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Industrial cultures

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  • Industrial cultures

  • Fermentation and scale up processing

    Handling and preservation of industrial

    microorganism

    Sterility in industrial microbiology

    Microbiological industrial application

  • Industrial microbiology and microbial

    biotechnology, are they in similar field?

  • Major microbial used:

    fungi (yeast and mold)

    Certain prokaryote: streptomyces

    Industrial microorganism are metabolite

    specialists, capable of synthesizing one or

    more product in high yield

    Genetically alter strains of industrial microbe

    by mutations or recombinant - achieved higher yield

  • Sources microbe:

    ATCC- American type culture collection

    DSMZ, germany Deutsche Sammlung von Microorganism

    Process:

    New biocatalyzed process (patented) deposited into national collection

  • Microbe suitable for industrial process must

    have other feature beside just being able to

    produce the substance of interest:

    Organism must capable to growth and product

    formation in large scale culture

    Produce spore or some reproductive cell form so

    that it can be easily inoculated into large scale

    fermentor

    Grow rapidly and produce desire product in a

    relatively short period of time

    Able to grow in a relatively inexpensive liquid

    culture medium obtainable in bulk quantities

  • Not be pathogenic esp to humans or economically

    important animals or plants

    Can be amenable to genetic manipulation.

    Example of industrial product:

    Microbial cell yeast

    Substances produced by cell

    Enzyme(glucose isomerase)

    Commodity chemical ethanol, citric acid, etc

  • Pyruvic acid metabolized in the absence of oxygen

    Definasi

    Pyruvic lactic acid

    No gas are produce Lactobacilli,

    streptococci

    Eg. In cheeses making

    Homolactic CO2 released

    from Pyruvic acid to form acetaldehydeethyl alcohol

    Yeast fermentation

    Eg in bread, wine

    Alcoholic

  • Vessel in which industrial process is carried

    oout: fermentor

    Fermentation:

    Any large scale microbial process whether or not

    it is biochemically fermentation

    Mostly involve aerobic

    size varies depend on the process and how it

    is operated.

    5-10 L : laboratory scale

    500000 L : industrial scale

  • Industrial fermentor: anaerobic and aerobic

    process

    Anerobic: require little special equipment except

    for removal of heat generated

    Aerobic: more elaborate equipment for better

    mixing and adequate earation

    Fermentor size (L) Product

    1-20 000 Diagnosis enzymes, substances

    for molecular biology

    40-80 000 Some enzyme, antibiotics

    100-150 000 Penicilin, aminoglycoside

    antibiotics, proteases, amylases,

    steroid transformations, amino

    acid, wine, beer

    200 000 500 000 Amino acid (glutamic acid), wine, beer

  • A-exhaust

    B-impeller

    C-sparger (high

    pressure air)

    D-harvest

    E- culture broth

    F-cooling jacket

    Sterile air

    Cooling water in

  • Installation. Note:

    External cooling coils

  • Installation. Note:

    Location of mezzanine

    floor

  • Top (mezzanine

    floor). Note:

    Agitator motor

  • Top (mezzanine

    floor). Note:

    Control panel (now

    superseded by

    microprocessor/comp

    uter control)

  • Top (mezzanine

    floor). Note:

    Inspection hatch

  • Interior view from

    bottom. Note:

    Agitators

  • Interior view from

    bottom. Note:

    Baffles

  • Interior view from

    bottom. Note:

    Inspection hatch and

    ladder

  • Fermenter Building Air mixed fermenters are taller/thinner than systems

    with agitators

  • Top

    Note lack of agitator motor

  • Base

  • CIP (clean in place) and in situ sterilisation

    Constructed in stainless steel:

    Inert and strong

    Cooling: Jacket or coils (internal or external)

  • General View

  • Control Consol.

    Note:

    Microprocessor logging

    and control

  • Control consol.

    Note:

    Microprocessor logging

    and control

    Gas supply rotameters

  • Control consol.

    Note:

    Microprocessor logging

    and control

    Gas supply rotameters

    Pumps for pH control,

    antifoam, nutrient

    feed etc

  • Fermenter vessel.

    Note:

    Detachable stirrer

    motor

  • Fermenter vessel.

    Note:

    Detachable stirrer

    motor

    pH/oxygen electrodes

  • Fermenter vessel.

    Note:

    Detachable stirrer

    motor

    pH/oxygen electrodes

    Exhaust gas condenser

  • Fermenter vessel. Note: Detachable stirrer

    motor

    pH/oxygen electrodes

    Exhaust gas condenser

    Dialysis unit (not usual!)

  • Measure of growth and product formation

    Control the process by altering environment

    parameters : temperature, pH, cell mass,

    level of key nutrients, product concentration

    Obtain data in real time:

    Eg:alter one or more environmental parameter as

    fermentation progress or to feed a nutrient at a

    rate that exactly balance growth

    Computer process of data on line and then

    response accordingly

  • Scale up:

    The transfer of a process from small scale

    laboratory equipment to large scale commercial

    eqipment

    Biocatalyst processes rarely behave the same

    way in large scale fermentor.

    Needed of biochemical engineer: familiar

    with gas transfer, fluid dynamic, mixing,

    thermodynamics

  • Laboratory flask

    -indication of possible process for commercial interest product

    Laboratory fermentor(1-10L)

    -small scale fermentor

    - First effcort of scale up

    - Test variation in medium, temp, pH etc (costing)

    Piloty plant stage (300-3000L)

    - Condition more closely approach to commercial scale

    Commercial fermentor(10 000-500000L

    -

  • Isolation of the microbe

    from nature resourc

    es

    Identification of desire

    microbe

    Characterization of the microbe

    Screening of the desire

    microbe

    Inoculum preparati

    on

    Strain improve

    ment fermentation

  • Microbial preservation

    microorganism or virus has been selected or created to serve a specific purpose, it must be preserved in its original form for further use and study

    Objective of preservation:

    to ensure optimal long-term viability and genetic stability

  • The preservation methods used in the

    collections may differ.

    Each collection must maintain detailed

    protocols of the applied preservation

    methods and their application to specific

    groups of microorganisms.

    After every preservation of a microbial

    strain, controls are necessary. e.g viability

    and purity, and where appropriate, the

    identity of the preserved culture have to be

    checked immediately after preservation.

  • Reduction of temperature of growth

    Dehydration

    Reduction of nutrients

    Reduction of microbial metabolite

  • Preservation on agar with ordinary refrigeration

    (4 10C)

    Organisms growing on suitable agar at normal growth temperatures attain the stationary phase and begin to

    die because of the release of toxic materials and the

    exhaustion of the nutrients. Agar-grown organisms are

    therefore refrigerated as soon as adequate growth

    Aerobic microbial Agar slant and petri disk

    Anaerobic microbial - oil overlay and agar stabs

    which are then sealed with sterile molten

    petroleum jelly,

  • Preservation in Deep Freezers at about -20C, or between -60C and -80C

    store microorganisms in either type of deep freezers in the form of agar plugs or on sterile glass beads coated with the organism to be stored

    Preservation on glass bead

    placed in broth containing cryoprotective compounds such as glycerol, raffinose, lactose, or trehalose. Sterile glass beads are placed in the glass vials containing the bacterial cultures. The vials are gently shaken before being put in the deep freezer

    Storage of agar cores with microbial growth

    placing agar plugs of confluent growth of bacteria and yeasts and hyphe of moulds or actinomycete in glass vials containing a suitable cryoprotectant and freezing the vials in deep freezers as above

  • Storage in low temperature liquid or vapor

    phase nitrogen (-156C to -196C)

    method for organisms which will not survive

    freeze-drying

    Some of the most commonly used

    cryoprotectants are (vol/vol) 10-20% glycerol and

    5-10% dimethyl sulfoxide (DMSO) in broth culture

    of the organism in vials which are then frozen in

    liquid nitrogen

  • Drying on silica gel

    Screw-cap tubes half-filled silica gel are sterilized in an oven. On cooling a skim-milk suspension of spores and the cells of the fungus or actinomycetes is placed over the silica gel and cooled. They are dried at 25C, cooled and stored in closed containers containing desiccants.

    Preservation on sterile filter paper

    placing drops of broth containing the spores on sterile filter paper in a Petri dish and drying in a low temperature oven or in a dessicator.

    After drying the filter paper may be placed in sterile screw caps bottles and stored either at room temperature or in the refrigerator.

  • Freeze-drying (drying with freezing), lyophilization organism is first frozen. Subsequently, water is removed

    by direct vaporization of the ice with the introduction of a vacuum.

    As the suspension is not in the liquid state, distortion of shape and consequent cell damage is minimized.

    At the end of the drying the ampoule containing the organism may be stored under refrigeration although survival for many years has also been obtained by storage at room temperature

    L-drying (liquid drying, drying without refrigeration) organisms are not frozen, but dried from the liquid state

    to preserve non-spore formers sensitive to freeze-drying, such as Cytophaga, Spirillum and Vibrio.

    Liquid drying has been effectively used to preserve organisms such as anaerobes that are

  • Many organisms die in distilled water

    because of water absorption by osmosis.

    However some have been known to survive

    for long periods in sterile distilled water.

    Usually such storage is accompanied by

    refrigeration;

  • Basic of loss by contamination

    Method of achieving sterility (physical and

    chemical)

    Aspects of sterilization in industry

    Sterilization of the fermentor and it accessories

    Medium sterilization

  • The contaminant may utilize the components of the fermentation broth to produce unwanted end-products and therefore reduce yield. e.g in beer industry when lactic acid bacteria

    contaminate the fermentating wort, they utilize sugars present therein to produce unwanted lactic acid which renders the beer sour

    contaminant may alter the environmental conditions such as the pH or oxidation-reduction potential of the fermentation and render it unsuitable for maximum production of the required product.

  • Contamination by lytic organisms such as

    bacteriophages or Bdellovibrio could lead to

    the entire destruction of the producing

    organism.

    The result could be losses in manpower time

    needed to devise means of dealing with the

    product

  • Physical method

    Asepsis

    Filteration

    Heat

    Radiation

    Chemical method

    Chemosterilants

    Gaseous sterilants

    Phenol and chlorine

  • Steam is used to sterilize the medium in situ in the fermentor but

    sometimes the medium may be sterilized separately in a retort or

    autoclave and subsequently transferred aseptically to a

    fermentor.

    In order to avoid microbial growth within the fermentor when not

    in use, crevices and rough edges are avoided in the construction

    of fermentors, because these provide pockets of media in which

    undesirable microorganisms can grow. These crevices and rough

    edges may also protect any such organisms from the lethal

    effects of sterilization.

    saturated steam should be used and should remain in contact

    with all parts of the fermentor for at least half an hour.

    Pipes which lead into the fermentor should be steam-sealed using

    saturated steam.

    The various probes used for monitoring fermentor activities,

    namely probes for dissolved oxygen, CO2, pH, foam, etc., should

    also be sterilized