Solution Mixing / Neutralization Calculator

Inspectable records

Ledger state

The current ledger marks this instrument verified clean within the source-bound verification corpus.

Area

Chemistry & Materials

Tranche

tranche-4

Evidence ID

t4-027

Ledger rows

1

No ledger note is attached.

Review findings

The concentration-mixing equation is conditionally correct, but the instrument claim of computing a general resulting concentration or pH is underspecified. The catalog should require solute identity and compatibility for mixing, acid/base identities and stoichiometric coefficients for neutralization, and pKa/equilibrium data for weak systems. It should honestly label the pH mode as limited to a defined model such as strong monoprotic acid/strong monoprotic base, with an explicit 25 °C or user-supplied temperature assumption.

Formula and scope findings

• C_final=(C1V1+C2V2)/(V1+V2) is valid only when both solutions contain the same conserved solute or analyte, concentrations use the same basis, and final volumes are treated as additive. It is not a general formula for combining arbitrary solutions.
• The description calls this a mass/mole balance, but the displayed equation is a mole balance; it does not account for density, mass fractions, volume contraction, reactions, precipitation, or dilution effects beyond additive volume.
• Comparing moles of H+ and OH- is sufficient for strong acid/strong base neutralization with known stoichiometry, but it is insufficient for weak acids or weak bases, polyprotic species, buffers, hydrolysis, or mixtures containing multiple acid-base equilibria.
• A resulting pH cannot be determined from only two volumes and concentrations unless acid/base identities, stoichiometry, strength assumptions, temperature, and relevant pKa or equilibrium constants are supplied. At equivalence, pH is not generally 7; that approximation applies to strong acid/strong base mixtures near 25 °C.
• The output description is ambiguous about whether final concentration means concentration of the original solute, leftover excess acid/base, total ionic concentration, or another species.

Unit assumptions

• V1 and V2 must use the same volume unit within each calculation; the test vectors convert milliliters to liters before multiplying by molarity.
• C1 and C2 are molar concentrations in mol/L for the displayed mole-balance equation.
• Volumes are assumed additive and solution volume change on mixing is neglected.
• Neutralization vectors assume monoprotic strong HCl and strong NaOH with 1:1 stoichiometry.
• pH is defined as -log10([H+] in mol/L relative to the 1 mol/L standard state).
• The equivalence-point vector assumes 25 °C, Kw=1.00e-14, and neglects activity coefficients; under those assumptions [H+]=1.00e-7 M and pH=7.00.

Boundary hardening

Recorded hazards

• Division by zero occurs if V1+V2=0; reject zero or negative total volume.
• Unit mismatch, such as multiplying molarity by milliliters without converting to liters, creates a factor-of-1000 error.
• The neutralization calculation must reject or explicitly handle negative concentrations and negative volumes.
• pH calculation is undefined if an excess-reagent concentration is zero unless water autoionization or an appropriate equilibrium model is used.
• Using pH=-log10(excess concentration) for a weak acid/base, polyprotic species, buffer, or equivalence point can be materially wrong.
• Acid/base stoichiometric coefficients must be included; a generic H+ versus OH- comparison is not sufficient for species such as H2SO4, H3PO4, Ca(OH)2, or weak electrolytes.
• The implementation needs an explicit policy for non-additive volumes, activity corrections, temperature dependence of Kw, precipitation, gas evolution, and reactions other than neutralization.

Errata and corrections

No applied erratum is attached to this unique-name record.

Inspectable example

4 review vectors are recorded. One source-bound sample is shown below.

{
  "inputs": {
    "operation": "same-solute_mixing",
    "solute": "NaCl",
    "C1_M": 0.2,
    "V1_L": 0.15,
    "C2_M": 0.05,
    "V2_L": 0.35
  },
  "expected_outputs": {
    "total_moles_mol": 0.0475,
    "total_volume_L": 0.5,
    "C_final_M": 0.095
  },
  "working": "n1=C1V1=0.200×0.150=0.0300 mol. n2=C2V2=0.050×0.350=0.0175 mol. n_total=0.0300+0.0175=0.0475 mol. V_total=0.150+0.350=0.500 L. C_final=n_total/V_total=0.0475/0.500=0.0950 M."
}

Related workflows

No source-defined multi-instrument workflow membership is recorded.

Sources and evidence

These pointers bind the page to evidence. They do not grant authority or collapse verification into deployment.

• VERIFIED_LEDGER.json · VERIFIED_CLEAN
• evidence-tranche4/tranche4-results.json