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Alcohol Blending and Accounting, Volume II — Full-Source Literature Note
Alcohol Blending and Accounting, Volume II — Full-Source Literature Note

Alcohol Blending and Accounting, Volume II — Full-Source Literature Note

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Tags
BlendingBlendingMixture Experiment DesignMixture Experiment DesignProof as Flavor ControlProof as Flavor ControlDilutionDilutionQuality GatesQuality Gates
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Legacy Single Excerpt
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Legacy Associated Permanent Note
Content
Citation(s) & Footnote(s)
Book(s)
One Literature Note synthesizes one Source. It should be understandable without reopening the source while remaining traceable to exact Excerpts.

Source argument

Renewed extracted-text review covers PDF1–114 of281; this is not full examination. Fireman develops software-oriented hydrometer corrections, density tables and blend calculations. Useful themes include declared reference conditions, conserved ethanol mass, instrument-versus-liquid temperature effects and explicit numerical provenance. Native PDF images, complete worksheet cells and publisher collation remain inaccessible; reader-capture pages14/15 and106/107 repeat material.

Evidence map

Connect the exact Excerpts that support this note. Do not place unlocated quotations only in the page body.

Researcher synthesis

Proposed Academy use: a critical measurement-literacy companion alongside Strickland's Batch Distillation and the reviewed distillation engineering volumes. Distinguish physical mass balances, conventional apparent weights, reference-temperature ABV, instrument correction and software lookup approximations. Round-trip consistency, additional decimal places and matching a fitted table do not alone establish measurement accuracy. No public course implementation has been made.

Assessment

Consequential concerns: PDF28–30 hand-fits temperature offsets to known targets;31–38 extends water expansion to unrelated liquids based on density;52 and95–101 modifies the fitted formula's temperature origin without a demonstrated coefficient transformation;60 contains a tenfold volume discrepancy;75 calls equal starting liters of water and ethanol50%ABV despite contraction and adds relative percentages incorrectly;77 treats half-average table spacing as a maximum tolerance;79 tunes brass-weight density for reciprocity;103–110 uses a boosted density lookup as an air-composition conversion. These are author methods requiring independent validation. PDF111–114 usefully considers meniscus effects but114 assigns instrument sensitivity1.0 because the result seems plausible, so its numerical surface-tension correction is not validated. Relevant original images and full software are unavailable.

Completion checklist

Exactly one canonical Source is related.
Every consequential assertion is backed by one or more Excerpts.
Core Summary is complete.
Author Argument and Researcher Synthesis are distinct.
Limitations and open questions are recorded.
Candidate durable ideas have been promoted to Zettels.
Note Status is Complete only after this checklist passes.

Renewed review through endmatter — provisional critical synthesis

Accessible prose has now been read through PDF281. Appendix tables238–247,249–265,267,269,271,273–274 remain partial because extraction loses labels and cells;254–255 additionally require an untruncated reread. No original page images have been inspected. Supplied281 reader captures include near-duplicates14/15,106/107,214/215 and finish at publisher277/277; publisher collation is unverified. This supersedes the earlier114-page checkpoint, not the incomplete-review status.

PDF116–170 makes a useful case for separate ethanol, water and sugar inventories. However123–132 subtracts unlike units,139 totals mass fractions above100%,141 acknowledges a coincidental success and159 treats iterative convergence as accuracy. Solubility limits, algorithm limits and sensory sweetness are different matters. Numerical ternary-mixture predictions require independent experimental support.

PDF171–186 extends mixture polynomials above100%mass to accommodate apparent hydrometer readings. Apparent readings outside a scale's physical composition range do not validate out-of-domain thermodynamic predictions. PDF187–206 correctly distinguishes composition from density and bubbles from dissolved gas, but mixes Henry-constant conventions and converts standard gas volume into dissolved geometric volume without justification. Molar mass alone cannot determine partial molar volume or density-change direction. Fireman's gas constants match predictive, not adjusted, simulations in Schnabel/Vrabec/Hasse2005 Table4; statistical error bars are not total model accuracy.

PDF207–228 discusses gravity and historical mass standards. Local calibration corrects a proportional gravity factor throughout a linear scale range, not only at the calibration mass. The tidal treatment confuses relative force changes with absolute effects and concedes uncertainty. These digressions have limited Academy teaching value. The artifact-kilogram discussion reflects2018; NIST records the2019 replacement.

PDF229–236 uses oversimplified molecular-size and hydrogen-bond explanations; barometer correction is distinct from sea-level pressure reduction. PDF237 explicitly identifies abridged ABS tables and omitted official tables. PDFs242–250 alter and compare historical tables;251–263 are author-generated grids including supra100%values. PDFs266–274 mix independent tables, interpolation, software values and fitted buoyancy constants. Do not import these appendices as official calculator data.

PDF275–281 bibliography, credits and author material have been read. The linked software, video, external publications and full8000-row data are separate resources, not examined by reading their citations. Pinterest attribution does not establish public-domain rights.

Proposed Academy application: a private measurement-literacy exercise distinguishing mass, apparent weight, reference volume, instrument response, solubility and numerical convergence. Compare with the reviewed Batch Distillation and engineering volumes; verify any operational method against original metrology sources. No public implementation. Existing four citations and evidence records remain Needs Review; no blanket full-source endorsement.

Primary checks were bounded: NIST kilogram history and selected sections/tables of Schnabel et al., not full external-resource reviews.

Date
August 31, 2026
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Contributors
Payton D. FiremanPayton D. Fireman
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Source
No access
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Excerpts
Hydrometer readings are temperature- and surface-tension-sensitiveHydrometer readings are temperature- and surface-tension-sensitiveSugar changes mass, density, and displaced volumeSugar changes mass, density, and displaced volumeAlcohol-sugar mixtures have practical blending limitsAlcohol-sugar mixtures have practical blending limitsMulti-component blends require component-level accountingMulti-component blends require component-level accounting
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Zettels
Reproducible blend math begins with declared units and proof conditionsReproducible blend math begins with declared units and proof conditionsSugar and flavor additions invalidate simple two-component proof arithmeticSugar and flavor additions invalidate simple two-component proof arithmetic
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Citations
Hydrometer readings are temperature- and surface-tension-sensitive — PDF p. 111Hydrometer readings are temperature- and surface-tension-sensitive — PDF p. 111Sugar changes mass, density, and displaced volume — PDF p. 116Sugar changes mass, density, and displaced volume — PDF p. 116Alcohol-sugar mixtures have practical blending limits — PDF p. 145Alcohol-sugar mixtures have practical blending limits — PDF p. 145Multi-component blends require component-level accounting — PDF p. 168Multi-component blends require component-level accounting — PDF p. 168
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