Cement Plant Gas Flow Measurement

Almost every number in a plant heat balance rests on a gas flow. This tool helps you set the duct measurement points, turn the readings into velocity, actual flow, normal flow and mass flow, and check whether the result is reliable enough for a plant decision. Press YOUR DUCT to set it up.

Why this matters now

Fan power, false air and unreliable gas measurements quietly increase fuel and electricity cost while weakening every heat and mass balance in the plant.

What this tool helps decide

Turn duct readings into a defensible gas flow for fan checks, heat balances and emissions decisions instead of relying on guessed air volume.

What subscription adds

Keep the gas-side audit together: save readings by fan, duct or machine, revisit the same equipment later and produce a report with findings, cost signals and priorities.

Connected to current industry priorities around energy efficiency, emissions measurement, waste heat and combustion optimisation reported in World Cement, CemNet and Global Cement.See process-tool plans

The duct, the points and what the gas is doing

The duct

Millimetres.
Millimetres from the duct wall to the outside face of the sample port. It is added to every mark, so what you read on the tube is what you push in.
More points, better answer. Six is the usual minimum, ten to twelve if the duct is large or the location is not ideal.

The gas

Degrees C.
Per cent by volume.
% dry
% dry
% dry
Pa at sea level.
Metres.
Pascals. Negative on the suction side of a fan.

The readings

0.84 for an S-type, 0.99 for an L-type. Use the calibration figure if the tube has one.
Velocity pressure at each point. The mark beside each row is how far to push the tube in — it updates as you change the duct.
WHAT THE GAS IS DOING
CAN YOU TRUST THIS READING
THE DUCT AND THE GAS ITSELF
Average gas speed
Actual flow
Normal flow, at 0 °C
Mass flow
Mean velocity pressure
Is this reading sound
Points under 75% of the top
Fastest against slowest
Fastest point
Slowest point
Duct area
Gas density here
Molar mass of the gas
Absolute pressure
Readings used

Take this to the plant — where to push the tube in, and what you read

What the gas measurement is telling you

How the numbers are worked out

Everything here was checked against your own Gas Flow.xls and the gas-flow.js built from it. They agree, and both are right.

Where to push the tube in. The marks are the standard equal-area traverse positions, taken straight from the Tube_Mark sheet of your workbook — the fraction of the duct diameter at which each point sits, for 2 to 24 points. Your port extension is added to every one, so the number on the tube is the number you push in. Checked against your own worked example: 0.044 of a 36 in duct plus a 2 in port gives 3.584 in, exactly your figure, and so does every other point. Every row of that table is symmetric about the centre, which is what an equal-area traverse has to be.

Why equal area and not equal spacing. A round duct carries far more gas in its outer rings than near the middle, because the area of a ring grows with its radius. Spacing the points evenly across the diameter would over-weight the centre and read high. Each of these points stands for the same slice of area, so a plain average of them is the true average.

The velocity. v = Cv × √(2 · pv / ρ). The important part is what gets averaged: the square roots of the velocity pressures are averaged first, then squared — pv = (mean of √pvi. Averaging the pressures themselves would read high, and the further your profile is from flat the worse it gets. Your file does this correctly.

The gas density. ρ = MW · pabs / (R · T) with the molar mass worked out from the wet composition, and the barometric pressure corrected for how high the plant sits: p = psea × ((288.15 − 0.0065h)/288.15)5.25588. At 1,000 m that is already 11 % off sea level, so it is not a detail.

The three flows are not interchangeable. Actual m³/h is what physically passes. Normal Nm³/h is that same gas counted at 0 °C, which is what most meters and contracts quote. Mass kg/h is the only one that does not change when the gas heats up. Mixing them up is the single most common error in a plant gas balance, so all three are shown together.

The 75 % rule. From your file: a point is called low when its velocity pressure is under 75 % of the highest reading, and the traverse passes when no more than a tenth of the points are low. Note that this is a test on the pressures. Pressure goes with the square of velocity, so it is a tighter test than the same number applied to velocities. Your threshold has been kept exactly as your file has it.

What a failed check actually means. Not that the arithmetic is wrong — that the location is. A traverse plane too close to a bend, a damper or the fan outlet gives a skewed profile, and no amount of care with the tube fixes it. Move at least eight duct diameters downstream of the last disturbance and two upstream of the next.