizes.

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Plot of measured and Predicted concentrations (Cb,i/Cb0,i) vs. Time for Acetic acid (a) and Lactic acid (b) at different for Lactic acid , Acetic acid, Ethanol, NaCl, Glucose and Malic acid.

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THANK YOU

QUESTIONS???