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Oxygen Response and Aeration in Steams ROBERT DRESNACK, Assistant Professor IVAN METZGER, Professor Department of Civil Engineering Newark College of Engineering Newark, New Jersey INTRODUCTION The response of oxygen to transient pollutional inputs may be described by a numerical solution of a partial differential equation describing the basic material balance. The stability of the method of solution depends on the relative values of the diffusive and convective fluxes while the actual response is most sensitive to lower-order terms. Since stability is insured for the range of relative values of the flux terms which apply to streams, attention is focused on the sensitivity of response to the lower-order terms such as aeration. A physical model of the mechanism of aeration is based on the concept that an interfacial liquid film is in a continuous state of random renewal by turbulent fluid from beneath the surface. BASIC EQUATIONS The temporal and spacial distribution of BOD in a stream for one-dimensional flow is given by * 9^ = D, 9!k - H9L . (K + K3)L t La (1) at LaiF ax where L is the BOD concentration at any time, t. at a location x. The first term in Equation 1 describes the effect of longitudinal dispersion, DL, and the second term, that of velocity, U. The decay or production represented by the third term is assumed to follow first order kinetics which is the sum of two distinct processes. A continuing decay due to oxidation is represented by K,. All other processes, such as settling or resuspension, are represented by K3 which can be either positive or negative. The last term, La, describes a uniform addition of BOD along a stretch. A similar equation describing the temporal and spacial distribution of dissolved oxygen, C, is |f = °L H -^-K.L.K^-O-DB (2) where the first three terms are analogous to those in Equation 1. Atmospheric aeration is described by a first-order reaction with coefficient, K2, and a driving force equal to the difference between the saturation concentration of oxygen, Cs, and the concentration C in the stream at any time. The net rate of addition of oxygen by all other processes is represented by Dg. This term is positive if the predominant processes are the removal of oxygen by plant respiration and the oxygen demand of the bottom sludge or negative if photosynthetic addition predomi- - 262 -
Object Description
Purdue Identification Number | ETRIWC196823 |
Title | Oxygen response and aeration in streams |
Author |
Dresnack, Robert Metzger, Ivan |
Date of Original | 1968 |
Conference Title | Proceedings of the 23rd Industrial Waste Conference |
Conference Front Matter (copy and paste) | http://earchives.lib.purdue.edu/u?/engext,15314 |
Extent of Original | p. 262-274 |
Series |
Engineering extension series no. 132 Engineering bulletin v. 53, no. 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 | 2009-05-20 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Resolution | 300 ppi |
Color Depth | 8 bit |
Description
Title | page 262 |
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 | Oxygen Response and Aeration in Steams ROBERT DRESNACK, Assistant Professor IVAN METZGER, Professor Department of Civil Engineering Newark College of Engineering Newark, New Jersey INTRODUCTION The response of oxygen to transient pollutional inputs may be described by a numerical solution of a partial differential equation describing the basic material balance. The stability of the method of solution depends on the relative values of the diffusive and convective fluxes while the actual response is most sensitive to lower-order terms. Since stability is insured for the range of relative values of the flux terms which apply to streams, attention is focused on the sensitivity of response to the lower-order terms such as aeration. A physical model of the mechanism of aeration is based on the concept that an interfacial liquid film is in a continuous state of random renewal by turbulent fluid from beneath the surface. BASIC EQUATIONS The temporal and spacial distribution of BOD in a stream for one-dimensional flow is given by * 9^ = D, 9!k - H9L . (K + K3)L t La (1) at LaiF ax where L is the BOD concentration at any time, t. at a location x. The first term in Equation 1 describes the effect of longitudinal dispersion, DL, and the second term, that of velocity, U. The decay or production represented by the third term is assumed to follow first order kinetics which is the sum of two distinct processes. A continuing decay due to oxidation is represented by K,. All other processes, such as settling or resuspension, are represented by K3 which can be either positive or negative. The last term, La, describes a uniform addition of BOD along a stretch. A similar equation describing the temporal and spacial distribution of dissolved oxygen, C, is |f = °L H -^-K.L.K^-O-DB (2) where the first three terms are analogous to those in Equation 1. Atmospheric aeration is described by a first-order reaction with coefficient, K2, and a driving force equal to the difference between the saturation concentration of oxygen, Cs, and the concentration C in the stream at any time. The net rate of addition of oxygen by all other processes is represented by Dg. This term is positive if the predominant processes are the removal of oxygen by plant respiration and the oxygen demand of the bottom sludge or negative if photosynthetic addition predomi- - 262 - |
Resolution | 300 ppi |
Color Depth | 8 bit |
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