Venturi effect

Summary

The Venturi effect is the reduction in fluid pressure that results when a moving fluid speeds up as it flows through a constricted section (or choke) of a pipe. The Venturi effect is named after its discoverer, the 18th-century Italian physicist Giovanni Battista Venturi.

The upstream static pressure (1) is higher than in the constriction (2), and the fluid speed at "1" is lower than at "2", because the cross-sectional area at "1" is greater than at "2".
A flow of air through a Pitot tube Venturi meter, showing the columns connected in a manometer and partially filled with water. The meter is "read" as a differential pressure head in cm or inches of water.
Video of a Venturi meter used in a lab experiment
Idealized flow in a Venturi tube

The effect has various engineering applications, as the reduction in pressure inside the constriction can be used both for measuring the fluid flow and for moving other fluids (e.g. in a vacuum ejector).

Background edit

In inviscid fluid dynamics, an incompressible fluid's velocity must increase as it passes through a constriction in accord with the principle of mass continuity, while its static pressure must decrease in accord with the principle of conservation of mechanical energy (Bernoulli's principle). Thus, any gain in kinetic energy a fluid may attain by its increased velocity through a constriction is balanced by a drop in pressure.

By measuring pressure, the flow rate can be determined, as in various flow measurement devices such as Venturi meters, Venturi nozzles and orifice plates.

Referring to the adjacent diagram, using Bernoulli's equation in the special case of steady, incompressible, inviscid flows (such as the flow of water or other liquid, or low-speed flow of gas) along a streamline, the theoretical pressure drop at the constriction is given by

 

where   is the density of the fluid,   is the (slower) fluid velocity where the pipe is wider, and   is the (faster) fluid velocity where the pipe is narrower (as seen in the figure).

Choked flow edit

The limiting case of the Venturi effect is when a fluid reaches the state of choked flow, where the fluid velocity approaches the local speed of sound. When a fluid system is in a state of choked flow, a further decrease in the downstream pressure environment will not lead to an increase in velocity, unless the fluid is compressed.

The mass flow rate for a compressible fluid will increase with increased upstream pressure, which will increase the density of the fluid through the constriction (though the velocity will remain constant). This is the principle of operation of a de Laval nozzle. Increasing source temperature will also increase the local sonic velocity, thus allowing increased mass flow rate, but only if the nozzle area is also increased to compensate for the resulting decrease in density.

Expansion of the section edit

The Bernoulli equation is invertible, and pressure should rise when a fluid slows down. Nevertheless, if there is an expansion of the tube section, turbulence will appear, and the theorem will not hold. In all experimental Venturi tubes, the pressure in the entrance is compared to the pressure in the middle section; the output section is never compared with them.

Experimental apparatus edit

 
Venturi tube demonstration apparatus built out of PVC pipe and operated with a vacuum pump
 
 
 
A pair of Venturi tubes on a light aircraft, used to provide airflow for air-driven gyroscopic instruments

Venturi tubes edit

The simplest apparatus is a tubular setup known as a Venturi tube or simply a Venturi (plural: "Venturis" or occasionally "Venturies"). Fluid flows through a length of pipe of varying diameter. To avoid undue aerodynamic drag, a Venturi tube typically has an entry cone of 30 degrees and an exit cone of 5 degrees.[1]

Venturi tubes are often used in processes where permanent pressure loss is not tolerable and where maximum accuracy is needed in case of highly viscous liquids.[citation needed]

Orifice plate edit

Venturi tubes are more expensive to construct than simple orifice plates, and both function on the same basic principle. However, for any given differential pressure, orifice plates cause significantly more permanent energy loss.[2]

Instrumentation and measurement edit

Both Venturi tubes and orifice plates are used in industrial applications and in scientific laboratories for measuring the flow rate of liquids.

Flow rate edit

A Venturi can be used to measure the volumetric flow rate,  , using Bernoulli's principle.

Since

 

then

 
A Venturi can also be used to mix a liquid with a gas. If a pump forces the liquid through a tube connected to a system consisting of a Venturi to increase the liquid speed (the diameter decreases), a short piece of tube with a small hole in it, and last a Venturi that decreases speed (so the pipe gets wider again), the gas will be sucked in through the small hole because of changes in pressure. At the end of the system, a mixture of liquid and gas will appear. See aspirator and pressure head for discussion of this type of siphon.

Differential pressure edit

As fluid flows through a Venturi, the expansion and compression of the fluids cause the pressure inside the Venturi to change. This principle can be used in metrology for gauges calibrated for differential pressures. This type of pressure measurement may be more convenient, for example, to measure fuel or combustion pressures in jet or rocket engines.

The first large-scale Venturi meters to measure liquid flows were developed by Clemens Herschel who used them to measure small and large flows of water and wastewater beginning at the end of the 19th century.[3] While working for the Holyoke Water Power Company, Herschel would develop the means for measuring these flows to determine the water power consumption of different mills on the Holyoke Canal System, first beginning development of the device in 1886, two years later he would describe his invention of the Venturi meter to William Unwin in a letter dated June 5, 1888.[4]

Compensation for temperature, pressure, and mass edit

Fundamentally, pressure-based meters measure kinetic energy density. Bernoulli's equation (used above) relates this to mass density and volumetric flow:

 

where constant terms are absorbed into k. Using the definitions of density ( ), molar concentration ( ), and molar mass ( ), one can also derive mass flow or molar flow (i.e. standard volume flow):

 

However, measurements outside the design point must compensate for the effects of temperature, pressure, and molar mass on density and concentration. The ideal gas law is used to relate actual values to design values:

   

Substituting these two relations into the pressure-flow equations above yields the fully compensated flows:

 

Q, m, or n are easily isolated by dividing and taking the square root. Note that pressure-, temperature-, and mass-compensation is required for every flow, regardless of the end units or dimensions. Also we see the relations:

 

Examples edit

The Venturi effect may be observed or used in the following:

Machines edit

Architecture edit

  • Hawa Mahal of Jaipur, also utilizes the Venturi effect, by allowing cool air to pass through, thus making the whole area more pleasant during the high temperatures in summer.
  • Large cities where wind is forced between buildings - the gap between the Twin Towers of the original World Trade Center was an extreme example of the phenomenon, which made the ground level plaza notoriously windswept.[7] In fact, some gusts were so high that pedestrian travel had to be aided by ropes.[8]
  • In the south of Iraq, near the modern town of Nasiriyah, a 4000-year-old flume structure has been discovered at the ancient site of Girsu. This construction by the ancient Sumerians forced the contents of a nineteen kilometre canal through a constriction to enable the side-channeling of water off to agricultural lands from a higher origin than would have been the case without the flume. A recent dig by archaeologists from the British museum confirmed the finding.

Nature edit

See also edit

References edit

  1. ^ Nasr, G. G.; Connor, N. E. (2014). "5.3 Gas Flow Measurement". Natural Gas Engineering and Safety Challenges: Downstream Process, Analysis, Utilization and Safety. Springer. p. 183. ISBN 9783319089485.
  2. ^ "The Venturi effect". Wolfram Demonstrations Project. Retrieved 2009-11-03.
  3. ^ Herschel, Clemens. (1898). Measuring Water. Providence, RI:Builders Iron Foundry.
  4. ^ "Invention of the Venturi Meter". Nature. 136 (3433): 254. August 17, 1935. Bibcode:1935Natur.136Q.254.. doi:10.1038/136254a0.
  5. ^ Blasco, Daniel Cortés. "Venturi or air circulation?, that's the question". face2fire (in Spanish). Retrieved 2019-07-14.
  6. ^ Anderson, John (2017). Fundamentals of Aerodynamics (6th ed.). New York, NY: McGraw-Hill Education. p. 218. ISBN 978-1-259-12991-9.
  7. ^ Dunlap, David W (December 7, 2006). "At New Trade Center, Seeking Lively (but Secure) Streets". The New York Times.
  8. ^ Dunlap, David W (March 25, 2004). "Girding Against Return of the Windy City in Manhattan". The New York Times.
  9. ^ Dusk to Dawn (educational film). Federal Aviation Administration. 1971. 17 minutes in. AVA20333VNB1.

External links edit

  • 3D animation of the Differential Pressure Flow Measuring Principle (Venturi meter)
  • UT Austin. "Venturi Tube Simulation". Retrieved 2009-11-03.
  • Use of the Venturi effect for gas pumps to know when to turn off (video)