Source: https://guthlabs.ai/docs/instruments/solution-mixing-neutralization-calculator/
instrument / verified-clean
# Solution Mixing / Neutralization Calculator
The current ledger marks this instrument verified clean within the source-bound verification corpus.
Status: **VERIFIED_CLEAN**Lifecycle: **verified-clean**
## Inspectable records
[01**Overview**Purpose and lifecycle]()[02**Mechanism**Method and assumptions]()[03**Implementation**Binding and validation]()[04**Qualification**Evidence and errata]()
## 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`