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handbook of modern sensors

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11.2 Pressure Gradient Technique 361<br />

The measurement <strong>of</strong> flow is rarely conducted for the determination <strong>of</strong> a displacement<br />

<strong>of</strong> volume. Usually, what is needed is to determine the flow <strong>of</strong> mass rather than<br />

volume. Of course, when dealing with virtually incompressible fluids (water, oil, etc.),<br />

either volume or mass can be used. A relationship between mass and volume for a<br />

incompressible material is through density ρ<br />

M = ρV. (11.5)<br />

The densities <strong>of</strong> some materials are given in Table A.12 (Appendix). The rate <strong>of</strong> mass<br />

flow is defined as<br />

dM<br />

= ρAv (11.6)<br />

dt<br />

The SI unit for mass flow is kilogram per second and the U.S. Customary System unit<br />

is pounds per second. For a compressible medium (gas), either mass flow or volume<br />

flow at a given pressure should be specified.<br />

There is a great variety <strong>of</strong> <strong>sensors</strong> that can measure flow velocity by determining<br />

the rate <strong>of</strong> displacement <strong>of</strong> either mass or volume. Whichever sensor is used, inherent<br />

difficulties <strong>of</strong> the measurement make the process a complicated procedure. It is necessary<br />

to take into consideration many <strong>of</strong> the natural characteristics <strong>of</strong> the medium,<br />

its surroundings, barrel and pipe shapes and materials, medium temperature and pressure,<br />

and so forth. When selecting any particular sensor for the flow measurement,<br />

it is advisable to consult with the manufacturer’s specifications and very carefully<br />

consider the application recommendations for a particular sensor. In this book, we do<br />

not cover such traditional flow measurement systems as turbine-type meters. It is <strong>of</strong><br />

interest to us to consider <strong>sensors</strong> without moving components which introduce either<br />

no or little restriction into the flow.<br />

11.2 Pressure Gradient Technique<br />

A fundamental equation in fluid mechanics is Bernoulli equation which is strictly<br />

applicable only to steady flow <strong>of</strong> nonviscous, incompressible medium:<br />

( ) 1<br />

p + ρ<br />

2 v2 a + gy = const, (11.7)<br />

where p is the pressure in a tube <strong>of</strong> flow, g = 9.80665 m/s 2 = 32.174 ft/s 2 is the gravity<br />

constant, and y is the height <strong>of</strong> the medium’s displacement. Bernoulli’s equation<br />

allows us to find fluid velocity by measuring pressures along the flow.<br />

The pressure gradient technique (<strong>of</strong> flow measurement) essentially requires the<br />

introduction <strong>of</strong> a flow resistance. Measuring the pressure gradient across a known<br />

resistor allows one to calculate a flow rate. The concept is analogous to Ohm’s law:<br />

Voltage (pressure) across a fixed resistor is proportional to current (flow). In practice,<br />

the restricting elements which cause flow resistances are orifices, porous plugs, and<br />

Venturi tubes (tapered pr<strong>of</strong>ile pipes). Figure 11.3 shows two types <strong>of</strong> flow resistor.<br />

In the first case, it is a narrow in the channel; in the other case, there is a porous

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