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McKay, Donald. "Front matter" Multimedia Environmental Models ...

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Worked Example 2.13<br />

Consider a river into which the 1.8 million population of a city discharges a<br />

detergent at a rate of 1 pound per capita per year, i.e., the discharge is 1.8 million<br />

pounds per year. The aim is to calculate the concentrations at distances of 1 and 10<br />

miles downstream from a knowledge of the degradation rate of the detergent and<br />

the constant downstream flow conditions, which are given below. This can be done<br />

in Eulerian or Lagrangian coordinate systems. The input data are first converted to<br />

SI units.<br />

The river flow rate is Uhw, i.e., 18270 m 3 /h. The rate constant k is 0.693/t 1/2, i.e.<br />

0.096 h –1 . When the detergent mixes into the river, the concentration will be C O or<br />

E/(Uhw) or 5.1 g/m 3 .<br />

Lagrangian Solution<br />

A parcel of water that maintains its integrity, i.e., it does not diffuse or disperse,<br />

will decay according to the equation<br />

©2001 CRC Press LLC<br />

C = C O exp(–kt)<br />

where t is the time from discharge. At 1 mile (1609 m), the time t will be 1609/U<br />

or 1.47 h, and at 10 miles, it will be 14.7 h.<br />

Substituting shows that, after 1 and 10 miles, the concentrations will be 4.4 and<br />

1.24 g/m 3 . The chemical will reach half its input concentration when t is 0.693/k or<br />

7.2 h, which corresponds to 7900 m or 4.92 miles. This Lagrangian solution is<br />

straightforward, but it is valid only if conditions in the river remain constant and<br />

negligible upstream-downstream dispersion occurs.<br />

Eulerian Solution<br />

Discharge rate 1.8 ¥ 106 lb per year 93300 g/h (E)<br />

River flow velocity 1 ft/s 1097 m/h (U)<br />

River depth 3 ft 0.91 m (h)<br />

River width 20 yards 18.3 m (w)<br />

Degradation half-life 0.3 days 7.2 h (t1/2) We now simulate the river as a series of connected reaches or segments or well<br />

mixed lakes, each being L or 200 m long. Each reach thus has a volume V of Lhw<br />

or 3330 m 3 . A steady-state mass balance on the first reach gives<br />

input rate = UhwC O = output rate = UhwC 1 + VkC 1<br />

where C O and C 1 are the input and output concentrations. C 1 is also the concentration<br />

in the segment. It follows that

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