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Chemostat

 
(′kē·mə′stat)

(microbiology) An apparatus, and a principle, for the continuous culture of bacterial populations in a steady state.


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Sci-Tech Encyclopedia: Chemostat
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An apparatus (see illustration) for the continuous cultivation of microorganisms or plant cells. The nutrients required for cell growth are supplied continuously to the culture vessel by a pump connected to a medium reservoir. The cells in the vessel grow continuously on these nutrients. Residual nutrients and cells are removed from the vessel (fermenter) at the same rate by an overflow, thus maintaining the culture in the fermenter at a constant volume.

Schematic representation of chemostat apparatus.
Schematic representation of chemostat apparatus.

An important feature of chemostat cultivation is the dilution rate, defined as the volume of nutrient medium supplied per hour divided by the volume of the culture. During chemostat cultivation, an equilibrium is established (steady state) at which the growth rate of the cells equals the dilution rate. The higher the dilution rate, the faster the organisms are allowed to grow. Above a given dilution rate the cells will not be able to grow any faster, and the culture will be washed out of the fermenter. The chemostat thus offers the opportunity to study the properties of organisms at selected growth rates. See also Fermentation.

The nutrient medium which is fed to the fermenter contains an excess of all growth factors except one, the growth-limiting nutrient. The concentration of the cells (biomass) in the fermenter is dependent on the concentration of the growth-limiting nutrient in the medium feed. Upon entering the fermenter, the growth-limiting nutrient is consumed almost to completion, and only minute amounts of it may be found in the culture and the effluent. Initially, when few cells have been inoculated in the growth vessel, even the growth-limiting nutrient is in excess. Therefore, the microorganisms can grow at a rate exceeding their rate of removal. This growth of cells causes a fall in the level of the growth-limiting nutrient, gradually leading to a lower specific growth rate of the microorganisms. Once the specific rate of growth balances the removal of cells by dilution, a steady state is established in which both the cell density and the concentration of the growth-limiting nutrient remain constant. Thus the chemostat is a tool for the cultivation of microorganisms almost indefinitely in a constant physiological state.

To achieve a steady state, parameters other than the dilution rate and culture volume must be kept constant (for example, temperature and pH). The fermenter is stirred to provide a homogeneous suspension in which all individual cells in the culture come into contact with the growth-limiting nutrient immediately, and to achieve optimal distribution of air (oxygen) in the fermenter when aerobic cultures are in use.

Laboratory chemostats usually contain 0.5 to 10.5 quarts (0.5 to 10 liters) of culture, but industrial chemostat cultivation can involve volumes up to 343,000 gal (1300 m3) for the continuous production of microbial biomass.

The chemostat can be used to grow microorganisms on very toxic nutrients since, when kept growth-limiting, the nutrient concentration in the culture is very low. The chemostat can be used to select mutants with a higher affinity to the growth-limiting nutrient or, in the case of a mixed population, to select the species that are optimally adapted to the growth limitation and culture conditions. The chemostat is of great use in such fields as physiology, ecology, and genetics of microorganisms. See also Bacterial genetics; Bacterial physiology and metabolism; Microbiology.


Veterinary Dictionary: chemostat
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A vessel that provides constant growth conditions for bacteria.

Wikipedia: Chemostat
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Stirred bioreactor operated as a chemostat, with a continuous inflow (the feed) and outflow (the effluent). The rate of medium flow is controlled to keep the culture volume constant.

A chemostat (from Chemical environment is static) is a bioreactor to which fresh medium is continuously added, while culture liquid is continuously removed to keep the culture volume constant.[1][2] By changing the rate with which medium is added to the bioreactor the growth rate of the microorganism can be easily controlled.

Contents

Operation

Steady State

One of the most important features of chemostats is that micro-organisms can be grown in a physiological steady state. In steady state, growth occurs at a constant rate and all culture parameters remain constant (culture volume, dissolved oxygen concentration, nutrient and product concentrations, pH, cell density, etc.).In addition environmental conditions can be controlled by the experimenter.[3] Micro-organisms grown in chemostats naturally strive to steady state: if a low amount of cells are present in the bioreactor, the cells can grow at growth rates higher than the dilution rate, as growth isn't limited by the addition of the limiting nutrient. The limiting nutrient is a nutrient essential for growth, present in the media at a limiting concentration (all other nutrients are usually supplied in surplus). However, if the cell concentration becomes too high, the amount of cells that are removed from the reactor cannot be replenished by growth as the addition of the limiting nutrient is insufficient. This results in an equilibrium situation (steady state), where the rate of cell growth is equal to the rate of cell removal.

Because obtaining a steady state requires at least 5 volume changes, chemostats require large nutrient and waste reservoirs.

Dilution Rate

At steady state the specific growth rate (μ) of the micro-organism is equal to the dilution rate (D). The dilution rate is defined as the rate of flow of medium over the volume of culture in the bioreactor:

D = \dfrac{\mbox{Medium flow rate}}{\mbox{Culture volume}} = \dfrac{\mbox{F}}{\mbox{V}}

Maximal growth rate

Each microorganism growing on a particular substrate has a maximum specific growth rate (μmax) (the rate of growth observed if none of the nutrients are limiting). If a dilution rate is chosen that is higher than μmax, the culture will not be able to sustain itself in the bioreactor, and will wash out.

Applications

Research

Chemostats in research are used for investigations in cell biology, as a source for large volumes of uniform cells or protein. The chemostat is often used to gather steady state data about an organism in order to generate a mathematical model relating to its metabolic processes. Chemostats are also used as microcosms in ecology[4][5] and evolutionary biology[6][7][8][9]. In the one case, mutation/selection is a nuisance, in the other case, it is the desired process under study. Chemostats can also be used to enrich for specific types of bacterial mutants in culture such as auxotrophs or those that are resistant to antibiotics or bacteriophages for further scientific study.[10]

Competition for single and multiple resources, the evolution of resource acquisition and utilization pathways, cross-feeding/symbiosis[11][12], antagonism, predation, and competition among predators have all been studied in ecology and evolutionary biology using chemostats.[13][14][15]

Industry

Chemostats are frequently used in the industrial manufacturing of ethanol. In this case, several chemostats are used in series, each maintained at decreasing sugar concentrations.[citation needed]

Concerns

  • Foaming results in overflow with the volume of liquid not exactly constant.
  • Some very fragile cells are ruptured during agitation and aeration.
  • Cells may grow on the walls or adhere to other surfaces[16], which is easily overcome by treating the glass walls of the vessel with a silane to render them hydrophobic.
  • Mixing may not truly be uniform, upsetting the "static" property of the chemostat.
  • Dripping the media into the chamber actually results in small pulses of nutrients and thus oscillations in concentrations, again upsetting the "static" property of the chemostat.
  • Bacteria travel upstream quite easily. They will reach the reservoir of sterile medium quickly unless the liquid path is interrupted by an air break in which the medium falls in drops through air.

Continuous efforts to remedy each defect lead to variations on the basic chemostat quite regularly. Examples in the literature are numerous.

  • Antifoaming agents are used to suppress foaming.
  • Agitation and aeration can be done gently.
  • Many approaches have been taken to reduce wall growth[17][18]
  • Various applications use paddles, bubbling, or other mechanisms for mixing[19]
  • Dripping can be made less drastic with smaller droplets and larger vessel volumes
  • Many improvements target the threat of contamination

Variations

Fermentation setups closely related to the chemostats are the turbidostat, the auxostat and the retentostat. In retentostats culture liquid is also removed from the bioreactor, but a filter retains the biomass. In this case, the biomass concentration increases until the nutrient requirement for biomass maintenance has become equal to the amount of limiting nutrient that can be consumed.

See also

References

  1. ^ Novick A, Szilard L (1950). "Description of the Chemostat". Science 112 (2920): 715–6. doi:10.1126/science.112.2920.715. PMID 14787503. 
  2. ^ James TW (1961). "Continuous Culture of Microorganisms". Annual Review of Microbiology 15: 27–46. doi:10.1146/annurev.mi.15.100161.000331. 
  3. ^ D Herbert, R Elsworth Telling RC (1956). "The continuous culture of bacteria;a theroretical and Experimental study". J. gen. Microbiol 14 (3): 601–622. doi:10.1099/00221287-14-3-601. 
  4. ^ Becks L, Hilker FM, Malchow H, Jürgens K, Arndt H (2005). "Experimental demonstration of chaos in a microbial food web". Nature 435 (7046): 1226–9. doi:10.1038/nature03627. PMID 15988524. 
  5. ^ Pavlou S, Kevrekidis IG (1992). "Microbial predation in a periodically operated chemostat: a global study of the interaction between natural and externally imposed frequencies". Math Biosci 108 (1): 1–55. doi:10.1016/0025-5564(92)90002-E. PMID 1550993. 
  6. ^ Wichman HA, Millstein J, Bull JJ (2005). "Adaptive molecular evolution for 13,000 phage generations: a possible arms race". Genetics 170 (1): 19–31. doi:10.1534/genetics.104.034488. PMID 15687276. 
  7. ^ Dykhuizen DE, Dean AM (2004). "Evolution of specialists in an experimental microcosm". Genetics 167 (4): 2015–26. doi:10.1534/genetics.103.025205. PMID 15342537. 
  8. ^ Wick LM, Weilenmann H, Egli T (2002). "The apparent clock-like evolution of Escherichia coli in glucose-limited chemostats is reproducible at large but not at small population sizes and can be explained with Monod kinetics". Microbiology (Reading, Engl.) 148 (Pt 9): 2889–902. PMID 12213934. 
  9. ^ Jones LE, Ellner SP (2007). "Effects of rapid prey evolution on predator-prey cycles". J Math Biol 55 (4): 541–73. doi:10.1007/s00285-007-0094-6. PMID 17483952. 
  10. ^ Schlegel HG, Jannasch HW (1967). "Enrichment cultures". Annu. Rev. Microbiol. 21: 49–70. doi:10.1146/annurev.mi.21.100167.000405. PMID 4860267. 
  11. ^ Daughton CG, Hsieh DP (1977). "Parathion utilization by bacterial symbionts in a chemostat". Appl. Environ. Microbiol. 34 (2): 175–84. PMID 410368. 
  12. ^ Pfeiffer T, Bonhoeffer S (2004). "Evolution of cross-feeding in microbial populations". Am. Nat. 163 (6): E126–35. doi:10.1086/383593. PMID 15266392. 
  13. ^ G. J. Butler and G. S. K. Wolkowicz. (july 1986). "Predator-mediated competition in the chemostat" (PDF). J Math Biol. 24 (2): 67–191. doi:10.1007/BF00275997. http://www.springerlink.com/content/nwg1r43026l47q45/fulltext.pdf. 
  14. ^ Dykhuizen DE, Hartl DL (June 1983). "Selection in chemostats". Microbiol. Rev. 47 (2): 150–68. PMID 6308409. http://mmbr.asm.org/cgi/pmidlookup?view=long&pmid=6308409. 
  15. ^ Dykhuizen DE, Hartl DL (May 1981). "Evolution of Competitive Ability in Escherichia coli". Evolution 35 (3): 581–94. doi:10.2307/2408204. http://www.jstor.org/sici?sici=0014-3820(198105)35%3A3%3C581%3AEOCAIE%3E2.0.CO%3B2-0&origin=crossref. 
  16. ^ Bonomi A, Fredrickson AG (1976). "Protozoan feeding and bacterial wall growth". Biotechnol. Bioeng. 18 (2): 239–52. doi:10.1002/bit.260180209. PMID 1267931. 
  17. ^ de Crécy E, Metzgar D, Allen C, Pénicaud M, Lyons B, Hansen CJ, de Crécy-Lagard V (2007). "Development of a novel continuous culture device for experimental evolution of bacterial populations". Appl. Microbiol. Biotechnol. 77 (2): 489–96. doi:10.1007/s00253-007-1168-5. PMID 17896105. 
  18. ^ Zhang Z, Boccazzi P, Choi HG, Perozziello G, Sinskey AJ, Jensen KF (2006). "Microchemostat-microbial continuous culture in a polymer-based, instrumented microbioreactor". Lab Chip 6 (7): 906–13. doi:10.1039/b518396k. PMID 16804595. 
  19. ^ Van Hulle SW, Van Den Broeck S, Maertens J, Villez K, Schelstraete G, Volcke EI, Vanrolleghem PA (2003). "Practical experiences with start-up and operation of a continuously aerated lab-scale SHARON reactor". Commun. Agric. Appl. Biol. Sci. 68 (2 Pt A): 77–84. PMID 15296140. 

External links

  1. http://www.midgard.liu.se/~b00perst/chemostat.pdf
  2. http://www.rpi.edu/dept/chem-eng/Biotech-Environ/Contin/chemosta.htm
  3. A final thesis including mathematical models of the chemostat and other bioreactors
  4. A page about one laboratory chemostat design

 
 
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Leo Szilard (Hungarian–American physicist)
Turbidostat
Thistle tube

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Sci-Tech Dictionary. McGraw-Hill Dictionary of Scientific and Technical Terms. Copyright © 2003, 1994, 1989, 1984, 1978, 1976, 1974 by McGraw-Hill Companies, Inc. All rights reserved.  Read more
Sci-Tech Encyclopedia. McGraw-Hill Encyclopedia of Science and Technology. Copyright © 2005 by The McGraw-Hill Companies, Inc. All rights reserved.  Read more
Veterinary Dictionary. Saunders Comprehensive Veterinary Dictionary 3rd Edition. Copyright © 2007 by D.C. Blood, V.P. Studdert and C.C. Gay, Elsevier. All rights reserved.  Read more
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