Although siphons can exceed the barometric height of the liquid in special circumstances, e.g. when the liquid is degassed and the tube is clean and smooth, in general the practical maximum height can be found as follows.
Setting equations 1 and 3 equal to each other gives:
Maximum height of the intermediate high point occurs when it is so high that the pressure at the intermediate high point is zero; in typical scenarios this will cause the liquid to form bubbles and if the bubbles enlarge to fill the pipe then the siphon will "break". Setting P = 0:
Solving for h:
:General height of siphon:
This means that the height of the intermediate high point is limited by pressure along the streamline being always greater than zero.
:Maximum height of siphon:
This is the maximum height that a siphon will work. Substituting values will give approximately  for water and, by definition of standard pressure,  for mercury. The ratio of heights (about 13.6) equals the ratio of densities of water and mercury (at a given temperature). As long as this condition is satisfied (pressure greater than zero), the flow at the output of the siphon is still only governed by the height difference between the source surface and the outlet. Volume of fluid in the apparatus is not relevant as long as the pressure head remains above zero in every section.  Because pressure drops when velocity is increased, a static siphon (or manometer) can have a slightly higher height than a flowing siphon.