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Industrial Microbiology INDM 4005 Lecture 2 100204

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Minimise waste streams. Heat and power used efficiently. Space requirement minimised ... Good process design should minimize heating and cooling steps ... – PowerPoint PPT presentation

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Title: Industrial Microbiology INDM 4005 Lecture 2 100204


1
Industrial MicrobiologyINDM 4005Lecture
210/02/04
2
Management Of Microbial Processes / Quality
Assurance
  • Overview
  • ? Principles of GMP
  • ? Process design / optimisation
  • ? Economics

3
Fermentation Economics
  • OBJECTIVE - yield a product at a competitive
    price
  • BASIC OBJECTIVES.
  • ? Capital investment a minimum
  • ? Inexpensive raw materials
  • ? High yielding strain of microorganism
  • ? Labour saving and automation
  • ? Batch Production cycles as short as possible
  • ? Recovery and purification - simple rapid
  • ? Minimise waste streams
  • ? Heat and power used efficiently
  • ? Space requirement minimised

4
Major Areas of Cost Minimisation
  • 1. Isolation and handling of microorganism
  • 2. Plant and equipment
  • 3. Media
  • 4. Air sterilisation
  • 5. Heating and cooling
  • 6. Aeration and agitation
  • 7. Recovery cost
  • 8. Process time and duration
  • 9. Prevention of contamination
  • See Stanbury and Whitaker p.231

5
Fermentation Economics
  • With so many criteria to consider a compromise is
    often reached for individual processes
  • It is important to know the cost breakdown
  • (Nyiri and Charles, 1977) concluded there are 4
    main components contributing to process cost
  • - Raw material
  • - Fixed costs
  • - Utilities
  • - Labour
  • (Atkinson Mavituna, 1991) report use of cost
    indices to update historical figures

6
Fermentation Economics
  • Government intervention is often required to make
    fermentation processes economically viable
  • Acetone-butanol and penicillin during 2nd world
    war
  • Agricultural aid programmes in the US made
    available low-cost supplies of grain to promote
    fermentation based industry
  • Changes in EC policy encouraged fermentation
    companies to buy sugar and starch at reduced
    prices to compete on a worldwide scale
  • Reference Small bugs, big business The economic
    power of the microbe, Arnold L. Demain
    Biotechnology advances 18 (2000) 499-514

7
Isolation and handling of microorganism
  • Can the microorganism grow on simple cheap media?
  • Can it grow at higher temperatures?
  • Does it have better resistance to contamination?
  • Strain improvement, 1 increase in product output
    could pay for a mutation programme

8
Plant and equipment
  • Relationship exist between cost and size of an
    item of equipment
  • cost1 size1
  • cost2 size 2
  • n scale factor
  • Brewing 0.6,
  • SCP, 0.7 to 0.8
  • Antibody production 0.6
  • Fermentation production 0.75

n

9
Media
  • Media can represent up to 73 of the total
    production cost in a fermentation process
  • The organic carbon source is usually the most
    expensive component
  • In a cost study analysis for tissue plasminogen
    activator by a mammalian -cell process,
    fermentation materials accounted for 75 of the
    total raw materials cost
  • A variety of waste material has commonly been
    used but they have restrictions
  • variability
  • impurities
  • high water content
  • seasonal variations

10
Air Sterilisation
  • Production of large volumes of sterile air for
    aerobic fermentations is costly
  • Using sterilisation by heat is too expensive
  • Commonplace to use fixed pore membrane filters
  • Contamination probability of 1 in 1000 is
    acceptable economically, (Banks, 1979)

11
Heating and Cooling
  • Heating and cooling should be avoided in
    fermentation processes
  • However this is virtually impossible to achieve
  • Good process design should minimize heating and
    cooling steps
  • Heating required for sterilisation or product
    concentration
  • Cooling equipment can represent 10-15 of the
    investment costs for SCP production (Moo-Young,
    1977)

12
Aeration and Agitation
  • Virtually all fermentation processes require some
    form of mixing
  • In processes that have a high oxygen demand eg
    antibiotics, acetic acid production, aeration is
    considered a major economic consideration
  • A 6-day antibiotic fermentation in a 100m3
    fermenter uses approx 8,000 of power
  • Hydrocarbon based feedstocks in yeast
    fermentation require 3 times as much oxygen as
    carbohydrate substrates which has cost
    implications

13
Recovery Costs
  • Older fermentations had a cost split of 11
    between fermentation costs and isolation/purificat
    ion costs (Reisman, 1993)
  • With advent of rDNA technology split now 18 or
    110
  • Capital investment on downstream processing
    equipment is expensive
  • Extraction / purification procedures need to be
    validated by FDA, thereby incurring higher cost

14
Calculation of productivity, cost, profit,
optimum production cycle.
  • PRODUCTIVITY
  • In a batch process productivity must be
    calculated for the complete cycle. The total time
    (t) for a fermentation may be calculated
  • t 1/?m? (ln Xf/Xo ) tT tL tD
  • where ?m maximum specific growth rate
  • Xo initial cell conc.
  • Xf final cell conc.
  • tT turn-around time (washing, filling,
    sterilisation, etc)
  • tD delay time until inoculation
  • tL lag time after inoculation

15
Productivity
  • The overall productivity P is given by P Xf/ t
  • It will be possible from this equation to
    determine the effect of process changes on the
    overall productivity.
  • For example, a larger initial inoculum would
    increase Xo and shorten the process time.
  • Actively growing inocula would reduce the lag
    time (tL)

16
Effect of running time on productivity and cost -
optimum time of harvesting
In Stanbury and Whitaker
17
Batch-Process Cycle Time
  • In a batch process productivity must be
    determined for a complete process cycle
  • Productivity is defined as units of product
    generated per unit of fermenter volume in a given
    time I.e, grams of product per litre per hour
  • In fermentations with short growth cycles 14-24
    (Bakers yeast) hours the turnaround time is more
    important that for long fermentations 6-7 days
    (penicillin) in terms of productivity

18
Continuous Culture
  • Few large scale continuous-culture processes are
    in operation, microbial biomass, glucose
    isomerase, yoghurt, (Heijnen, 1992)
  • Nonetheless it is possible to compare batch v
    continuous culture productivity
  • Basically the faster the organism grows (maximum
    specific growth rate) the more favourable
    continuous over batch (Wang et al., 1979)
  • However disadvantages outweigh the advantages
  • Manufacturers reluctant to make radical changes
    to established and validated processes

19
Hazard Analysis Critical Control Point(HACCP)
  • Introduction
  • Beer safety and HACCP
  • The basics of HACCP
  • HACCP Terminology and Definitions
  • Steps to develop a HACCP Plan
  • Apply 7 principles
  • HACCP and SOPs
  • Explanation of a typical critical control point
    in Microbreweries
  • General flow diagram of a brewing process
  • CCP Decision Tree

20
Conclusion
  • Understand the importance of being able to manage
    microbial processes
  • What is HACCP?
  • How to implement HACCP
  • Fermentation economics
  • How to calculate productivity in batch culture
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