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Kinetics of the Steady-State Bacterial Culture. I. Mathematical Model E. J. MARTIN, Public Health Service Trainee D. R. WASHINGTON, Associate Professor Department of Environmental Engineering Rensselaer Polytechnic Institute Troy, New York SUMMARY A mathematical model for the continuous flow steady-state bacterial culture is presented which permits the experimental determination of carbon transfer rates within the system by use of radioactive tracer techniques. The transfer rates are specific for hydraulic loading rates, feed concentrations, type of organism and the substrate. The model is established with a view toward elucidating the effect of changes in dilution rate on the carbon transfer rates. PRESENT THEORY The continuous culture of microorganisms, particularly the behavior in the steady-state, is difficult to treat experimentally since the parameters normally monitored to observe the functioning of biological systems (e.g., flow rate, substrate concentration, etc.) remain constant with time as long as there are no environmental disturbances. Research has indicated the need for the application of radioisotope techniques to the continuous culture to study the changes occurring within the system. The theory of such systems has been presented in the past and is composed of equations describing both the organism balance and substrate balance within the culture vessel (1,2,3). Mass Balance The rate of change of mass of organisms in the reactor can be described by the balance equation (individual terms are rates) mass change = growth - loss in effluent - death or rtM.' MMa'-DMa,-f(S1, Ma') (1) dMa' dt where Ma' is the total active organism weight in the culture vessel at time, t, u is the specific growth rate, D is the dilution rate equal to flow rate divided by volume of the reactor (V) and S-^ is the concentration of organic material in solution in the reactor at time, t. The function describing the "death" contribution has been discussed by Moser (4) and Powell (5) and is generally taken to be merely some function of the mass of organisms present, even though it is probably a function of the concentration of substrate (Sj) as well. The death rate of the organisms could be ef- - 724 -
Object Description
Purdue Identification Number | ETRIWC196457 |
Title | Kinetics of the steady-state bacterial culture. I. Mathematical model |
Author |
Martin, E. J. (Edward J.) Washington, D. R. (Donald R.) |
Date of Original | 1964 |
Conference Title | Proceedings of the nineteenth Industrial Waste Conference |
Conference Front Matter (copy and paste) | http://earchives.lib.purdue.edu/u?/engext,11114 |
Extent of Original | p. 724-737 |
Series |
Engineering extension series no. 117 Engineering bulletin v. 49, no. 1(a)-2 |
Collection Title | Engineering Technical Reports Collection, Purdue University |
Repository | Purdue University Libraries |
Rights Statement | Digital object copyright Purdue University. All rights reserved. |
Language | eng |
Type (DCMI) | text |
Format | JP2 |
Date Digitized | 2009-05-19 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Resolution | 300 ppi |
Color Depth | 8 bit |
Description
Title | page 724 |
Collection Title | Engineering Technical Reports Collection, Purdue University |
Repository | Purdue University Libraries |
Rights Statement | Digital object copyright Purdue University. All rights reserved. |
Language | eng |
Type (DCMI) | text |
Format | JP2 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Transcript | Kinetics of the Steady-State Bacterial Culture. I. Mathematical Model E. J. MARTIN, Public Health Service Trainee D. R. WASHINGTON, Associate Professor Department of Environmental Engineering Rensselaer Polytechnic Institute Troy, New York SUMMARY A mathematical model for the continuous flow steady-state bacterial culture is presented which permits the experimental determination of carbon transfer rates within the system by use of radioactive tracer techniques. The transfer rates are specific for hydraulic loading rates, feed concentrations, type of organism and the substrate. The model is established with a view toward elucidating the effect of changes in dilution rate on the carbon transfer rates. PRESENT THEORY The continuous culture of microorganisms, particularly the behavior in the steady-state, is difficult to treat experimentally since the parameters normally monitored to observe the functioning of biological systems (e.g., flow rate, substrate concentration, etc.) remain constant with time as long as there are no environmental disturbances. Research has indicated the need for the application of radioisotope techniques to the continuous culture to study the changes occurring within the system. The theory of such systems has been presented in the past and is composed of equations describing both the organism balance and substrate balance within the culture vessel (1,2,3). Mass Balance The rate of change of mass of organisms in the reactor can be described by the balance equation (individual terms are rates) mass change = growth - loss in effluent - death or rtM.' MMa'-DMa,-f(S1, Ma') (1) dMa' dt where Ma' is the total active organism weight in the culture vessel at time, t, u is the specific growth rate, D is the dilution rate equal to flow rate divided by volume of the reactor (V) and S-^ is the concentration of organic material in solution in the reactor at time, t. The function describing the "death" contribution has been discussed by Moser (4) and Powell (5) and is generally taken to be merely some function of the mass of organisms present, even though it is probably a function of the concentration of substrate (Sj) as well. The death rate of the organisms could be ef- - 724 - |
Resolution | 300 ppi |
Color Depth | 8 bit |
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