Recovery and Purification of Bio-Products -Strategies to recovery and purify bio-products Fermenter...

Recovery and Purification of Bio-Products

- Strategies to recovery and purify bio-products

Fermenter

Solid-liquid separation

Recovery

Purification

SupernatantCellsCell products

Cell disruption or rupture

Cell debris

Crystallization and drying

Cell DisruptionDisruption: the cell envelope is physically broken, releasing all intracellular

components into the surrounding medium

Methods: Mechanical and non mechanical

- Mechanical

- Ultrasonication (sonicators)bacteria, virus and spores suspensions at lab-scale

Electronic generator→ultrasonic waves→mechanical oscillation by a titanium probe immersedin a cell disruption.

http://www.biologics-inc.com/sd-models.htm

http://www.biologics-inc.com/ultrasonic_homogenizers.htm

Cell Disruption- Mechanical

Milling: continuous operation,

Algae, bacteria and fungiLarge scale, up to 2000kg/h liquid and solid

Principle of operation:

A grinding chamber filled with about 80% beads.

A shaft with designed discs or impellers is within the chamber.

The shift rotates at high speeds, high shearing and impact forces from the beads break the cell wall.

http://www.cbmills.com/Products/horizontalmills.htm

Dyno-Mill(liquid)

Cell Disruption- Mechanical

Ball Mill: solid Frozen cell paste, cells attached to or within a solid matrix.Large scale

http://www.unitednuclear.com/mills.htm

Cell Disruption- MechanicalHomogenization: suspension, large scale

To pump a slurry (up to 1500 bar) through a restricted orifice valve.

The cells disrupt as they are extruded through the valve to atmosphere pressure by

- high liquid shear in the orifice

- sudden pressure drop upon discharge

i.e. French press & Gaulin-Manton: lab scale Rannie high-pressure Homogenizer (large scale)

High pressure

orifice

Cell Disruption- Nonmechanical

- Chemicals: use chemicals to solubilise the components in the cell walls to release the product.

Chemical requirements:- products are insensitive to the used chemicals.- the chemicals must be easily separable.

Types of chemicals:- surfactants (solubilising lipids): sodium sulfonate,

sodium dodecylsulfate.

- Alkali: sodium hydroxide, harsh

- Organic solvents: penetrating the lipids and swelling the cells. e.g. toluene.

e.g. Bacteria were treated with acetone followed by sodium dodecyl sulfate extraction of cellular proteins.

Cell Disruption- Nonmechanical

- Enzymes: to lyse cell walls to release the product.gentle, but high cost

i.e. lysozyme (carbohydrase) to lyse the cell walls of bacteria.

- Osmotic shockOsmosis is the transport of water molecules from high- to a low-concentration region when these two phases are separated by a selective membrane.

Water is easier to pass the membrane than other components.When cells are dumped into pure water, cells can swell and burst due to the osmotic flow of water into the cells.

Cell Disruption

Challenge: Damage to the product

- Heat denaturation

- Oxidation of the product

- Unhindered release of all intracellular products



Fermenter


Recovery

Purification



Cell debris


Separation of Soluble ProductsLiquid-liquid extraction:

- Difference of solubility in two immiscible liquid

- Applicable: separate inhibitory fermentation products such as ethanol and acetone-butanol from fermentation broth.antibiotics (i.e. solvent amylacetate)

- Requirements of liquid extractants :

nontoxic, selective, inexpensive, immiscible with fermentation broth and high distribution coefficient: KD=YL/XH

YL and XH are concentrations of the solute in light and heavy phases, respectively.

The light phase is the organic solvent and the heavy phase is the fermentation broth. e.x. Penicillin is extracted from a fermentation broth using isoamylacetate. KD could reach 50.

Heavy, XH

Light, YL

Separation of Soluble Products• Liquid-liquid extraction:

When fermentation broth contains more than one component, then the selectivity coefficient (β) is important.

βil = KD,,i/KD,j

KD,,I and KD,j are distribution coefficients of component i and j.

The higher the value of βil is, the easier the separation of i from j.

pH effect

e.g. at low pH <4, Penicillin can be separated from other impurities such as acetic acid from the fermentation broth to organic phase amylacetate. Heavy, I, j

Light, i, j

Separation of Soluble Products

Precipitation

Reduce the product solubility in the fermentation broth by adding chemicals.

Applicable: separate proteins or antibiotics from fermentation broth.

Separation of Soluble ProductsPrecipitation

- Methods:- salting-out by adding inorganic salts such as ammonium sulfate, or sodium sulfate to increase high ionic strength (factors: pH, temperature)

e.g. The solubility of hemoglobin is reduced with increased amount of ammonium sulfate.

- added salts interact more stronger with water so that the proteins precipitate.

- inexpensive

- Isoelectric (IE) precipitation:

Precipitate a protein at its isoelectric point. E.g. The IE of cytochrome cM (without histidine tag) is 5.6 (Cho, et.al., 2000,

Eur. J. Biochem. 267, 1068±1074).

Separation of Soluble ProductsAdsorption

Adsorb soluble product from fermentation broth onto solids.

Approaches: physical adsorption (activated carbon), ion exchange (carboxylic acid cation exchange resin for recovering streptomycin)

Adsorption capacity: mass of solute adsorbed per unit mass of adsorbent

Affected by properties of adsorbents: functional groups and their numbers, surface properties

by properties of solution: solutes, pH, ionic strength and temperature

- Difference of Affinity of product in the solid and liquid phase.

- Applicable: soluble products from dilute fermentation


CHALLENGE!

SCREENING ADSORBENTS: THE MOST PROMISING TYPES

- high capacity- reusable

0

2

4

6

8

10

12

14

0 10 20 30 40 50

Equilibrium solute concentration in liquid (mol/l)

Equ

ilibr

ium

sol

ute

conc

enta

tion

on

solid

(m

ol/g

ads

orbe

nt)

Adsorption Isotherms

Saturated uptake

affinity

C1

Cs1*

Cs2*

Adsorbent 1

Adsorbent 2


Freundlich isotherm:

Cs* =KF CL* 1/n

KF and n are empirical constants.

Langmuir isotherm:

Cs*=CsM

CL*/(K+CL*)

CsM

is the maximum concentration of solute adsorbed on the solid phase. K is a constant. Cs* and CL* are equilibrium concentration of solute in solid and liquid phases, respectively.


Membrane separation:

- Microfiltration: 0.1 - 10 µm, bacterial and yeast cells.

- Ultrafiltration: macromolecules (2000 <MW< 500,000)

- Dialysis: removal of low-MW solutes: organic acids (100<MW<500) and inorganic ions (10<MW<100).

- Reverse osmosis: a pressure is applied onto a salt-containing phase, which drives water from a low to a high concentration region. MW < 300.

The common features of the above methods:- Use membrane - Driving forces: pressure

Separation of Soluble ProductsChromatography

To separate the solutes based on the different rate of movement of the solutes in the column with adsorbent materials.

Principles:Chromatographic processes involve a stationary phase and a

mobile phase.

Stationary phase can be adsorbent, ion-exchange resin, porous solid, or gel usually packed in a cylindrical column.

Mobil phase is the solution containing solutes to be separated and the eluant that carriers the solution through the stationary phase.

Applicable for protein, organics separation.


Method: A solution containing several solutes is injected at one end of the column followed by the eluant carrying the solution through the column.

Each solutes in the original solution moves at a rate proportional to its relative affinity for the stationary phase and comes out at the end of the column as a separated band.

(M. Shuler, Bioprocess. Eng. 2005)

Mechanism:

Similar to adsorption: interaction of solute-adsorbent

Different to adsorption:

- Chromatography is based on different rate of movement of the solute in the column

- Adsorption is based on the separation of one solute from other constituents by being captured on the adsorbent.



Electrophoresis

To separate charged solutes based on their specific migration rates in an electrical field.

Positive charged solutes are attracted to anodeand negative charged solutes to cathode.

Factors: electric field strength, electric charge of the solutes, viscosity of liquid and the particles size.

Applicable for protein separation.

Proteins Electrophoresis

http://fig.cox.miami.edu/~cmallery/150/protein/SDS.electrophoresis.jpg



Fermenter


Recovery

Purification



Cell debris



- Crystallization: last step in producing highly purified products such as antibiotics.

Supersaturated solution, low temperature, Crystals are separated by filters.

- DryingTo remove solvent from purified wet product such as crystal or dissolved solute.

Vaccum-tray dryers: pharmaceutical products

Freezing drying: by sublimation (from solid ice to vapor), antibiotics, enzyme, bacteria

Spray dryer: heat-sensitive materials

Summary of separation and purification

• Liquid-Solid Separation

- Filtration: rotary vaccum drum filter, micro- and ultrafiltration

- Centrifugation

• Cell disruption

- Mechanical: ultrasonication, milling, homogenization

- Nonmechanical: chemicals, enzyme and osmotic shock

Summary of separation and purification

• Separation of soluble products

- Liquid-liquid extraction

- Precipitation

- Adsorption

- Membrane separation: ultrafiltration, dialysis, reverse osmosis

- Chromatography

- Electrophoresis

• Crystallization and drying

Recovery and Purification of Bio-Products -Strategies to recovery and purify bio-products Fermenter...

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Transcript of Recovery and Purification of Bio-Products -Strategies to recovery and purify bio-products Fermenter...