Give step-by-step solution with explanation and final answer:
{give me the answer without using bulling-points}Consider a reservoir that receives a continuous inflow of wastewater with a specific biochemical
Reacration, K, oxygen demand (BOD) concentration, Li,
Ons Lig vl and flow rate, Q;,. The BOD within the
TR o B reservoir is subject to first-order kinetics
rganic 8 g
matter k; Settling of of decay (kg) and settling (ks) whey while
particulate BOD Lows Lout being continuously mixed. The outflow,
Ga I) outflow, Qout, has a BOD concentration
E— - 7 Loy. The system eventually reaches a
steady state.
(a) Sketch the qualitative time-dependent profile of the BOD concentration, L(t), within the
reservoir, starting from an initial concentration Ly at t = 0 and approaching a steady-state
value Ly. By deriving the governing differential equation from a mass balance as, show the
expression for Lo.
(b) Plot the steady-state BOD removal efficiency, £ = (Lin — Loo)/Lin, as a function of the
hydraulic residence time, 7 = V/Q, by developing the equation relating E to 7 and the overall
removal rate constant K = kq + ks.
(c) Illustrate the impact of temperature on the overall removal rate constant K and, consequently,
on the steady-state BOD concentration Loo, by developing the Arrhenius relationship for K(T').
Question:
Give step-by-step solution with explanation and final answer:
{give me the answer without using bulling-points}Consider a reservoir that receives a continuous inflow of wastewater with a specific biochemical
Reacration, K, oxygen demand (BOD) concentration, Li,
Ons Lig vl and flow rate, Q;,. The BOD within the
TR o B reservoir is subject to first-order kinetics
rganic 8 g
matter k; Settling of of decay (kg) and settling (ks) whey while
particulate BOD Lows Lout being continuously mixed. The outflow,
Ga I) outflow, Qout, has a BOD concentration
E— - 7 Loy. The system eventually reaches a
steady state.
(a) Sketch the qualitative time-dependent profile of the BOD concentration, L(t), within the
reservoir, starting from an initial concentration Ly at t = 0 and approaching a steady-state
value Ly. By deriving the governing differential equation from a mass balance as, show the
expression for Lo.
(b) Plot the steady-state BOD removal efficiency, £ = (Lin — Loo)/Lin, as a function of the
hydraulic residence time, 7 = V/Q, by developing the equation relating E to 7 and the overall
removal rate constant K = kq + ks.
(c) Illustrate the impact of temperature on the overall removal rate constant K and, consequently,
on the steady-state BOD concentration Loo, by developing the Arrhenius relationship for K(T').
This is AI generated Response.
Asked by: Francis
Created at: 2026-01-29 10:09:58
Final Answer:
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### (a) Time-dependent BOD Profile and Steady-State Expression
Let \( L(t) \) be the BOD concentration in the reservoir at time \( t \).
Initial concentration: \( L() = L_ \).
At steady state (as \( t \to \infty \)): \( L(t) \to L_\infty \).
**Mass balance on the reservoir:**
\[
\text{Accumulation} = \text{In} - \text{Out} - \text{Decay} - \text{Settling}
\]
\[
V \frac{dL}{dt} = Q_{in}L_{in} - Q_{out}L - V k_d L - V k_s L
\]
Assume \( Q_{in} = Q_{out} = Q \):
\[
V \frac{dL}{dt} = Q L_{in} - Q L - V (k_d + k_s)L
\]
\[
\frac{dL}{dt} = \frac{Q}{V}(L_{in} - L) - (k_d + k_s)L
\]
\[
\frac{dL}{dt} = \frac{Q}{V}L_{in} - \left(\frac{Q}{V} + k_d + k_s\right)L
\]
Define the hydraulic residence time \( \tau = \frac{V}{Q} \), and \( K = k_d + k_s \):
\[
\frac{dL}{dt} = \frac{1}{\tau}L_{in} - \left(\frac{1}{\tau} + K\right)L
\]
At steady state (\( \frac{dL}{dt} = \)):
\[
= \frac{1}{\tau}L_{in} - \left(\frac{1}{\tau} + K\right)L_\infty
\]
\[
\left(\frac{1}{\tau} + K\right)L_\infty = \frac{1}{\tau}L_{in}
\]
\[
L_\infty = \frac{L_{in}}{1 + K\tau}
\]
So, the BOD concentration \( L(t) \) will exponentially decay from \( L_ \) to \( L_\infty \).
---
### (b) Steady-State BOD Removal Efficiency
Removal efficiency is:
\[
E = \frac{L_{in} - L_\infty}{L_{in}}
\]
Substitute \( L_\infty \):
\[
E = 1 - \frac{L_\infty}{L_{in}} = 1 - \frac{1}{1 + K\tau}
\]
\[
E = \frac{K\tau}{1 + K\tau}
\]
This shows that removal efficiency increases with higher \( K \) (removal rate) and higher \( \tau \) (residence time).
---
### (c) Impact of Temperature on \( K \) and \( L_\infty \)
The removal rate constant \( K \) is temperature dependent. The Arrhenius equation for \( K \) is:
\[
K(T) = K_{20} \theta^{(T-20)}
\]
where \( K_{20} \) is the rate constant at \( 20^\circ\text{C} \), \( \theta \) is typically 1.03–1.07, and \( T \) is temperature in °C.
As \( T \) increases, \( K(T) \) increases, which leads to a lower steady-state BOD \( L_\infty \):
\[
L_\infty = \frac{L_{in}}{1 + K(T)\tau}
\]
Higher temperature → higher \( K \) → lower \( L_\infty \), meaning better BOD removal at higher temperatures.
---
**Summary of Answers:**
(a) The BOD concentration \( L(t) \) decays exponentially from \( L_ \) to \( L_\infty = \frac{L_{in}}{1 + K\tau} \).
(b) The steady-state BOD removal efficiency is \( E = \frac{K\tau}{1 + K\tau} \).
(c) As temperature increases, the removal rate constant \( K \) increases according to \( K(T) = K_{20}\theta^{(T-20)} \), thereby decreasing \( L_\infty \) and improving removal efficiency.
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