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Merge updates in conventional wastewater configurations #103
Commits on May 28, 2023
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Simplified Step 4 (ASM2d-ADM1)
Simplified step 4 of ASM2d-ADM1 interface. Case II/III/IV, all need the same if else conditions. Also rectified an error message in Step 5(a).
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Correct checks for modified ASM2d-ADM1
X_S in ASM1 did not have N content, as it was taken care of by X_ND. However, in ASM2d X_S has non-zero N content, which we use as 'X_ND_asm1' in the code. Therefore, we no longer need the check (same with S_F). On the other hand N/P content in S_A now needs a check.
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Added check for P content in SI (ASM2d-ADM1)
Since in step 5(b) soluble inert P is assumed to be 0, a check needs to be put in place. Other changes made with regard to documentation.
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Updated check on COD/TKN/TP balance
Modified the function which checks simultaneous balance of nutrients. In ASM1-ADM1 only COD, and TKN were checked. Now the simultaneous balanced of COD, TKN, and TP would be verified.
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Checks for direct mapping of X_PAO, X_PHA, and X_PP
Deployed checks for N and P content in PAO across ASM2d and ADM1, since PAO is mapped directly. Similar checks were not deemed necessary for PHA, and PP.
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Updated charge balance (ASM2d-ADM1)
Updated charge balance to include inorganic phosphorous on the ADM1 side.
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Commits on May 29, 2023
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Updated checks and step 1(a) (ADM1-ASM2d)
Modified the function which checks simultaneous balance of nutrients. In ADM1-ASM1 only COD, and TKN were checked. Now the simultaneous balanced of COD, TKN, and TP would be verified. Also modified step 1(a) to update N balance
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Step 2 ADM1-ASM2d now includes TP balance
Changed step 2 to include P balance
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Commits on May 30, 2023
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Step 1(a) and 1(b): ADM1-ASM2d interface
Modified step 1(a) and 1(b) to include P balance.
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Commits on May 31, 2023
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Made changes in ADM1-ASM2d interface
Made several changes for ADM1-ASM2d interface to accommodate COD, TN, and TP balance.
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Commits on Jun 1, 2023
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ADM1-ASM2d interface completed
Completed transitions and checks on ADM1-ASM2d interface. COD, TN, and TP balance holds.
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Commits on Jun 2, 2023
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Modified charge balance (ADM1-ASM2d)
Modified charge balance to accommodate ADM1 and ASM2d.
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Commits on Jun 16, 2023
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Commits on Jul 2, 2023
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Commits on Jul 3, 2023
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Secondary clarifier design function
Added design function to secondary clarifier. For the same purpose, added new property 'height'.
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TEA default parameters (clarifier)
Adding default F_BM and lifetime values for pump, and metals.
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Commits on Jul 6, 2023
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Added design_pump function for pumping of influents. Used it in the main design function. The edits may seem weird as they were made in another desktop and copied here.
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Commits on Jul 7, 2023
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Adding mADM1toASM2d to junction
Adding the new junction class mADM1toASM2d, which acts as an interface between modified ADM1 and ASM2d. A copy of this class exists in 'junction_copy'.
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Adding ASM2dtomADM1 to junction
Adding the new junction class ASM2dtomADM1, which acts as an interface between ASM2d and modified ADM1. A copy of this class exists in 'junction_copy'.
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Commits on Jul 10, 2023
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Updated design and cost (Clarifier)
1. Updated design and cost functions of SC. 2. Added user-defined parameters for fixed design variables such as upflow_velocity, cylinderical_depth.
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Commits on Jul 11, 2023
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Design and cost function of thickener
Updated design and cost function of thickener. Diameter is based on solid loading rate. Otherwise the design and cost is similar to that of clarifier.
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Commits on Jul 12, 2023
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Changed order of import statements
Changed the order of import statements to use pump in clarifier. Co-Authored-By: Yalin <mailto.yalin.li@gmail.com>
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Changed dependency of SanUnits
Changed order of import statements to use pump in clarifier Co-Authored-By: Yalin <mailto.yalin.li@gmail.com>
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Updated design of secondary clarifier
Fixed typo (cylinderical to cylindrical). Made changes in design_pump() function of secondary clarifier.
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Changed dependency among SanUnits
Changed order of import statements to use pump in primary clarifier.
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Changed design_pump() function to allow use of pump (based on discussion with Yalin). Changed typo (cylinderical to cylindrical).
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Commits on Jul 13, 2023
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fix pump inf setting in
SecondaryClarifier
Now the 'design_pump' function has a influent stream which is copied from self._mixed, and its properties are updated accordingly. (Adapted based on Yalin's change to Primary clarifier)
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Commits on Jul 14, 2023
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Commits on Jul 16, 2023
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To be checked later (self._mixed definition)
Added the design and cost of screw conveyor to dewatering unit. Along with changes in the definition of self._mixed stream. Not sure about these changes, to be checked at a later date.
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Commits on Jul 18, 2023
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Utility power consumption now included. Co-Authored-By: Yalin <mailto.yalin.li@gmail.com>
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Commits on Jul 25, 2023
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Primary clarifier has just one pump (of type 'sludge') that is used to pump the waste sludge out of the unit. Usually no pump is employed for the influent and gravity is relied upon.
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Updated pump setting in secondary clarifier
Secondary clarifier would have two sludge pumps for RAS and WAS respectively. No pump required for influent.
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Set bare module factor for pumps
In both Primary and Secondary clarifier.
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Commits on Jul 26, 2023
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Added equipment (V notch weir)
Added V notch to both PC and SC. Added scraper to SC as well.
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Updated cost of mechanical thickener
Allowing multiple thickener units, and added cost of equipment (scraper).
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Commits on Aug 6, 2023
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Updated number of clarifiers based on design flow which in turn is based on total flow
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Made changes related to number of clarifiers for secondary sedimentation too
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Commits on Aug 7, 2023
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Cost of multiple pumps included based on number of clarifiers. The 'Q_mgd' argument in the WWTpump is changed.
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Made changes related to number of pumps in thickener, also added weir in equipments, and changed the default design flow based on metroWWTP.
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Set bare module factors for thickener and dewatering unit
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16
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Changed name of 'DewateringUnit' to 'Centrifuge'
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Commits on Aug 8, 2023
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Commits on Aug 10, 2023
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Made necessary changes to centrifuge
Changed pump settings and using exponent scaling for equipments in dewatering unit.
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Commits on Aug 11, 2023
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Changed pump settings in SC and undo some changes made by Yalin
1. Changed WWTpump settings in secondary clarifier based on Joy's suggestion. 2. Undo changes made by Yalin w.r.t. uf, of. uf is underflow (sludge), and of is overflow (treated effluent).
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Commits on Sep 11, 2023
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Added functions for estimation of aeration energy
Added functions to calculate oxygen demand for heterotrophs, autotrophs, and required airflow.
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Commits on Sep 12, 2023
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Updated calculation of O2 demand
Added TKN as the correct parameter while calculating oxygen demand in autotrophs
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Commits on Sep 18, 2023
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Added required power for blower
Added function to calculate required power for aeration.
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Commits on Sep 19, 2023
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Commits on Sep 20, 2023
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Commits on Sep 22, 2023
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In process of changing primary clarifier
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Commits on Sep 28, 2023
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Commits on Oct 3, 2023
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Commits on Oct 4, 2023
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'PrimaryClarifierBSM2' is the design of primary clarifier based on BSM2. While 'PrimaryClarifier' is the PC design we use in our centralized WRRFs.
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The lower limit of check on center feed depth has been modified to 10% based on advised range of upflow velocity
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Commits on Oct 5, 2023
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Updated clarifier design and cost estimates
Made several changes to secondary clarifier design, and added checks on calculated parameters based on MOP 8. Replicated few minor changes to PC as well.
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Commits on Oct 9, 2023
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Updates in design of SC: Area of clarifier either given by the user, or calculated from user defined influent TSS, influent flow, and SLR. A SLR is calculated based on simulation conditions, and the deviation is checked with design_SLR given by user.
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Commits on Oct 12, 2023
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Added concrete slab to clarifiers
Include the design and cost of concrete slab in both clarifiers. In secondary clarifier, the slab forms the bottom of the tank. In primary clarifier, the slab forms the conical portion of the tank.
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Updated design of gravity thickener (based on MOP 8) Have made several changes accordingly. Primarily, the diameter of the tank is limited to 22 m, and a design SLR is used to determine the surface area. The surface area governs the diameter. Changes in incinerator are commented for now.
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Commits on Oct 14, 2023
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Commits on Oct 15, 2023
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Commits on Oct 16, 2023
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Added bare module factor for slab concrete. Also added specific citation for primary clarifier.
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Updated thickener based on MOP-8
Updated thickener based on MOP-8.
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Commits on Oct 17, 2023
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Commits on Oct 18, 2023
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Commits on Oct 25, 2023
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Added BM factors to centrifuge
Added missing bare module factors to centrifuge.
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Update design, cost, and default design parameters for centrifuge.
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Commits on Oct 30, 2023
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Started adding design components for aeration tank.
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Commits on Oct 31, 2023
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A dummy unit to account for the design and cost of treatment chain in ASP.
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Assumed design Q_air (in m3/hr) for individual treatment chain as a user input.
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Commits on Nov 1, 2023
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Included pump design to treatment chain
Added a design recirculation flow, and a 'design_pump' function to facilitate the working of pump in treatment chain.
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Minor adjustments in treatment chain
Minor adjustments with documentation and debugging, made while integrating the unit with a centralized WRRF.
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Commits on Nov 3, 2023
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Commits on Nov 12, 2023
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Commits on Nov 13, 2023
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Commits on Nov 14, 2023
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Commits on Nov 15, 2023
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Revert "workaround to prevent negatives/better error prompting"
This reverts commit 9a439ce.
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Commits on Dec 6, 2023
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Discarding scraper capital cost because not sure whether the base flow is flow of sludge or effluent. Discarding scraper power because the scaling exponent is not correct.
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Removed scraper, edited capital of centrifuge
Removed scraper from thickener. Changed design of centrifuge since it is an equipment.
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Scaling centrifuge motor power
scaling the motor power in the centrifuge linearly w.r.t influent mass flowrate.
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Commits on Dec 7, 2023
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Coded function to compile pumping power demand in WRRF
New function to retrieve the pumping costs and other motor costs of all units involve in sludge management is coded.
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Commits on Dec 11, 2023
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Scaling the power of motor deployed in centrifuge linearly with respect to mass flowrate.
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Commits on Dec 18, 2023
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Change in default total static head
Changing H_ts based on Jeremy's recommendation.
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Commits on Dec 19, 2023
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Corrected logic flow, and modified ANSI dictionary
Made changes to select_pipe function to make sure that the selected inner diameter from ANSI is actually less than the calculated maximum diameter.
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Update documentation (select_pipe)
Changed documentation of select-pipe
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Commits on Jan 3, 2024
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Added thermo argument to waste stream to debug an error related to ASM1-ADM1 interface.
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Changing default head from 1 foot to 5 foot.
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Commits on Jan 4, 2024
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Added thermo to pumps in thickeners
Added thermo to pump in thickener and centrifuge to debug an error related to use of ASM-ADM interface.
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Commits on Jan 11, 2024
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Function to determine GHG emission in secondary treatment
Added new function that calculates GHG emission associated with secondary treatment processes like ASP.
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Revert "Function to determine GHG emission in secondary treatment"
This reverts commit c08375b.
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Function to determine GHG emission in secondary treatment
Added new function that calculates GHG emission associated with secondary treatment processes like ASP.
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Function to determine GHG emission during discharge
Added new function that calculates GHG emission associated with discharge of wastewater to natural waters.
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Commits on Jan 13, 2024
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More flexible GHG emission functions
Made the sludge and effluent wastestreams an iterable to make the GHG emission functions more flexible.
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Function to calculate CO2 emissions due to electricity consumption
Added new function that calculates GHG emission associated with consumption of electricity.
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Commits on Jan 24, 2024
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Added function to quantify GHG emission from sludge disposal
The function calculates methane emission from sludge disposal using a first-order decay equation.
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Commits on Jan 29, 2024
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updated sludge disposal GHG function
Changed function to calculate GHG emissions from sludge disposal to include emissions over project lifetime. Also using a more accurate proxy for W*DOC
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Commits on Jan 31, 2024
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Added new functions that return normalized energy consumption, and GHG emissions at WRRF.
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Optimized the code that calculates GHG emission from sludge disposal
Optimized the code to a less computationally demanding
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Updated secondary treatment GHG
Changed variables names to be consistent with IPCC norms.
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Commits on Feb 1, 2024
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The function now gives the breakdown of GHG emissions into type of gas (methane, nitrous oxide, carbon-di-oxide) for each of the five sources.
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Added function which calculates the sludge treatment and disposal costs, and another which compiles all operational costs.
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System is not required as an input to either of the functions.
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Commits on Feb 4, 2024
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Updated estimated range of sludge disposal costs
Updated the estimated range of sludge disposal costs based on new suggested reference.
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Updated GHG emissions from electricity
The equivalent GHG emissions are updated assuming medium voltage.
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Commits on Feb 5, 2024
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Accounted for methane emission from leftover sludge
Also added methane emissions due to leftover sludge at the end of project lifetime.
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Commits on Feb 13, 2024
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Changed the limits of analysis to satisfy mass balance.
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Commits on Feb 16, 2024
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Copied changes made by @joyxyz1994 on the bsm2 branch.
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Updated cost estimates due to unit
Changed cost estimates based on unit correction.
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Commits on Feb 19, 2024
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Facilitating uncertainty analysis
1. Added functions to facilitate uncertainty analysis on total operational cost and GHG emissions. 2. Corrected EFs for discharge based on IPCC report. 3. Made other minor changes.
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Commits on Feb 20, 2024
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Corrected typos in documentation
Edited out typos in documentation.
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Commits on Feb 21, 2024
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Revert "Adding file with initial conditions"
This reverts commit 098018e.
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Charge balance in ASM2d-ADM1 interface.
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Step 5(b) deployed to match S_I was incorrect. Corrections, and corresponding check have been made.
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ASM2d-mADM1 interface: check for direct mapping of PAO
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Added comments to enhance my understanding of charge balance.
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Changes to validate ASM2d-mADM1
Minor changes to prevent problems while validating the ASM2d-mADM1 interface.
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New class for enabling mADM1 interfaces
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Added H3PO4, and HPO4 2- acid/base pair to the mADM1 junction
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Commits on Mar 22, 2024
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Partially unresolved: When the ASM2d-mADM1 checks for TKN balance, it is not using updated value of ASM(X_I.i_N) even after I update while initializing the system. For now, I have made a modification in the interface itself.
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Partially unresolved: I need enthalpy of formation for ‘H3PO4/H2PO4-’ which I couldn’t find reliably. Filled in a placeholder value of 5000 J/mol for now.
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Commits on Mar 26, 2024
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Added name for contribution, and removed an irrelevant comment.
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Updated part of Step 1 of mADM1-ASM2d junction. Mapping of biomass to X_S.
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Updated part of Step 1 of mADM1-ASM2d junction. Mapping of particulate inert and biomass to X_I.
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Mapped soluble substrates: mADM1-ASM2d
Mapped soluble substrates while conserving COD, TKN, and TP.
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Commits on Mar 27, 2024
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Update pKa used to calculate delta of S_IP
pKa2 (7.20) should be used to calculate delta of S_IP, since it would be the reaction forming dominant specie between pH 5-8.
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Commits on Mar 28, 2024
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Replaced placeholder value for Delta H for dissociation of H2PO4- with correct enthalpy of formation.
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Commits on Apr 9, 2024
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I noticed that according to Flores Alsina et al. 2016 only SF is translated to amino acids and sugars, while acetate is directly mapped.
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According to Flores Alsina et al. 2016, X_I should be directly mapped by ensuring N and P content is same across ASM-ADM models
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According to Flores Alsina et al. 2016, X_I should be directly mapped by ensuring N and P content is same across ASM-ADM models.
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According to Flores Alsina et al. 2016 soluble inerts are also directly mapped.
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Reframing calling the function to avoid zero error.
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Commits on Apr 10, 2024
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Updating stoichiometry of new processes in P extension to ADM1.
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Defined stoichiometric coefficients for associated with K and Mg in P extension processes.
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Added mechanisms to conserve C, N, and P in process 23 and 25.
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Rate eqn in process description
Added rate equations to the description of processes.
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Removing rate equations description from ADM1 processes since they are not entirely correct.
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Commits on Apr 18, 2024
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Merge pull request #121 from QSD-Group/metro-bsm2
Minor updates to `metro`
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minor changes for temperature correction
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Soluble and particulate inert are now directly mapped.
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Minor updates where I have added functions for uncertainty analysis for Gates
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Made this change to debug an error related to dynamic pH calculation.
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Adding separate categories for emission sources for uncertainty analysis.
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