1 Valve Sizing Te chnic al Bulletin Scope Valve size often is described by the nominal size of the end connections, but a more important measure is the flow that the valve can provide. And determining flow through a valve can be simple. This technical bulletin shows how flow can be estimated well enough to select a valve size easily, and without complicated calculations. Included are the principles of flow calculations, some basic formulas, and the effects of specific gravity and temperature. Also given are six simple graphs for estimating the flow of water or air through valves and other components and examples of how to use them. Sizing Valves The graphs cover most ordinary industrial applications from the smallest metering valves to large ball valves, at system pressures up to 000 psig and 0 bar. The water formulas and graphs apply to ordinary liquids and not to liquids that are boiling or flashing into vapors, to slurries (mixtures of solids and liquids), or to very viscous liquids. The air formulas and graphs apply to gases that closely follow the ideal gas laws, in which pressure, temperature, and volume are proportional. They do not apply to gases or vapors that are near the pressure and temperature at which they liquefy, such as a cryogenic nitrogen or oxygen. For convenience, the air flow graphs show gauge pressures, whereas the formulas use absolute pressure (gauge pressure plus one atmosphere). All the graphs are based on formulas adapted from ISA S75.01, Flow Equations for Sizing Control Valves. 1 Flow Calculation Principles The principles of flow calculations are illustrated by the common orifice flow meter (Fig. 1). We need to know only the size and shape of the orifice, the diameter of the pipe, and the fluid density. With that information, we can calculate the flow rate for any value of pressure drop across the orifice (the difference between inlet and outlet pressures). For a valve, we also need to know the pressure drop and the fluid density. But in addition to the dimensions of pipe diameter and orifice size, we need to know all the valve passage dimensions and all the changes in size and direction of flow through the valve. However, rather than doing complex calculations, we use the valve flow coefficient, which combines the effects of all the flow restrictions in the valve into a single number (Fig. 2). Pipe diameter Orifice diameter Pressure drop Orifice shape Fluid density Fig. 1. The flow rate through a fixed orifice can be calculated from the meter dimensions of pipe diameter and orifice size and shape. Pressure drop Safe Product Selection When selecting a product, the total system design must be considered to ensure safe, trouble-free performance. Function, material compatibility, adequate ratings, proper installation, operation, and maintenance are the responsibilities of the system designer and user. Pipe diameter Size changes Valve passage size Fluid density Direction changes Fig. 2. Calculating the flow rate through a valve is much more complex. The valve flow coefficient (C v ) takes into account all the dimensions and other factors including size and direction changes that affect fluid flow.
2 2 Valve Sizing Fig. 3. Valve manufacturers determine flow coefficients by testing the valve with water using a standard ISA test method. p 1 p p 2 Flow meter Test valve Flow control valve Flow control valve Standard distances from test valve Minimum lengths of straight pipe Valve manufacturers determine the valve flow coefficient by testing the valve with water at several flow rates, using a standard test method 2 developed by the Instrument Society of America for control valves and now used widely for all valves. Flow tests are done in a straight piping system of the same size as the valve, so that the effects of fittings and piping size changes are not included (Fig. 3). Liquid Flow Because liquids are incompressible fluids, their flow rate depends only on the difference between the inlet and outlet pressures (Dp, pressure drop). The flow is the same whether the system pressure is low or high, so long as the difference between the inlet and outlet pressures is the same. This equation shows the relationship: Symbols Used in Flow Equations q = N 1 C v p G f C v = flow coefficient q = flow rate p 1 = inlet pressure p 2 = outlet pressure Dp = pressure drop (p 1 p 2 ) G f = liquid specific gravity (water = 1.0) G g = gas specific gravity (air = 1.0) N 1, N 2 = constants for units T 1 = absolute upstream temperature: K = C R = F + 4 Note: p 1 and p 2 are absolute pressures for gas flow. The water flow graphs (pages 6 and 7) show water flow as a function of pressure drop for a range of C v values. Gas Flow p = p 1 p 2 p 1 p 2 C v Gas flow calculations are slightly more complex, because gases are compressible fluids whose density changes with pressure. In addition, there are two conditions that must be considered low pressure drop flow and high pressure drop flow. G f q
3 p 2 < 1/2p 1 q Valve Sizing 3 Low and High Pressure Drop Gas Flow The basic orifice meter illustrates the difference between high and low pressure drop flow conditions. In low pressure drop flow when outlet pressure (p 2 ) is greater than half of inlet pressure (p 1 ) outlet pressure restricts flow through the orifice: as outlet pressure decreases, flow increases, and so does the velocity of the gas leaving the orifice. When outlet pressure decreases to half of inlet pressure, the gas leaves the orifice at the velocity of sound. The gas cannot exceed the velocity of sound and therefore this becomes the maximum flow rate. The maximum flow rate is also known as choked flow or critical flow. Any further decrease in outlet pressure does not increase flow, even if the outlet pressure is reduced to zero. Consequently, high pressure drop flow only depends on inlet pressure and not outlet pressure. Low pressure drop p 1 p 2 Maximum flow p 1 p 2 Sonic flow High pressure drop p 1 p 2 q p 2 > 1/2p 1 p 2 = 1/2p 1 q This equation applies when there is low pressure drop flow outlet pressure (p 2 ) is greater than one half of inlet pressure (p 1 ): 2 p q = N 2 C v p 1 (1 ) 3p 1 p p 1 G g T 1 p 2 > 1/2p 1 pressure does not increase the flow because the gas has reached sonic velocity at the orifice, and it cannot break that sound barrier. The equation for high pressure drop flow is simpler because it depends only on inlet pressure and temperature, valve flow coefficient, and specific gravity of the gas: q = N 2 C v p 1 1 G g T 1 G g T 1 p 1 p 2 q p 2 < 1/2p 1 The low pressure drop air flow graphs (pages 8 and 9) show low pressure drop air flow for a valve with a C v of 1.0, given as a function of inlet pressure (p 1 ) for a range of pressure drop (Dp) values. When outlet pressure (p 2 ) is less than half of inlet pressure (p 1 ) high pressure drop any further decrease in outlet C v G g T 1 p 1 p 2 The high pressure drop air flow graphs (pages and 11) show high pressure drop air flow as a function of inlet pressure for a range of flow coefficients. C v q
4 4 Valve Sizing + Fig. 4. For most common liquids, the effect of specific gravity on flow is less than %. Also, most high-density liquids such as concentrated acids and bases usually are diluted in water and consequently the specific gravity of the mixtures is much closer to that of water than to that of the pure liquid. Percent change Change in specific gravity Change in flow rate Ether Alcohol Oils Nitric acid Sulfuric acid + Fig. 5. For common gases, the specific gravity of the gas changes flow by less than % from that of air. And just as with liquids, gases with exceptionally high or low densities often are mixed with a carrier gas such as nitrogen, so that the specific gravity of the mixture is close to that of air. Percent change + 0 Change in specific gravity Change in flow rate 1 Hydrogen Natural gas Oxygen Argon Carbon dioxide Effects of Specific Gravity The flow equations include the variables G f and G g liquid specific gravity and gas specific gravity which are the density of the fluid compared to the density of water (for liquids) or air (for gases). However, specific gravity is not accounted for in the graphs, so a correction factor must be applied, which includes the square root of G. Taking the square root reduces the effect and brings the value much closer to that of water or air, 1.0. For example, the specific gravity of sulfuric acid is % higher than that of water, yet it changes flow by just 34 %. The specific gravity of ether is 26 % lower than that of water, yet it changes flow by only 14 %. Figure 4 shows how the significance of specific gravity on liquid flow is diminished by taking its square root. Only if the specific gravity of the liquid is very low or very high will the flow change by more than % from that of water. The effect of specific gravity on gases is similar. For example, the specific gravity of hydrogen is 93 % lower than that of air, but it changes flow by just 74 %. Carbon dioxide has a specific gravity 53 % higher than that of air, yet it changes flow by only 24 %. Only gases with very low or very high specific gravity change the flow by more than % from that of air. Figure 5 shows how the effect of specific gravity on gas flow is reduced by use of the square root. Effects of Temperature Temperature usually is ignored in liquid flow calculations because its effect is too small. Temperature has a greater effect on gas flow calculations, because gas volume expands with higher temperature and
5 Valve Sizing 5 Temperature, C Percent change 0 Change in flow rate Fig. 6. Many systems operate in the range F ( C) to +212 F (+ C). Within this range, temperature changes affect flow by little more than % Temperature, F Numerical Constants for Flow Equations Constant contracts with lower temperature. But similar to specific gravity temperature affects flow by only a square-root factor. For systems that operate between F ( C) and +212 F (+ C), the correction factor is only +12 to 11 %. Figure 6 shows the effect of temperature on volumetric flow over a broad range of temperatures. The plus-or-minus % range covers the usual operating temperatures of most common applications. Other Services Units Used in Equations N q p T 1 N U.S. gal/min psia Imperial gal/min psia L/min bar L/min kg/cm 2 N std ft 3 /min psia R 69 std L/min bar K 6816 std L/min kg/cm 2 K As noted above, this technical bulletin covers valve sizing for many common applications and services. What about viscous liquids, slurries, or boiling and flashing liquids? Suppose vapors, steam, and liquefied gases are used? How are valves sized for these other services? Such applications are beyond the scope of this document, but the ISA standards S75.01 and S75.02 contain a complete set of formulas for sizing valves that will be used in a variety of special services, along with a description of flow capacity test principles and procedures. These and other ISA publications are listed in the references. Also, most standard engineering handbooks have sections on fluid mechanics. Several of these are given in the references, as well. Cited References 1. ISA S75.01, Flow Equations for Sizing Control Valves, Standards and Recommended Practices for Instrumentation and Control, th ed., Vol. 2, ISA S75.02, Control Valve Capacity Test Procedure, Standards and Recommended Practices for Instrumentation and Control, th ed., Vol. 2, Other References L. Driskell, Control-Valve Selection and Sizing, ISA, J.W. Hutchinson, ISA Handbook of Control Valves, 2nd ed., ISA, Chemical Engineers Handbook, 4th ed., Robert H. Perry, Cecil H. Chilton, and Sidney D. Kirkpatrick, Ed., McGraw-Hill, New York. Instrument Engineers Handbook, revised ed., Béla G. Lipták and Kriszta Venczel, Ed., Chilton, Radnor, PA. Piping Handbook, 5th ed., Reno C. King, Ed., McGraw-Hill, New York. Standard Handbook for Mechanical Engineers, 7th ed., Theodore Baumeister and Lionel S. Marks, Ed., McGraw-Hill, New York.
6 6 Valve Sizing Water Flow U.S. Units Water flow, U.S. gallons per minute C v = Pressure Drop, psi Flow, U.S. gal/min Example: Enter the vertical scale with the pressure drop across the valve (Dp = psi). Read across to the desired flow rate (q = 4 U.S. gal/min). The diagonal line is the desired C v value (C v = 0.).
7 Water Flow Metric Units Water flow, liters per minute Valve Sizing C v = Pressure Drop, bar Flow, L/min Example: Enter the vertical scale with the pressure drop across the valve (Dp = bar). Read across to the desired flow rate (q = 0.2 L/min). The diagonal line is the desired C v value (C v = ).
8 8 Valve Sizing Low Pressure Drop Air Flow U.S. Units Low pressure air drop flow, standard cubic feet per minute psi 0 psi 0 psi 0 psi 0 25 psi 0 Inlet Pressure, psig 0 0 p = 5 psi psi High pressure drop flow Flow, std ft 3 /min Example: Enter the vertical scale with the inlet pressure at the valve (p 1 = 0 psig). Read across to the diagonal line for the pressure drop across the valve (Dp = 25 psi). Read down to the horizontal scale for the flow rate through a valve with a C v of 1.0 (q = 65 std ft 3 /min). Multiply that flow rate by the valve C v to determine the actual flow rate.
9 Low Pressure Drop Air Flow Metric Units Low pressure air drop flow, standard liters per minute Valve Sizing bar bar 5 bar 2.5 bar 1.0 bar 0. bar Inlet Pressure, bar p = bar High pressure drop flow Flow, std L/min Example: Enter the vertical scale with the inlet pressure at the valve (p 1 = bar). Read across to the diagonal line for the pressure drop across the valve (Dp = 1 bar). Read down to the horizontal scale for the flow rate through a valve with a C v of 1.0 (q = 00 std L/min). Multiply that flow rate by the valve C v to determine the actual flow rate.
10 Valve Sizing High Pressure Drop Air Flow U.S. Units High pressure drop air flow, standard cubic feet per minute C v C= v Inlet Pressure, psig Flow, std ft 3 /min Example: Enter the vertical scale with the inlet pressure at the valve (p 1 = 0 psig). Read across to the desired flow rate (q = std ft 3 /min). The diagonal line is the desired C v value (C v = 0.).
11 Valve Sizing 11 High Pressure Drop Air Flow Metric Units High pressure drop air flow, standard liters per minute 0 C v = Inlet Pressure, bar Flow, std L/min Example: Enter the vertical scale with the inlet pressure at the valve (p 1 = bar). Read across to the desired flow rate (q = 00 std L/min). The diagonal line is the desired C v value (C v = 1.0).
12 Safe Product Selection When selecting a product, the total system design must be considered to ensure safe, trouble-free performance. Function, material compatibility, adequate ratings, proper installation, operation, and maintenance are the responsibilities of the system designer and user. Swagelok TM Swagelok Company 1994, 1995, 00, 02 Swagelok Company December 07, R4 MS E
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