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Hydraulic Design — Valves & Fittings

Minor losses and valve sizing: K loss coefficients, equivalent length, flow coefficient Cv/Kv, control-valve authority and a K-factor reference table with a worked valve-sizing example.

K·v²/2g
minor loss
Cv / Kv
valve flow
0.25–0.5
authority

Sizing Valves & Counting Minor Losses

Bends, tees, reducers and valves each take a bite out of the head budget — the so-called minor losses that, on a fitting-heavy plant, can rival the straight-pipe friction. Control valves add a second job: they must be sized so they actually control, holding enough authority over the system without being permanently near-shut. Both come down to two numbers: the loss coefficient K and the flow coefficient Cv / Kv.

K Factors & Flow Coefficient

Minor (fitting) losshm = K · (v² / 2g)   ·   hm,total = (ΣK) · v²/2g

Or, equivalently, as an equivalent length of straight pipe, Le = K·D/f. Control-valve capacity is rated by the flow coefficient:

Valve flow coefficient (Kv, SI)Q = Kv · √(ΔP / SG)    (Q in m³/h, ΔP in bar)

The control valve should take a meaningful share of the variable head — its authority N = ΔPvalve(open) / ΔPsystem should be roughly 0.25–0.5, or it loses controllability and runs nearly shut.

Typical Loss Coefficients (K)

FittingK (approx.)FittingK (approx.)
90° elbow (long radius)0.6Gate valve (open)0.15
90° elbow (standard)0.9Globe valve (open)6–10
45° elbow0.4Butterfly valve (open)0.3–1.5
Tee (through-run)0.2Check valve (swing)2.0
Tee (branch flow)1.0Sudden contraction0.3–0.5
Sharp entrance0.5Sudden enlargement / exit1.0

Globe valves throttle well but cost ~10× the head of a gate valve fully open — chosen for control, not isolation. Sum the K’s on the route, multiply by v²/2g, and the minor-loss head drops straight into the budget.

Sizing a Control Valve

Worked example: control-valve Kv & minor losses

Q = 30 m³/h water; allocate ΔP = 0.6 bar across the control valve at design flow. Also count the fittings on a DN100 line at v = 1.06 m/s: two LR elbows, one branch tee, one swing check.

Kv = Q / √(ΔP/SG) = 30 / √(0.6/1.0) = 30/0.775 = 38.7 m³/h → select next size up (e.g. Kv ≈ 40–50)
ΣK = 2(0.6) + 1.0 + 2.0 = 4.2  →  hm = 4.2 × 1.06²/19.62 = 0.24 m
The valve at authority ~0.3 controls well; the fittings add 0.24 m to the head budget. Reducer and expansion losses on the same line are best taken from the flow & reducer calculator.

Run the Numbers

Add reducer and fitting losses, and check velocities, with the pipe hydraulics tools.

Related Hydraulic Design

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