| 1 |
Choose low-loss isolation valves Full-port ball or gate valves |
Usually low when correctly sized; full-port designs can approach the pressure loss of a straight pipe section. |
Lower permanent pressure loss reduces the duty required from pumps or compressors during continuous operation. |
On/off service for water, air, gas, and compatible process fluids. |
Use full-port construction where pressure loss matters. Do not use standard ball or gate valves for continuous throttling unless specifically designed for it. |
| 2 |
Use butterfly valves for large-diameter lines Wafer, lug, or double-flanged designs |
Generally low to moderate when fully open; resistance increases as the disc moves toward the closed position. |
Lower valve mass and compact actuation can reduce actuator energy, especially on large pipe sizes. |
HVAC, cooling water, wastewater, fire protection, and general utility systems. |
Confirm the disc, seat, and liner materials against fluid temperature, pressure, and chemical compatibility. |
| 3 |
Reserve globe valves for control duty Single-seat or balanced control valves |
Moderate to high by design because the flow path changes direction through the body and trim. |
A globe valve can provide accurate control, but its higher pressure drop may increase pump energy in continuous service. |
Steam, temperature control, pressure control, and applications requiring precise modulation. |
Select the trim using the required flow coefficient, operating range, cavitation risk, and acceptable pressure drop—not only the line size. |
| 4 |
Size the valve for the actual flow range Review Cv, Kv, and operating percentage |
A valve that is too small creates excessive pressure loss; an oversized valve may operate near the seat and waste throttling energy. |
Efficient operation normally requires stable control across the minimum, normal, and maximum design flow rates. |
All liquid, gas, and steam systems where flow varies during operation. |
Provide minimum, normal, and maximum flow, inlet and outlet pressure, temperature, fluid density, and viscosity to the valve supplier. |
| 5 |
Match the actuator to the duty cycle Pneumatic, electric, or hydraulic actuation |
Actuator energy is affected by valve torque or thrust, differential pressure, breakaway force, and operating frequency. |
Pneumatic systems consume compressed air during stroking; electric actuators mainly consume power while moving and during control or heating functions. |
Pneumatic for fast repetitive cycling; electric for distributed or intermittent operation; hydraulic for very high force requirements. |
Compare total operating energy, including compressor or hydraulic power, rather than actuator nameplate power alone. |
| 6 |
Prevent unnecessary throttling Use a dedicated control valve where modulation is continuous |
Partially closed isolation valves can generate significant turbulence and permanent pressure loss. |
Operating a pump against an artificially restricted valve can increase system power consumption and noise. |
Variable-flow pumping, process regulation, and systems with frequent load changes. |
Consider a variable-speed pump or fan when appropriate. A control valve should be selected for stable control rather than used as a permanent restriction. |
| 7 |
Specify reliable sealing and maintenance access Seat design, packing, position feedback, and serviceability |
Leakage, friction, deposits, and misalignment can increase operating torque and pressure loss over time. |
A well-maintained valve requires less actuator effort and avoids energy losses caused by process leakage or repeated cycling. |
Long-life utility and process installations where downtime and maintenance access affect lifecycle cost. |
Specify the required leakage class, emissions requirements, cycle life, ambient conditions, spare parts, and inspection intervals before purchase. |