Printed tables, typed properties
Enthalpy, specific volume and saturation temperature copied from a table and interpolated by hand. Change the pressure and every cell downstream depends on someone remembering to update it.
Size steam lines, ring and radial networks, condensate return and steam traps, pressure-reducing stations, desuperheaters, control valves and safety valves and the consumers that load the network — heat exchangers, jacketed vessels and steam-water mixers — on one IAPWS-IF97 engine, with a calculation report in Word for every one of them.
Your steam system lives in spreadsheets fed by a printed steam table, each consumer in its own file and none of them knows what happens at start-up. Which number goes into the project?
Enthalpy, specific volume and saturation temperature copied from a table and interpolated by hand. Change the pressure and every cell downstream depends on someone remembering to update it.
A line sized for the design flow says nothing about the start-up: valve wide open, cold consumer, blocked flow. That is where velocity and Mach run away — and the start-up flow should be calculated, not guessed.
A steam trap "sized" only by condensate load ignores start-up, minimum pressure, back pressure and stall. A consumer calculated outside the network ignores the pressure it actually receives.
Header pressure and temperature, line routes with fittings and elevation, insulation, consumers and their duty — the data you already have in the steam balance and the piping layout.
Maximum, minimum and start-up, with the start-up flow calculated from the valve wide open and the cold consumer. All properties come from the same IAPWS-IF97 engine — saturated, superheated or wet steam.
A calculation report with the inputs, formulas, cited references and a three-level verdict per item: meets, meets with open items, does not meet. What has no documented basis is reported as not evaluated.
All 10 steam calculators, on one IAPWS-IF97 engine — every one runs on the server, so an account is required.
Spreadsheets are flexible but run on typed table values and nobody audits them; vendor sizing tools cover their own products, and process simulators are not built to produce a line-by-line sizing report. LOGOS sizes lines, network, condensate, valves and consumers on the same IAPWS-IF97 engine, on the web.
| Feature | LOGOS | Excel spreadsheet | Vendor tool or simulator |
|---|---|---|---|
| Price | Free to start | Free | free for one brand, or a licence |
| Calculation report in Word | ✓ | ✕ | sometimes |
| Standardized, citable methods | ✓ | depends on who built it | ✓ |
| Traceability and versioning | ✓ | ✕ | partial |
| Nothing to install (web) | ✓ | ✓ | ✕ |
| Network, consumers and start-up together | ✓ | ✕ | one item or one brand at a time |
| Methods per IAPWS, IEC, API and ISO | IAPWS · IEC · API · ISO | — | vendor rules or own model |
| Learning curve | minutes | inherited and fragile | one tool per brand, or weeks of training |
Informative comparison, based on the typical use of each alternative. “Vendor tool or simulator” refers to the sizing tools steam equipment manufacturers distribute for their own products and to general-purpose process simulators.
No black box. Properties come from IAPWS-IF97 and the IAPWS transport releases; valves follow IEC 60534-2-1 and API 520 / 526; heat loss follows ISO 12241. The engine is cross-checked against open libraries (iapws, CoolProp, fluids) and published worked examples.
Every account gets full access — all disciplines, every calculator, no project or seat limit. No credit card, no deadline.
Pricing will be published before the beta ends, and nothing is charged unless you subscribe first.
“I am an engineer. I got tired of steam lines checked only at design flow, traps picked from a load figure and consumers calculated as if the network did not exist. I built LOGOS Steam to give every steam calculation what those spreadsheets never had: provenance.”
— the team behind LOGOS