INGENIA

ENV-01

Streeter–Phelps oxygen sag

DO deficit from first-order BOD and reaeration.

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River qualityStreeter–Phelps 1925

Governing equation

D=k1Lak2k1(ek1tek2t)+D0ek2tD=\dfrac{k_1 L_a}{k_2-k_1}(e^{-k_1 t}-e^{-k_2 t})+D_0 e^{-k_2 t}

where

k_1
Deoxygenation (1/d)
k_2
Reaeration (1/d)
L_a
Initial BOD (mg/L)
D_0
Initial deficit (mg/L)
t
Travel time (d)
D
DO deficit (mg/L)

Lecture brief

Historical brief

Streeter–Phelps (1925) oxygen sag, settling theory and Guldberg–Waage kinetics made water and air quality a rate problem. The lab computes sag, overflow and a snapshot of reactor mass balance. This sheet (ENV-01 — Streeter–Phelps oxygen sag) is the form associated with Streeter–Phelps 1925. Working symbols: k1k_1, k2k_2, LaL_a, D0D_0, tt \rightarrow DD. Streeter and Phelps coupled dL/dt = −k1 L with dD/dt = k1 L − k2 D, giving the classic sag curve.

Purpose

Purpose: compute DD from k1k_1, k2k_2, LaL_a, D0D_0, tt in Environmental via D=k1Lak2k1(ek1tek2t)+D0ek2tD=\dfrac{k_1 L_a}{k_2-k_1}(e^{-k_1 t}-e^{-k_2 t})+D_0 e^{-k_2 t} DO deficit from first-order BOD and reaeration. Use it when a real environmental question must be answered in SI before a code check.

Live realistic example

In symbols

Live case. Given k1=0.3001/dk_1 = 0.300\,\mathrm{1/d}, k2=0.6001/dk_2 = 0.600\,\mathrm{1/d}, La=20.000mg/LL_a = 20.000\,\mathrm{mg/L}, D0=1.000mg/LD_0 = 1.000\,\mathrm{mg/L}, t=2.000dt = 2.000\,\mathrm{d}, the governing relation D=k1Lak2k1(ek1tek2t)+D0ek2tD=\dfrac{k_1 L_a}{k_2-k_1}(e^{-k_1 t}-e^{-k_2 t})+D_0 e^{-k_2 t} yields D=5.254mg/LD = 5.254\,\mathrm{mg/L}. Point source, steady, well-mixed 1-D reach. Move a slider: the numbers are this situation, not a canned story.

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Inputs

Outputs

  • DO deficit D5.254 mg/L
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ENV-01 · pipe
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Narration of this film

Point source, steady, well-mixed 1-D reach.

Streeter and Phelps coupled dL/dt = −k1 L with dD/dt = k1 L − k2 D, giving the classic sag curve.

Reading speed

Watch on YouTube