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Derive siphon inlet to outlet leg ratio

Short answer

Applying Bernoulli and constant friction slope, the siphon’s inlet-to-outlet leg ratio must satisfy l1/l2 ≤ [Pa – (ZB – ZA)] / [(ZB – ZC) – Pa] to prevent absolute pressure at the summit from dropping below zero.

Derive an expression for ratio of length of inlet to outlet leg for typical siphon as follows: l1l2≤Pa−(ZB−ZA)(ZB−ZC)−Pa\frac{l_1}{l_2} \le \frac{P_a - (Z_B - Z_A)}{(Z_B - Z_C) - P_a}, where PaP_a is atmospheric pressure, ZAZ_A, ZBZ_B, ZCZ_C are elevation of inlet, summit and outlet of syphon.

Setting up. A siphon has an inlet leg ABAB (length l1l_1) from the intake A in the upper reservoir up to the summit B, and an outlet leg BCBC (length l2l_2) down to the outlet C. The pipe has uniform diameter, so the friction loss per unit length is the same in both legs. Neglect minor losses and the velocity head. Let ZAZ_A, ZBZ_B, ZCZ_C be the elevations of intake water level, summit and outlet, and PaP_a the atmospheric pressure head (m of water).

        B (summit)
       /\
      /  \
 A __/    \
 ~~~ l1    \ l2
(upper      \___ C (outlet)
 reservoir)

Step 1: energy gradient. The whole fall is used to overcome friction over the total length:

H=ZA−ZC=hf,S=hfl1+l2=ZA−ZCl1+l2H = Z_A - Z_C = h_f, \qquad S = \frac{h_f}{l_1 + l_2} = \frac{Z_A - Z_C}{l_1 + l_2}

Step 2: pressure at the summit. Applying Bernoulli between A and B (velocity head is the same and ignored):

pAγ+ZA=pBγ+ZB+S l1  ⇒  pBγ=−[(ZB−ZA)+S l1](gauge)\frac{p_A}{\gamma} + Z_A = \frac{p_B}{\gamma} + Z_B + S\,l_1 \;\Rightarrow\; \frac{p_B}{\gamma} = -\left[(Z_B - Z_A) + S\,l_1\right] \quad\text{(gauge)}

The pressure at B is below atmospheric. The water column will break (cavitation, air release) if the absolute pressure falls below zero, i.e. pBγ<−Pa\dfrac{p_B}{\gamma} < -P_a. For the siphon to work:

(ZB−ZA)+S l1≤Pa  ⇒  S l1≤Pa−(ZB−ZA)⋯(1)(Z_B - Z_A) + S\,l_1 \le P_a \;\Rightarrow\; S\,l_1 \le P_a - (Z_B - Z_A) \quad\cdots(1)

Step 3: substitute the gradient.

(ZA−ZC) l1l1+l2≤Pa−(ZB−ZA)\frac{(Z_A - Z_C)\,l_1}{l_1 + l_2} \le P_a - (Z_B - Z_A)

Let X=Pa−(ZB−ZA)X = P_a - (Z_B - Z_A) and H=ZA−ZCH = Z_A - Z_C. Then H l1≤X (l1+l2)H\,l_1 \le X\,(l_1 + l_2), so

l1 (H−X)≤X l2  ⇒  l1l2≤XH−Xl_1\,(H - X) \le X\,l_2 \;\Rightarrow\; \frac{l_1}{l_2} \le \frac{X}{H - X}

Now

H−X=(ZA−ZC)−Pa+(ZB−ZA)=(ZB−ZC)−PaH - X = (Z_A - Z_C) - P_a + (Z_B - Z_A) = (Z_B - Z_C) - P_a l1l2≤Pa−(ZB−ZA)(ZB−ZC)−Pa\boxed{\frac{l_1}{l_2} \le \frac{P_a - (Z_B - Z_A)}{(Z_B - Z_C) - P_a}}

Meaning. For a siphon of given height the inlet leg must be shorter than the limit given by this ratio. For the denominator to be positive the outlet must be lower than PaP_a below the summit; otherwise the siphon works for any ratio. In practice, a smaller limiting pressure (vapour pressure, about 2 to 3 m of water absolute) is used in place of zero.

✓ Answer checked by Claude Sonnet 5.5

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