| Gate valve |
On/off isolation |
Main distribution lines, plant headers, and pipelines where a straight-through flow path is useful. |
Designed to be fully open or fully closed. It is generally not suitable for routine throttling because partial opening can cause vibration, erosion, and seat damage. |
Consider face-to-face space, operating time, pressure rating, and whether the valve will remain in one position for long periods. |
| Globe valve |
Throttling and flow regulation |
Flow-control branches, dosing lines, and services that need frequent adjustment. |
Provides comparatively precise manual or actuated flow adjustment, but typically creates more pressure loss than a full-bore gate or ball valve. |
Check allowable pressure drop, flow range, trim materials, and whether an actuator or positioner is needed for automatic control. |
| Butterfly valve |
Isolation and, with suitable design, throttling or modulation |
Large-diameter water mains, treatment-plant headers, and space-constrained piping. |
Quarter-turn operation supports compact manual or actuated control. Modulating performance depends on valve design, sizing, and operating range. |
Confirm pressure and temperature limits, liner and disc compatibility, shutoff requirements, and the control accuracy needed. |
| Ball valve |
Fast on/off isolation |
Equipment isolation, sampling points, utility lines, and smaller process connections. |
Quarter-turn operation provides quick shutoff and low flow resistance when fully open. Standard ball valves are generally intended for on/off service; characterized or V-port designs may be used for control. |
Verify seat and body compatibility with the fluid, required shutoff performance, pressure rating, and whether throttling is explicitly supported by the valve design. |
| Diaphragm valve |
Isolation and moderate flow control |
Chemical dosing, corrosive liquid service, and applications where the process fluid should be separated from the operating mechanism. |
A flexible diaphragm closes against a weir or seat. The design can limit fluid contact with internal moving parts, but the diaphragm is a wear component. |
Match diaphragm and body materials to the chemical, temperature, pressure, and cleaning conditions. Check replacement intervals and required flow capacity. |
| Pinch valve |
Isolation and flow control for suitable slurry or solids-bearing fluids |
Sludge, abrasive suspensions, and some process streams containing suspended solids. |
A sleeve is compressed to stop or restrict flow, leaving the fluid in contact mainly with the sleeve. The sleeve can wear and requires inspection or replacement. |
Assess particle size, abrasiveness, sleeve compatibility, pressure, and the maintenance access needed for sleeve replacement. |
| Check valve |
Automatic non-return flow control |
Pump discharge lines and process lines where reverse flow could damage equipment or disrupt operation. |
Opens and closes in response to flow conditions; it does not provide normal manual or modulating flow control. Selection must account for potential water hammer and minimum operating flow. |
Choose a suitable check-valve design and orientation for the flow direction, installation layout, closing behavior, and system surge conditions. |