Olimetra WTS calculates operating conditions of choke, separators, flares, pipelines and PSVs in a connected network — in seconds. Full technical reports included. Validated against real field reports.
✓ Local install · Windows 10/11 · ✓ Offline-capable · One-time online activation
Designing a well test requires calculating pressure, temperature, erosion, radiation and safety — all connected. Spreadsheets don't propagate changes. General-purpose simulators cost USD 30–50k/year and weren't designed for this.
Every piece of equipment in a different file. A change in wellhead pressure forces updates across five tables. Propagation errors cost rig time.
HYSYS and Pipesim cost USD 30–50k/year and were built for plants, not well tests. Weeks of training for a 30-minute calculation.
Compiling the full calculation document with results, alarms and safety verifications takes hours after every single test.
API 521 radiation and flame length calculated separately, often in different file versions. Safety margin never properly documented.
Example simulation — demo well, choke 3/8", 2,213 psia. Every number below comes from an actual calculation run by the engine.
Real calculation · demo well · Choke 3/8" · Separator TP-5 · Q = 4.668 MMscfd · API 521 radiation
Build the PFD node by node. Calculations propagate automatically — wellhead pressure and temperature cascade through every choke, separator, heater, and line to the flare in one solve.
Choke · Sep · Pipeline · Heater · PSV · KODJT coefficient from Peng-Robinson EOS, dependent on P, T and composition. Liquid heat-capacity buffering included. Validated ±1.3°C across 5 real well reports.
Validated vs real field reportsPoint-source radiation for gas flares and air-atomized crude burners. Radiated fraction F(ALR) from Dutta et al. (1994) measurements. Heat-flux heatmap with water-screen correction and multi-source superposition.
API 521 · Dutta 1994 · ChamberlainAPI 520 orifice area for gas, liquid and two-phase relief (HEM direct integration, Annex C). Back-pressure Kb from tabular API 520 Fig. 3-9. Inlet ΔP 3% rule (§5.1.3) verified automatically.
API 520 · API 526 · HDI methodDescribe your test in plain language and the system builds the PFD. Analyzes results, flags out-of-spec equipment, and generates executive narrative for the report.
Powered by Claude AIOne click generates the Word calculation document with all results, alarms, radiation heatmaps, PSV certificates and CO₂e — ready for client or regulatory delivery.
DOCX · CO₂e · SO₂ · HeatmapsBeggs-Brill for horizontal and inclined pipelines. Erosional velocity per API 14E. Elbow erosion rate with ρV² criterion. Separator gas capacity by Arnold, Bradley or droplet-settling method.
Beggs-Brill · API 14E · ρV²Hydrate formation temperature along the flow path. MEG/methanol injection dose. Integrated alert when choke outlet approaches the hydrate curve. Correction for H₂S and CO₂.
Hammerschmidt · Wichert-Aziz · Sour correctionPR-EOS phase envelope with cricondentherm and cricondenbar. Operating points plotted on the diagram to confirm flow regime at each node. CVD retrograde dropout curve for gas condensates.
PR-EOS · Michelsen · CVDAir-to-oil ratio adequacy (ALR vs minimum required per Lefebvre), preheat temperature, compressor power and pressure ratio. Radiation F(ALR) validated against Dutta 1994 Alberta crude measurements.
Dutta 1994 · GPSA §13 · Lefebvre 1989Horizontal KOD for the flare system per API RP 521 §4.3.3. Gas velocity criterion K = 0.035 ft/s (4× more conservative than a process separator) plus liquid surge retention ≥ 10 min.
API 521 §4.3.3 · Slug protectionSO₂ mass rate for sour gas flaring (H₂S stoichiometry, η = 0.98) for ASEA/NOM-098 regulatory reporting. Full CO₂e inventory — combustion CO₂, CH₄ slip, SO₂ — per EPA AP-42 and GHG Protocol O&G.
NOM-098 · EPA AP-42 · IPCC AR6 GWPParticle-size distribution defined at the wellhead, size-resolved cyclonic and screen separation, and sand mass balance propagated through the network. Sand erosion per DNV-RP-O501.
Lapple 1951 · Svarovsky 1984 · DNV-RP-O501Orifice-plate gas metering with Reader-Harris/Gallagher discharge coefficient and ISO 5167 expansibility. Multiphase Venturi metering for wet streams.
AGA-3 · ISO 5167 · RHG 1998Enter molar composition or gas gravity and API. PVT and Z-factor calculated automatically.
Drag equipment from the catalog: choke manifold, separators, heaters, flare, lines and tanks.
Engine solves the network in steady state. Pressures, temperatures, erosion and safety in seconds.
Full technical Word document ready for client or operator delivery.
Annual license. Local installation on your machine. No data in the cloud.
In development · Q4 2026
In development · Q1 2027
Prices in USD · Annual billing · 1 license = 1 machine · Cancel anytime
Send us your well data. We simulate, analyze and deliver a full technical report — the same output as the licensed software, without any installation or learning curve.
Download, activate and simulate your first case in under 10 minutes. No learning curve, no scattered spreadsheets.
See plans →Olimetra WTS was developed by a team of petroleum engineers with hands-on experience in well testing operations across multiple basins worldwide. We spent years relying on disconnected spreadsheets and expensive general-purpose simulators that were never designed for what we actually needed in the field.
We built Olimetra WTS because we couldn't find a tool that combined rigorous thermodynamic calculations, safety analysis and automatic documentation in a single, affordable platform built specifically for well testing engineers.
📖 Technical note: Joule-Thomson cooling in well test chokes →
Last updated: June 2026
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Contact
Questions about this policy: sales@olimetra.com
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