Activated Sludge Process

QSDsan: Quantitative Sustainable Design for sanitation and resource recovery systems

This module is developed by:

This module is under the University of Illinois/NCSA Open Source License. Please refer to https://github.com/QSD-Group/QSDsan/blob/main/LICENSE.txt for license details.

class qsdsan.sanunits._activated_sludge_process.ActivatedSludgeProcess(ID='', ins: Sequence[AbstractStream] | None = None, outs: Sequence[AbstractStream] | None = (), thermo=None, init_with='WasteStream', F_BM_default=1, include_construction=False, N_train=2, T=308.15, X_i0=None, X_v=1210, X_e=15, X_w=10000, SLR=20, SF=4, aeration_power=1, q_hat=12, K=20, Y=0.5, b=0.396, f_d=0.8, COD_factor=1.42, q_UAP=1.8, q_BAP=0.1, k1=0.12, k2=0.09, K_UAP=100, K_BAP=85, F_BM={'Pump building': 1.1800826, 'Pumps': 1.1800826}, lifetime={'Pump pipe stainless steel': 15, 'Pump stainless steel': 15, 'Pumps': 15}, **kwargs)

A steady-state activated sludge process containing rectangular continuously stirred tank reactors and clarifiers for settling based on [1] (largely followed Example 6.2) and code scripts for [2] .

Single tank and clarifier are assumed to have the same width; pump/blower buildings are assumed to have the same width as the total tanks/clarifiers.

Parameters:

  • ins (Iterable) – Influent, air for aeration.

  • outs (Iterable) – Effluent, waste activated sludge sludge, gas emission.

  • N_train (int) – Number of treatment train, should be at least two in case one failing.

  • T (float) – Temperature in the aeration tank/anaerobic digester, [K].

  • X_i0 (float) – Inert biomass concentration in the influent, [mg VSS/L], will calculated based on inert_biomass of the current CompiledComponents if not provided.

  • X_v (float) – Reactor volatile suspended solids (biomass concentration in the aeration tank), referred to as mixed volatile liquor suspended solids (MLVSS, assumed to be the same as MLSS in [2]), [mg/L]. X_v = X_i + X_a (inert + active)

  • X_e (float) – Biomass concentration in the effluent, [mg VSS/L].

  • X_w (float) – Biomass concentration in the waste activated sludge, [mg VSS/L].

  • SLR (float) – Solids loading rate for the clarifier, [lb/ft2/d].

  • SF (float) – Safety factor to scale up the minimum solids retention time (SRT), should be larger than 1.

  • aeration_power (float) – Unit power usage for aeration, [kWh/kg O2].

  • q_hat (float) –

    Maximum specific rate of substrate utilization, [mg BOD/mg VSS/d], other important definitions are:

    • q_hat = mu_hat * Y (mu_hat is maximum specific growth rate, [1/time])

    • r_ut = -q_hat*(S/(K+S))*X_a (r_ut is rate of substrate utilization, [substrate mass/volume/time])

  • K (float) – Substrate concentration giving one-half the maximum rate, [mg COD/L].

  • Y (float) – Biomass yield, [mg VSS/mg BOD].

  • b (float) – Endogenous decay coefficient, [1/d].

  • f_d (float) – Fraction of the active biomass that is biodegradable.

  • COD_factor (float) – Biomass-to-COD conversion factor, [mg COD/mg VSS].

  • q_UAP (float) –

    Maximum specific rate of utilization-associated products degradation, [mg COD/mg VSS/d].

    SMP = UAP + BAP

    • SMP: soluble microbial products

    • UAP: utilization-associated products, produced directly from substrate metabolism

    • BAP: biomass-associated products, produced by basic metabolism

  • q_BAP (float) – Maximum specific rate of biomass-associated products degradation, [mg COD/mg VSS/d].

  • k1 (float) – UAP-formation coefficient, [mg COD/mg BOD].

  • k2 (float) – BAP-formation coefficient, [mg COD/mg VSS/d].

  • K_UAP (float) – Half-maximum rate concentrations for UAP, [mg COD/L].

  • K_BAP (float) – Half-maximum rate concentrations for BAP, [mg COD/L].

  • kwargs (dict) – Other attributes to be set.

References

See also

MATLAB codes used in ref 1, especially the system layout diagrams.

property A_clarifier

[float] Area of the clarifier, [ft2].

property D_WW

[float] Depth of the wet well for mixed liquor storage, [ft].

property D_tank

[float] Depth of the aeration tank, [ft].

property HRT

[float] Hydraulic retention time, [d].

property L_BB

[float] Length of the blower building, [ft].

property L_WW

[float] Length of the wet well for mixed liquor storage, [ft].

property L_tank

[float] Length of the aeration tank, [ft].

property N_train

[int] Number of treatment train, should be at least two in case one failing.

property Q

[float] Influent flow rate, [m3/d].

property Q_ras

[float] Return activated sludge flow rate, [m3/d].

property Q_was

[float] Waste activated sludge flow rate, [m3/d].

property R

[float] Sludge recycle ratio.

property V_tank

[float] Volume of the aeration tank, [ft3].

property W_BB

[float] Width of the blower building, [ft].

property W_PB

[float] Width of the pump building, [ft].

property W_WW

[float] Width of the wet well for mixed liquor storage, [ft].

property W_dist

[float] Width of the distribution channel, [ft].

property W_eff

[float] Width of the effluent channel, [ft].

property W_tank

[float] Width of the aeration tank, [ft].

auxiliary_unit_names: tuple[str, ...] = ('heat_exchanger',)

Auxiliary unit operation names.

property constr_access

[float] Extra room for construction access, [ft].

property excav_slope

[float] Slope for excavation (horizontal/vertical).

property freeboard

[float] Freeboard added to the depth of the reactor tank, [ft].

line: str = 'Activated sludge process'

class-attribute Name denoting the type of Unit class. Defaults to the class name of the first child class

run()

Run mass and energy balance. This method also runs specifications user defined specifications unless it is being run within a specification (to avoid infinite loops).

See also

_run, specifications, add_specification, add_bounded_numerical_specification

property t_slab

[float] Concrete slab thickness, [ft], default to be 2 in thicker than the wall thickness.

property t_wall

[float] Thickness of the wall concrete, [ft]. default to be minimum of 1 ft with 1 in added for every ft of depth over 12 ft.