Why two identical-looking quotes ship two different fans — and the single enquiry line that closes each gap.
Reviewed by Jitamitra application engineering
Share on LinkedInTwo vendors quote you a fan for “50,000 m³/hr at 100 mmWG.” One runs quietly for fifteen years. The other hunts, surges and eventually arrives at a repair shop on the back of a truck. Same headline numbers — two entirely different machines. The difference is the seven things the enquiry left unsaid. Here are all seven, and the single line of a request-for-quotation that closes each one.
Catalogue and test performance is quoted at standard air: 1.2 kg/m³ at 20 °C. Real process gas is almost never standard air, and two errors follow from ignoring that.
Flow basis. “10,000 Nm³/h of flue gas at 200 °C” is not 10,000 m³/hr of fan work — it is 17,300 actual m³/hr once the gas expands, because volume scales with (273+200)∕273. Quote the fan against the normal number and you undersize it by about 42 percent. This is how the well-known “up to 2×” sizing error happens.
Density. At 200 °C the same gas is roughly 38 percent lighter, so the same wheel develops about 38 percent less pressure. Worse, shaft power scales with density too: the cold start, when the air is heavy again, absorbs far more power than the hot duty — about 1.6× in this case. An induced-draft (ID) fan sized only on the hot number can look “too small” hot and still trip its motor cold. Forced-draft (FD) and ID fans on boilers live squarely in this trap.
| # | Mistake | What it costs | The RFQ line that prevents it |
|---|---|---|---|
| 1 | Oversizing “for safety” | Blanket margins push the duty left on the curve toward stall — wasted power, unstable running, shortened life | State the real calculated static at the fan; buy headroom as a higher pressure class or VFD speed reserve, never a bigger wheel |
| 2 | Ignoring gas density | Fan “too small” hot, or the motor trips on a cold start | Temperature — operating, maximum and cold-start — plus altitude and gas composition |
| 3 | Confusing actual and standard flow | The classic up-to-2× sizing error | Flow with its basis: actual m³/hr at conditions, or normal Nm³/hr |
| 4 | Ignoring inlet system effect | An elbow or drop-box at the inlet robs pressure the fan never sees (drop-box inlets: up to 45% flow loss) | The real duct layout at the fan — elbows, tees, inlet boxes, space limits |
| 5 | Selecting left of the curve's peak | Hunting, pulsing, surge | Ask for the duty point marked on the curve in the reply |
| 6 | Wrong material for the airstream | Erosion or corrosion failure, warranty claims | Dust loading and type, moisture / dew point, and required construction |
| 7 | Mismatched fans in parallel | One fan trapped in stall while the other carries the load | Declare parallel operation and quantity up front |
Ratings come from a clean, straight test inlet. An elbow hard against the inlet, a tee, a drop-box — none of that was in the rating, and each one quietly steals pressure. Give the wheel one to two straight duct diameters at the inlet, or turning vanes, and put the layout in the enquiry so the allowance is added before the frame is chosen, not discovered at commissioning. The US Department of Energy's fan system sourcebook (public domain) illustrates the tee-at-inlet case precisely.
Two traps worth naming. Stainless steel is a corrosion choice, not a wear choice — it resists abrasion barely better than mild steel. And no paint is wear protection. Abrasive service — think dust extraction on a mineral, foundry or cement stream — calls for wear plate, hard-facing overlay or ceramic, matched to the actual dust. That decision needs the dust, moisture and construction fields filled, not left blank.
The stable operating zone sits to the right of peak pressure. A duty point left of peak hunts and surges. Engineers have read this off characteristic curves for over a hundred years (Innes, The Fan, 1916, public domain). Ask where on the curve your duty lands — a credible vendor shows you, in writing.
Every mistake above is closed at enquiry stage, before a single rupee is committed. A complete duty is twelve fields: flow (with basis), static pressure at the fan, temperature (operating / maximum / cold-start), altitude, gas, dust, moisture, duct layout at the fan, drive, materials, accessories, and test standard. Note the last one honestly — ask for a fan tested to IS 4894 / AMCA 210 method, — the honest phrasing. Be wary of any quote that claims the fan itself is “certified” to those standards: IS and AMCA define a test method, not a product stamp a fan carries.
That is how we work here. Every duty we quote gets a committed selection — family, size, the duty point on the curve, absorbed power and the wheel rationale in writing — across a served range up to roughly 2,25,000 m³/hr, 2,000 mmWC, 425 HP and 500 °C. Where a duty sits outside that, we say so and route it to engineering rather than guess.
Talk to us about your fan duty →
Jitamitra Electro Engineering · Fan-engineering notes, written for the engineer.
Sources & basis. Further reading on this site: Specifying the duty point (/insights/), the 12-field fan RFQ template (/resources/), and the Jitamitra fan-engineering knowledge base (/insights/). Public-domain references: the US DOE fan system sourcebook (2003) and Innes, The Fan (1916).
Not as it stands. That is not 10,000 m3/hr of fan work — it is 17,300 actual m3/hr once the gas expands, because volume scales with (273+200)/273. Quote the fan against the normal number and you undersize it by about 42 percent. State flow with its basis: actual m3/hr at conditions, or normal Nm3/hr.
Because shaft power scales with density too. At 200 degC the gas is roughly 38 percent lighter, so the same wheel develops about 38 percent less pressure — but the cold start, when the air is heavy again, absorbs far more power, about 1.6 times in this case. Give temperature three ways: operating, maximum and cold-start, plus altitude and gas composition.
Not as a bigger wheel. Blanket margins push the duty left on the curve toward stall — wasted power, unstable running, shortened life. State the real calculated static at the fan and buy headroom as a higher pressure class or VFD speed reserve instead. The stable zone sits right of peak pressure, so ask for your duty point marked on the curve in the reply.
It does, and the rating never saw it. Ratings come from a clean, straight test inlet; an elbow, a tee or a drop-box quietly steals pressure the fan never sees, and drop-box inlets can cost up to 45% flow. Give the wheel one to two straight duct diameters or turning vanes, and put the real layout in the enquiry so the allowance is added before the frame is chosen.
No. Stainless steel is a corrosion choice, not a wear choice — it resists abrasion barely better than mild steel, and no paint is wear protection. Abrasive service on a mineral, foundry or cement stream calls for wear plate, hard-facing overlay or ceramic, matched to the actual dust. That needs the dust, moisture and construction fields filled, not left blank.
Better to ask for a fan tested to the IS 4894 / AMCA 210 method — that is the honest phrasing. Be wary of any quote claiming the fan itself is certified to those standards: IS and AMCA define a test method, not a product stamp a fan carries. And where a duty sits outside the range we serve, we say so and route it to engineering rather than guess.
Flow, static, gas temperature, application — or attach a spec, GA drawing or a multi-fan schedule. Engineer to engineer.
ISO 9001:2015 quality system · performance-tested to IS 4894 / ISO 5801 / AMCA 210 method · witnessed FAT on request.
*For our standard range. ATEX and special projects need 5 to 7 working days.
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