Wastewater Treatment Plant Design...

Chapter 07 - Receiving Waters...

Nomenclature...

Symbol Definition Units
L BOD remaining at time t mg / L
K 1 BOD reaction rate constant to base " e " 1 / day
t Time of flow day
k 1 BOD reaction rate constant to base " 10 " 1 / day
k T Value of k 1 at T O C 1 / day
k 20 Value of k 1 at 20 O C 1 / day
L O BOD ultimate mg / L
T L O Value of L O at T O C mg / L
20 L O Value of L O at 20 O C mg / L
T Temperature O C
C S Saturation concentration of oxygen in pure water mg / L
C Actual oxygen concentration in the stream mg / L
D Dissolved oxygen deficit ; D = C S - C mg / L
D O Value of D when t = 0 mg / L
k 2 Reaeration coefficient to base 10 1 / day
K L a Reaeration coefficient to base e 1 / day
K 2 Reaeration coefficient to base e 1 / day
L A BOD ultimate in Streeter - Phelphs equation when t = 0 mg / L
D A Dissolved oxygen deficit in stream when t = 0 mg / L
D C Dissolved oxygen deficit at critical point mg / L
t C Time when critical deficit occurs day
f Constant ; k 2 / k 1 -
DELTA t Time interval, time of flow between stations day or h
L A ( 1 ) and L A ( 2 ) Values of L A at stations ( 1 ) and ( 2 ) mg / L
V Mean velocity of flow in stream over distance between stations m / s
R Mean depth in stream between stations m

7.1. Introduction...

The effluents from wastewater treatment plants are eventually discharged either into the ground, if the works is very small, a river or lake, or directly to the sea.

7.2. BOD...

The assumption of a first order kinetic can be made as ;

( dL / dt ) = ( - K 1 ) ( L )

and ;

L = ( L O ) [ 10 ( - k 1 ) ( t ) ]

where L and L O are the carbonaceous BOD remaining at time t and the ultimate carbonaceous BOD, respectively, and K 1 and k 1 are the reaction rate constants to base " e " and base " 10 ", respectively. The change in BOD with temperature is twofold :

( a ) k 1 changes with temperature as ;

k T = ( k 20 ) ( THETA T - 20 )

where THETA is the temperature correction factor ( usually = 1.047 ).

( b ) L O also changes ;

T L O = ( 20 L O ) [ 1 + ( 0.02 ) ( T - 20 ) ]

The combination of the two effects of temperature changes can cause considerable changes in the total load to receiving waters.

Example 7-1 :

A BOD 5 ( 20 O C ) test was carried out on a river water sample and gave a BOD 5 value of 20 mg / L with a reaction rate constant of 0.18 1 / day. Calculate the BOD 5 at a temperature of 10 O C.

Calculation :

At 20 O C, BOD 5 = ( L O ) [ 1 - 10 ( - k 1 ) ( 5 ) ]

thus ;

L O ( 20 O C ) = ( 20.0 ) / ( 1 - 10 - 0.9 ) = 22.9 mg / L

and L O at 10 O C ;

L O ( 10 O C ) = ( 22.9 ) [ 1 + ( 0.02 ) ( - 10 ) ] = 18.3 mg / L

k 1 at 10 O C ;

k 1 ( 10 O C ) = ( 0.18 ) ( 1.047 10 - 20 ) = 0.11 1 / day

Thus ;

BOD 5 ( 10 O C ) = ( 18.3 ) [ 1 - 10 ( - 0.11 ) ( 5 ) ] = 13.1 mg / L

7.3. Oxygen Saturation and Dissolved Oxygen Deficits...

For fresh water the saturation dissolved oxygen level C S is given by ;

C S = 14.61 - 0.394 x T + 0.007714 x T 2 - 0.0000646 x T 3 ( mg / L )

where T is the temperature in O C. The dissolved oxygen deficit ( D , mg / L ) is the difference between C S and the actual oxygen concentration in the river ( C , mg / L ), i.e. ;

D = C S - C

From Chapter - 4 ;

( dC / dt ) = ( K L a ) ( C S - C )

( dD / dt ) = ( - K L a ) ( C S - C )

D = ( D O ) [ 10 ( - k 2 ) ( t ) ]

T k 2 = ( 20 k 2 ) [ 1.024 ( T - 20 ) ]

Example 7-2 :

If k 2 for a body of fresh water, initially 0 % saturated, is 0.6 1 / day at 20 O C, calculate the initial rate of change of dissolved oxygen in the water. Calculate also the initial rate of change if the water were originally at 0 O C.

Calculation :

( dC / dt ) = ( K L a ) ( C S - C )

K L a = ( 2.3 ) ( k 2 )

( C S - C ) = 0 when C = 0

Thus, at 0 O C ( C S - C ) = 14.6 mg / L and at 20 O C ( C S - C ) = 9.3 mg / L. Also at 20 O C, k 2 = 0.6 1 / day and at 0 O C, k 2 = ( 0.6 ) [ 1.024 ( 0 - 20 ) ] = 0.37 1 / day. Thus at 20 O C ;

( dC / dt ) = ( 2.3 ) ( 0.6 ) ( 9.3 ) = 12.8 mg / L . day

at 0 O C ;

( dC / dt ) = ( 2.3 ) ( 0.37 ) ( 14.6 ) = 12.4 mg / L . day

The ratio of the two iniitial aeration rates is 1.03.

7.4. Sag Curves in Rivers...

A very simple river oxygenation model is described by the equation of Streeter and Phelphs ;

( dD / dt ) = ( K 1 ) ( L ) - ( K 2 ) ( D )

i.e. the oxygen deficit will be increased by increasing the polluting load L and diminished by reaeration. Although this model neglects the effects of photosynthetic oxygen production ( by algae ) and the oxygen depletion by benthic ( bottom ) deposits, it can be surprisingly accurate, since these two neglected effects often cancel out. Streeter and Phelphs also showed that, by integrating the equation given just above, a general equation for the dissolved oxygen deficit at any time t could be written, namely ;

D = { [ ( k 1 ) / ( k 2 - k 1 ) ] ( L A ) [ 10 ( - k 1 ) ( t ) - 10 ( - k 2 ) ( t ) ] } + ( D A ) [ 10 ( - k 2 ) ( t ) ]

The general form of the equation is a " sag " curve.

Example 7-3 :

If k 1 and k 2 for a given river are 0.15 1 / day and 0.20 1 / day, respectively, calculate the dissolved oxygen deficits for the flow 6 days downstream if the river is initally 80 % saturated and has an ultimate BOD of 10 mg / L. The value of C S for the river is 12 mg / L.

Calculation :

For day 0 ;

D A = ( 0.20 ) ( 12 ) = 2.4 mg / L

For day 1 ;

D 1 = { [ ( 0.15 ) / ( 0.20 - 0.15 ) ] ( 10 ) [ 10 ( - 0.15 ) - 10 ( - 0.20 ) ] } + ( 2.4 ) [ 10 ( - 0.20 ) ] = 3.82 mg / L

For day 2 ;

D 2 = { [ ( 0.15 ) / ( 0.20 - 0.15 ) ] ( 10 ) [ 10 ( - 0.30 ) - 10 ( - 0.40 ) ] } + ( 2.4 ) [ 10 ( - 0.40 ) ] = 4.05 mg / L

Similarly, D 3 = 3.71 mg / L, D 4 = 3.16 mg / L, D 5 = 2.57 mg / L and D 6 = 2.04 mg / L. The shape of the curve of C versus time is shown in figure given below, which clearly indicates a minimum DO concentration somewhere around 1.7 to 1.8 days.



This critical value of the dissolved oxygen deficit D C which is reached at time t C occurs when ( dD / dt ) = 0 in the equation. Hence, putting D C = D and L = ( L A ) [ 10 ( - k 1 ) ( t C ) ] it can be shown that ;

D C = ( k 1 / k 2 ) ( L A ) [ 10 ( - k 1 ) ( t C ) ]

and occurs at ;

t C = [ 1 / ( k 2 - k 1 ) ] log 10 { ( k 2 / k 1 ) { 1 - ( D A / L A ) [ ( k 2 - k 1 ) / ( k 1 ) ] } }

For the conditions in the last example ;

t C = [ 1 / ( 0.20 - 0.15 ) ] log 10 { ( 0.20 / 0.15 ) { 1 - ( 2.4 / 10 ) [ ( 0.20 - 0.15 ) / ( 0.15 ) ] } } = 1.77 days

and ;

D C = ( 0.15 / 0.20 ) ( 10 ) [ 10 ( - 0.15 ) ( 1.77 ) ] = 4.07 mg / L

Example 7-4 :

A town discharges 0.05 m 3 / s of settled sewage with a BOD 5 of 150 mg / L ( for which the reaction rate is 0.17 1 / day at 20 O C ) into a river which has a minimum flow of 0.30 m 3 / s. The temperatures of the river and effluent are 15 O C and k 1 and k 2 for the river are found to be 0.20 1 / day and 0.30 1 / day by experiment, respectively. The dissolved oxygen contents of the effluent and river are 2.1 and 9.4 mg O 2 / L, respectively, prior to mixing and the BOD ultimate of the river is 2 mg / L. Calculate the magnitude of the critical dissolved oxygen deficit and the time at which it occurs.

Calculation :

For the sewage BOD 5 test ;

L O ( 20 O C ) = ( 150 ) / [ 1 - 10 ( - 0.17 ) ( 5 ) ] = 175 mg / L

Correcting L O to 15 O C gives ;

L O ( 15 O C ) = ( 175 ) [ 1 + ( 0.02 ) ( 15 - 20 ) ] = 158 mg / L

For the stream dilution of BOD ;

( 158 ) ( 0.05 ) + ( 2.0 ) ( 0.30 ) = ( L A ) ( 0.05 + 0.30 )

Thus ;

L A = 24.3 mg / L

For the stream dilution of dissolved oxygen ;

( 2.1 ) ( 0.05 ) + ( 9.4 ) ( 0.30 ) = ( C ) ( 0.05 + 0.30 )

C = 8.36 mg / L

The value of C S at 15 O C for fresh water is 10.2 mg / L ; thus D A = 10.2 - 8.4 = 1.8 mg / L. Thus ;

t C = [ 1 / ( 0.30 - 0.20 ) ] log 10 { ( 0.30 / 0.20 ) { 1 - ( 1.8 / 24.3 ) [ ( 0.30 - 0.20 ) / ( 0.20 ) ] } } = 1.60 days

and ;

D C = ( 0.20 / 0.30 ) ( 24.3 ) [ 10 ( - 0.20 ) ( 1.60 ) ] = 7.75 mg / L

Fair has proposed modifying Streeter and Phelphs equation by using a cipher f to represent ( k 2 / k 1 ). The time t C then becomes ;

t C = [ 1 / ( k 1 ) ( f - 1 ) ] log 10 { ( f ) [ 1 - ( D A / L A ) ( f - 1 ) ] }

and ;

D C = ( L A / f ) [ 10 ( - k 1 ) ( t C ) ]

7.5. Determination of k 1 and k 2 in Rivers...

The value of k 1 found in the stream differs from the values of k 1 found from the BOD tests not only because of the effects of temperature but also because turbulance, dilution, predation and UV disinfection of bacteria influence the oxidation rate. If the ultimate BODs for two stations 1 ( upstream ) and 2 ( downstream ) are known, then k 1 can be assessed from ;

k 1 = ( 1 / DELTA t ) log 10 [ ( L A ( 1 ) / L A ( 2 ) ) ]

For the determination of k 2 , Churchill has suggested that the k 2 ( 20 O C ) value is a function of the mean forward velocity V, ( Q / A ) in m / s, and the mean depth ( mean cross - sectional area / mean width ) R, in m, i.e. ;

k 2 ( 20 O C ) = ( 2.18 ) ( V 0.969 / R 1.673 )

Example 7-5 :

Table shown below gives the results of an investigation into a reach of a river. From the information provided, estimate whethera sag curve occurs in the reach, and, if so, determine its position and magnitude.

Calculation :

For the determination of k 1 ;

L A = 18.4 mg / L ; L B = 5.3 mg / L ; V MEAN = 3.9 / 13.1 = 0.30 m / s

DELTA t = ( 65 x 10 3 ) / [ ( 0.30 ) ( 8.64 x 10 4 ) ] = 2.5 days

k 1 = ( 1 / 2.5 ) log 10 ( 18.4 / 5.3 ) = 0.22 1 / day

R MEAN = 13.1 / 9.3 = 1.41 m

k 2 ( 20 O C ) = ( 2.18 ) ( 0.30 0.969 / 1.41 1.673 ) = 0.38 1 / day

k 2 ( 10 O C ) = ( 0.38 ) ( 1.024 10 - 20 ) = 0.30 1 / day

C S at 10 O C is 11.4 mg / L, thus D A = 11.4 - 6.3 = 5.1 mg / L. If a critical deficit occurs, it will occur at time t C where ;

t C = [ 1 / ( 0.30 - 0.22 ) ] log 10 { ( 0.30 / 0.22 ) { 1 - ( 5.1 / 18.4 ) [ ( 0.30 - 0.22 ) / ( 0.22 ) ] } } = 1.11 days

i.e. at a distance ( 0.30 m / s ) ( 86,400 s / day ) ( 1.11 day ) = 28,771 m = 28.8 km downstream of A the magnitude will be ;

D C = ( 0.22 / 0.30 ) ( 18.4 ) [ 10 ( - 1.11 ) ( 0.22 ) ] = 7.7 mg / L

Station Distance
( km )
Mean flow
( m 3 / s )
Mean cross - section
( m 2 )
Mean width
( m )
Ultimate BOD
( mg / L )
DO
( mg / L )
Temperature
( O C )
A 0.0 3.9 13.1 9.3 18.4 6.3 10
B 65.0 3.9 13.1 9.3 5.3 - 10