Quiz 3 - Pt. 2 (Solid state fermentation) Flashcards
- fermentations of solid materials
- low moisture levels
- smaller reactor volume
-
low contamination and easy product separation
▪ Easy product separation
▪ Energy efficiency
▪ Differentiated microbiological
structures
Solid-state Fermentations
feed flows through a column packed with immobilized cells
Packed column
feed flows up through a bed of immobilized cells, fluidizing the immobilized cell particles
Fluidized bed
air bubbles suspend the immobilized cell particles in a reactor
Airlift
- multilayer growth of cells on solid support
- common in waste water treatment
▪ Support materials can be biologically active or inert
Biological films
_____ is widely used for enzymes but not for cells
In general, good ______ should be rigid and chemically inert, should bind cells firmly, high loading capacity
Covalent binding
good support materials
there is direct contact between nutrient and support materials; high cell loading
Physical adsorption
- animal cell culture
- cell retention and selective removal of dead cells
- removal of cell debris and inhibitory by-products
- high medium use, costs raw materials and sterilization
Perfusion culture
________ provide cofactors, reducing power, energy that many enzymatic reactions require
Whole cells
Physical Adsorption
selection of suitable support materials is highly based on ______ and _________
adsorption capacity;
strength of binding
methods of preparing polymer beads for Physical Entrapment
1) Gelation of polymers
2) Precipitation of polymers
3) Ion exchange gelation
4) Polycondensation
5) Polymerization
_____ most widely used method of cell entrapment
▪ Various matrices: porous polymers
(agar, alginate, carrageenan, polyacrylamide, chitosan, gelatin, collagen)
▪ Porous metal screens
▪ Polyurethane
▪ Silica gel
▪ Polystyrene
▪ Cellulose triacetate
* polymer beads
Physical entrapment
similar to enzyme immobilization; entrapment and binding
Active immobilization
uses biofilm
Passive immobilization
multi-layer growth on solid surfaces
Biofilm
- high cell concentrations
- eliminates cell washout at high dilution rates
- high volumetric productivities
- May provide favorable microenvironment
▪ Genetic stability
▪ Protection from shear damage - Major Limitation: Mass transfer (_____) resistances
Immobilized cell system
diffusional
taken through many feeding cycles, with each feeding cycle followed by a harvest cycle during which the volume is drawn back down to V0 and the cycle begins again
Repeated fed-batch
Fed-batch Operation
are started as batch cultures and grown to an initial cell concentration X
Fed-batch cultures
Fed-batch Operation
- gain some advantages of a CSTR, retain some disadvantages of batch
- ____reduces substrate inhibition or catabolic repression
- ____ nature usually leads to higher operations cost and batch variability
Fed-batch reactors
Semi-batch nature
Multistage chemostat
First ________ is fed with a non-inducing growth substrate, allowing the recombinant strain to be produced
the _____ from the first chemostat feeds a second chemostat that is _______, and the product is produced.
Chemostat
Effluent
Fed inducer
Special Cases - Chemostat
________ and wild type grow at the same rate if the recombinant product is not expressed
Recombinant strain
Special Cases - Chemostat
if the recombinant product is expressed, the recombinant strain grows much ________
Slower
are continually added to the second chemostat not allowing take-over by a fast growing mutant
New recombinant cells
chemostats cannot be operated if ______
Umax < D (dilution rate)
What is desired if we have a high volume of feed with a low concentration of substrate?
High dilution rate
- is more mechanically reliable and more flexible
- equations were for cell mass
Batch reactor
maintaining the organism with the desired characteristics
Genetic stability
maintaining a sterile system
Operability
validating the process; initially, many process batch is too expensive to revalidate after clinical trials
Regulatory
rate of product per time per volume. Chemostat better for growth associated products. Wasted time in batch process.
Productivity
ability to make more than one product with the same reactor. Batch better.
Flexibility
maintaining the same conditions for all of the product produced. In theory, chemostat better, steady state.
Control
Specialized Reactors
▪ Chemostat with recycle
▪ Multistage chemostat
▪ Fed-batch
▪ Perfusion
▪ Recombinant product under the
control of an inducible promoter.
Special Cases - Chemostat
types of immobilization
active immobilization
passive immobilization
porous support materials causes intraparticle pore diffusion (at high cell densities) and hard to control microenvironmental conditions
Disadvantage of Physical Entrapment
▪ Analysis similar to immobilized enzymes
▪ Damkohler number
▪ Effectiveness factor
▪ Thiele modulus
Diffusional Limitations of bilogical films
3 Immobilized Bioreactors
▪ Packed-column
▪ Fluidized-bed
▪ Airlift