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Heavy Metal Index

and species is particularly important, because its material balance can be formulated purely in terms pH

Source

This source page is a mechanical bulk-ingest record for a PDF in the methylmercury infant-formula research pull.

Page snapshot
Cited by4 pages
Metals measured1
Evidence tierB
Year2022

Overview

This source page is a mechanical bulk-ingest record for a PDF in the methylmercury infant-formula research pull. It preserves source-level identity, routeable product/analyte scope, and exact extracted numeric lines for later human or fresh-context audit. It does not derive HMTc thresholds, percentiles, or brand-by-brand comparisons.

Key numbers

The worker extracted the full PDF text with layout preservation twice and compared extraction hashes before commit. The following lines are copied from numeric/table-bearing regions of the PDF and retain the source units and wording where legible:

  • Part 5: Ionic speciation
  • WASH R&D Centre, School of Engineering, University of KwaZulu-Natal, Durban 4041, South Africa
  • Water Research Group, Department of Civil Engineering, University of Cape Town, Rondebosch 7700, South Africa
  • of a plant-wide wastewater treatment model as an example. Received: 3 July 2019
  • explained in Part 1 (Brouckaert et al., 2021a), the overall model is divided into a kinetically controlled computational efficiency
  • calculation involves algebraic equations only. Commons Attribution 4.0
  • Aqueous ionic speciation models such as MINTEQA2 (Allison et al., 2009) and PHREEQC (Parkhurst
  • to the scope of each biochemical model to reduce the computational burden. Lizzaralde et al. (2014)
  • model used in the anaerobic digestion model of Brouckaert et al. (2010). Only acid/base and ion-
  • ISSN (online) 1816-7950 32
  • (Loewenthal et al., 1994). Additionally, sodium, potassium, of measurable quantities. However, this apparent advantage is
  • municipal wastewaters. The ionic model therefore has 12 ionic up from pure chemicals. Measurements on wastewater samples
  • components for the mass balances: H+, Na+, K+, Ca2+, Mg2+, NH4+, very seldom cover all the ions present, and, even when they
  • Cl−, Ac−, Pr−, CO32−, SO42− and PO43−. Sulphide, NO2−, NO3− and do, measurement errors upset the charge balance. The solution
  • iron (Fe2+, Fe3+) were not included in this the model, as partial state is very sensitive to the H+ concentration, so the measured
  • components (HS−, NO2−, NO3−, Fe2+, Fe3+, Al3+), but more than composition measurements.
  • The concentrations of the 42 ionic species are related to the
  • The source of information was the minteq.v4.dat database concentrations of the 12 components by a set of 12 stoichiometric
  • distributed with PHREEQC. PHREEQC automatically includes all balances, together with a set of 30 equilibrium relationships which
  • (5, 7 and 9). Species were selected that contributed at least 2% to
  • the inventory of any component in at least one of the model runs. In Eq. 1 the square brackets indicate molal concentrations, italics
  • So, for example, the species NaHCO3 had to amount to at least indicate species, and Roman typeface indicates a component.
  • 2% of the total Na+, H+ or CO32− in at least one of the simulated (Pr−) is also referred to as a total concentration, as it is the sum of
  • solutions. The 42 ionic species that were selected in this way were: the concentrations of all species present that include Pr−.
  • MgHCO3+, H2PO4−, MgPO4−, CaPO4−, MgHPO4, CaHPO4, CaSO4, from more than one component (e.g. HPr, CaPr+). Take HPr, for
  • MgSO4, CaOH+, MgOH+, NH4SO4−, NaHPO4−, NaCO3−, NaHCO3, example. Its entry in Table 1 corresponds to the formation reaction
  • MgH2PO4+, CaAc+, NaAc, MgAc+, CaPr+, MgPr+ and NaSO4−, H+ + Pr− → HPr, with the corresponding equilibrium relationship:
  • where the last 24 in the list are often referred to as ion pairs. Note {HPr }  K H Pr  {H  }  {Pr  } (2)
  • to distinguish them from components. In Eq. 2, {…} indicates the activity of the species, and KHPr is an
  • Table 1 presents the reaction scheme in a form known as a tableau, equilibrium constant, which is a function of temperature only,
  • matrix contains the stoichiometric coefficients for the formation Table 1.
  • at 25°C or 298.15°K (obtained from the minteq.v4.dat database).
  • linear equations. Whether this level of complexity is really required {Pr  }   Pr  (Pr  ) (4)
  • a great deal of investigation to answer fully. If alkalinity and pH Equation 4 can be dimensionally confusing, since {Pr−} and γPr are
  • to the ion pairs (Solon et al., 2015). As will be discussed in the next {i }   i  (i )( io)
  • which is defined so that (iO) = 1 mol/kg for all species i. This
  • al., 2015) prefer a different formulation of the set of speciation (e.g. KHPr in Eq. 2). By convention (iO) = 1, whatever concentration
  • equations, in which H+ in the tableau is replaced by the charge units are used, so the form of Eq. 4 remains the same if the units
  • Table 1. Tableau representation of the Brouckaert et al. (2010) speciation model
  • CaSO4 1 1 2.36 7 100
  • NaSO4- 1 1 0.73 1 000
  •  0. 3 I  (5) variables. Since this happens only once at the beginning of a

Methods (brief)

  • model used in the anaerobic digestion model of Brouckaert et al. (2010). Only acid/base and ion-
  • close to equilibrium. These were represented in the anaerobic digestion model as rate-controlled
  • anaerobic digestion model. An anaerobic digester typically includes the carbonate, phosphate,
  • municipal wastewaters. The ionic model therefore has 12 ionic up from pure chemicals. Measurements on wastewater samples
  • an approximation in the anaerobic digestion model, and dosing of further considerations have to be used to establish an appropriate
  • the anaerobic digestion model might be expected to encounter
  • for the anaerobic digestion model is a question that would require
  • solution obtained at the previous time step provides an excellent A typical set of measurements on a wastewater sample will not
  • appropriately included in the kinetically limited sub-model. anaerobic digestion model. Proceedings 12th IWA Anaerobic
  • In setting up an equilibrium speciation sub-model, modellers Digestion Conference (AD12), Guadalajara, Mexico, 1–4 Nov 2010.
  • KwaZulu-Natal Anaerobic Digestion Model (1994) Modelling struvite precipitation in anaerobic treatment
  • {i} activity of species i, dimensionless anaerobic digestion. Water Res. 70 235–245. https://doi.org/10.1016/j.
  • The anaerobic digestion model of Brouckaert et al. (2010) whereas PCO2 is calculated from the gas phase mass balance. The

Implications

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Verification notes

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Update history

The five most recent substantive edits to this page, classified major (evidence or structure moved), correction (a published value or statement was wrong and has been fixed), or minor (narrative rewritten without changing the underlying evidence). Each description is derived from what the edit did to this page; the linked commit is the authoritative record, routine regeneration passes are excluded, and the full version history lives in git. When DOI minting comes online (see schema docs), each entry below will also link to a version-pinned DataCite DOI.

CommitDateChangeDescription
3171d062026-08-02major1 section added
bc84bfc2026-08-02major6 sections added; narrative text revised