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SKILL verified Apache-2.0 Self-run

Thermo Process Properties

skill-jskherman-engg-skills-thermo-process-properties · by jskherman

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$ agentstack add skill-jskherman-engg-skills-thermo-process-properties

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No issues found. Passed automated security review. · v0.1.0 How review works →

  • Prompt-injection patterns
  • Secret / credential exfiltration
  • Dangerous shell & filesystem operations
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  • Known-malicious package signatures

What it can access

  • Network access No
  • Filesystem access No
  • Shell / process execution No
  • Environment & secrets No
  • Dynamic code execution No

From automated source analysis of v0.1.0. “Used” means the capability is present in the source — more access means more to trust, not that it’s unsafe.

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About

Thermodynamic Property Calculations

Overview

Caleb Bell library wrapper utilities. Implements:

  • recommend: property-method recommendation given components and

application context.

  • costald-density: COSTALD (saturated) or COSTALD_compressed mixture

liquid density for light hydrocarbons.

  • pr-translated-eos: instantiate thermo.eos_mix.PRMIXTranslatedPPJP

with reported molar volumes, Z-factors, and departure functions.

  • iapws-state / iapws-saturation: pure water / steam properties.

Heuristics for method selection are transparent and built from public sources (DWSIM, Carlson, AVEVA / Aspen training material). No proprietary defaults are reproduced.

Prerequisites

  1. uv available.
  2. On first use, the script writes LICENSE_NOTIFICATION.txt listing

the upstream library terms.

When to Use

  • Picking a property method for a flowsheet zone.
  • Estimating LPG liquid density at storage / vessel conditions (COSTALD).
  • Getting a Translated-PR liquid molar volume for an LPG mixture.
  • Pure-water / steam state at known T, P.

Don't use for

  • Multi-component flash (vle-flash-calculations).
  • EOS decision tree by itself (equation-of-state-selection).
  • Steam-table-only calculations (steam-tables-iapws).
  • Non-LPG hydrocarbon systems where COSTALD is outside its accuracy

envelope.

Utility Scripts

  • uv run scripts/property_methods.py recommend --components propane,n-butane,isobutane --application LPG --pressure-pa 1200000 --output /tmp/method.json
  • uv run scripts/property_methods.py costald-density --components propane,n-butane --zs 0.5,0.5 --temperature-k 300 --pressure-pa 1000000 --output /tmp/lpg_density.json
  • uv run scripts/property_methods.py iapws-state --temperature-k 373.15 --pressure-pa 101325 --output /tmp/steam.json
  • uv run scripts/property_methods.py pr-translated-eos --components propane,n-butane --zs 0.5,0.5 --temperature-k 300 --pressure-pa 1000000 --output /tmp/pr.json

Procedure

  1. Identify components and the operating envelope (T, P, composition).
  2. Run recommend for a property-method check.
  3. For LPG liquid density at vessel conditions, prefer COSTALD compressed.
  4. For pure water/steam, prefer IAPWS.
  5. For full flash, hand off to vle-flash-calculations with the selected

EOS.

Pitfalls

  • Using PR (default) for LPG liquid density at moderate pressure; PR

underpredicts liquid density by 5-15%. Use Translated-PR or COSTALD.

  • Using COSTALD for a non-light-hydrocarbon (water, alcohol, amine);

COSTALD is accurate only for nonpolar light hydrocarbons.

  • Using IAPWS for water-in-hydrocarbon systems; IAPWS is pure water only.
  • Passing the kij matrix as zeros for a sour LPG mixture; H2S / mercaptan

/ amine interactions need real kij.

  • Confusing mass density (kg/m³) with molar volume (m³/mol).
  • Treating the PRMIXTranslatedPPJP molar volume as exact without

providing the per-component translation constants cs.

  • Using recommend output as a final decision without doing the

second-opinion flash recommended by the decision-tree.

  • Treating water-content trace as negligible without checking with a

hydrate / glycol skill.

Fallback Strategies

  • If thermo / chemicals import fails for an exotic component, fall

back to built-in LPG defaults via engg_skills_common.property_backends.

  • For density that is wildly off, switch from COSTALD to

PRMIXTranslatedPPJP (or vice versa) and report both.

Verification

  • Run the listed script with representative inputs and an --output file when a deterministic calculation is available.
  • Confirm the JSON result contains ok: true, expected units, and no unhandled warnings.
  • Check result magnitudes against the stated assumptions, references, and a hand calculation or known operating range before reporting them.

References

  • references/property_method_selection.md — full method matrix.
  • references/caleb_bell_libraries.md — library overview and links.
  • thermo docs: https://thermo.readthedocs.io/
  • chemicals docs: https://chemicals.readthedocs.io/
  • DWSIM property package selection wiki.

Anti-Patterns

  • Reporting properties without naming the EOS or correlation.
  • Using cubic EOS for steam.
  • Reporting LPG liquid density without naming whether COSTALD or PR was

used.

Source & license

This open-source skill is cataloged on AgentStack and links to its original source — we do not rehost the code.

Install and usage instructions live in the source repository linked above.

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Versions

  • v0.1.0 Imported from the upstream source.