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Biochemical Engineering CEN 551 Instructor: Dr. Christine Kelly Chapter 11: Recovery and Purification of Products
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Biochemical Engineering CEN 551

Feb 08, 2016

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Biochemical Engineering CEN 551. Instructor: Dr. Christine Kelly Chapter 11: Recovery and Purification of Products. Schedule. Thursday 3/4 chapter 11HW due take home exam homework solutions Tuesday 3/16 – Haowen, Ashutosh, Nilay Thursday 3/18 – take home exam due. General Approach. - PowerPoint PPT Presentation
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Page 1: Biochemical Engineering CEN 551

Biochemical EngineeringCEN 551

Instructor: Dr. Christine Kelly

Chapter 11: Recovery and Purification of Products

Page 2: Biochemical Engineering CEN 551

Schedule

• Thursday 3/4– chapter 11HW due

– take home exam

– homework solutions

• Tuesday 3/16 – Haowen, Ashutosh, Nilay

• Thursday 3/18 – take home exam due

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General Approach

1. Separation of insoluble products or components.

2. Primary isolation or concentration and removal of water.

3. Purification and removal of contaminated chemicals.

4. Product preparation.

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Factors that impact difficulty and cost of recovery

• Product can be biomass, intracellular or extracellular component.

• Fragile or heat sensitive.

• Concentration or titer in the broth.

• Typically recovery and purification is more than 50% of total manufacturing costs

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Insoluble Products or Components

• Filtration

• Centrifugation

• Coagulation and Flocculation

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Filtration• Most cost-effective, most common in

industrial biotechnology.

• Rotary vacuum precoat filters: traditional. Penicillin mold.

• Cross flow ultrafiltration: 0.02-0.2 um bacterial separations

• Cross flow microporous filtration0.2-2 um for yeast

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Rotary vacuum precoat filters

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V = volume of filtrate

A = surface area of filter

p = pressure drop through the cake and filter medium

u = viscosity of filtrate

rm= resistance of filter medium

rc = resistance of cake

)μr(r

ΔpAg

dt

dV

cm

c

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• Substitute, integrate, linearize

= specific resistance of cake, C = cake weight/volume filtrate

• Plot t/V vs. V, slope = 1/K, intercept = 2Vo

• Can find rm and

)2V(VK

1

V

t Equation Ruth o

c

2m

o ΔpgαCμ

2AK andA

αC

r V

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• Assumes incompressible cake.• Fermentation cakes are

compressible.• Filter aid is added to decrease the

cake resistance.• pH and fermentation time can

affect resistance.• Heat treatment can reduce cake

resistance.

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Centrifugation• Used to separate solids of size 0.1 um to

100 um using centrifugal forces.

• Being replaced by microfiltration.

• Fc=2Uo

• Fc= flow, Uo= free settling velocity

=centrifugation coefficient = re2Vc/gLe

• Re=radius of rotation, = angular velocity, Le=settling distance,

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Coagulation and Flocculation

• Pretreatment to centrifugation, gravity settling or filtration to improve separation.

• Coagulation: formation of small flocs of cells using coagulating agents, electrolytes.

• Flocculation: formation of agglomeration of flocs into settleable particles using flocculating agents, polyelectrolytes or CaCl2.

• Used wastewater treatment processes to improve clarification.

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Cell Disruption – Intracellular Products

• Mechanical Methods– Sonication

– Bead beating

– Pressing

• Non-Mechanical methods– Osmotic shock

– Freeze-thaw

– Enzymatic

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• Ultrasound: disrupts cell membrane. Mostly used at the laboratory scale.

• Pressing: extrude cell paste at high pressure.

• Bead beating: grind cells with glass, metal beads.

• Heat dissipation is a problem with all of these methods.

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• Osmotic shock: Salt differences to cause the membrane to rupture. Common.

• Freeze-thaw: Causes cell membrane to rupture. Common.

• Enzymatic: Lysozyme attacks the cell wall.

Can use a combination of these methods.

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Separation of Soluble Products

• Liquid-liquid extraction• Aqueous two phase extraction• Precipitation• Adsorption• Dialysis• Reverse osmosis• Ultrafiltration and microfiltration• Cross-flow filtration and microfiltration• Chromatography• Electrophoresis• Electrodialysis

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Liquid-Liquid Extraction• Separate inhibitory fermentation

products from broth.

• Based on solubility difference for the compound between the phases.

• Distribution coefficient = KD = YL/XH

• YL=concentration in the light phase

• XN=concentration in the heavy phase

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• Mass balance assuming immiscibility yields…

X1/X0 = 1/(1+E) where E = extraction factor = LKD/H

• Percent extraction = f(E and the number of stages)

• Antibiotics are extracted using liquid-liquid extraction.

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http://www.facstaff.bucknell.edu/mvigeant/field_guide/kandle01/

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http://www.liquid-extraction.com/

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Precipitation

1. Salting out – inorganic salts (NH4)2SO4 at high ionic strength

2. Solubility reduction at low temperatures (less than –5oC) by adding organic solvents

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Adsorption

• Removal of solutes from aqueous phase onto a solid phase.

• Chromatography is based on adsorption.

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Dialysis• Membrane separation used to remove

low molecular weight solutes.• For example, removal of urea from

urine medical treatment ‘dialysis’ for diabetic patients.

• Used to remove salts from protein solutions.

• Transport occurs due to a concentration gradient driving force.

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Reverse Osmosis (RO)

• Osmosis: Transport of water molecules from a high to a low concentration pure water to salt water.

• In RO, pressure is applied to salt phase causing water to move against a concentration gradient.

• Salt phase becomes more concentrated.

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Ultrafiltration and Microfiltration

• Pressure driven molecular sieve to separate molecules of different size.

• Dead end filtration: retained components accumulate on the filter. Gel layer formed on the filter.

• Cross flow filtration: retained components flow tangentially across the filter

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Cross-flow filtration

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Types of filtration equipment

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http://www.gewater.com/equipment/membranehousing/1193_Membrane_elements.jsp

                                                                        

http://www.lcsupport.com/home.htm

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http://www.gewater.com/equipment/membranehousing/1193_Membrane_elements.jsp

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Configurations of filtration equipment

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Effect of pressure and protein concentration

on flux

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Costs of filtration equipment

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Chromatography

• Separates mixtures into components by passing the mixture through a bed of adsorbent particles.

• Solutes travel at different speeds through the column resulting in the separation of the solutes.

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http://sepragen.com/products/columns/process_columns.html

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Affinity Chromatography

Highly specific interaction between a ligand on the particle and a component in the mixture. Often based on antibodies.

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Electrophoresis

Separation of molecules based on size and charge in an electric field.

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Electrodialysis

Membrane separation to separate charged molecules from a solution.

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Finishing Steps

•Crystallization

•Drying