| 1 |
Shaft Diameter |
Measure the shaft or sleeve diameter at the seal location with a calibrated vernier caliper or micrometer. |
Record the actual diameter in millimetres. Common industrial seal shaft sizes include 16, 18, 20, 22, 25, 28, 30, 33, 35, 38, 40, 43, 45, 48, and 50 mm. |
Order a seal designed for the measured shaft size. Do not select by pump name or appearance alone. |
| 2 |
Stationary Seat and Housing Dimensions |
Confirm the stationary seat outside diameter, seat thickness, housing bore, and available counterbore depth. |
Typical seat arrangements include O-ring-mounted, rubber-cup-mounted, and gasket-mounted designs. The seat must fit the housing bore without excessive looseness or forced distortion. |
Compare the seal drawing with the pump housing drawing and verify both the seat diameter and installation depth. |
| 3 |
Axial Installation Length |
Measure the distance from the seal reference shoulder to the mating face after the impeller and sleeve are correctly positioned. |
The working length must match the seal design within the manufacturer’s stated tolerance. Excessive compression can cause heat and wear; insufficient compression can cause leakage. |
Request a dimensional drawing and confirm the installed length, spring position, and required compression before purchase. |
| 4 |
O-Ring Size and Groove |
Check the O-ring inside diameter, cross-section, groove width, groove depth, stretch, and squeeze. Inspect whether the O-ring moves axially or rotates with the seal. |
O-ring sizes may follow ISO 3601 metric series or AS568 inch series. A static O-ring seal commonly uses approximately 10% to 30% radial squeeze, subject to the groove design and material. |
Match the O-ring standard, size code, cross-section, and groove geometry. Never replace an O-ring using diameter alone. |
| 5 |
Fluid, Temperature, and Materials |
Identify the pumped liquid, concentration, temperature range, pressure, abrasives, and compatibility requirements. |
Common material options include carbon, silicon carbide, tungsten carbide, ceramic, stainless steel, elastomers such as EPDM or FKM, and PTFE. Compatibility depends on the actual fluid and operating conditions. |
Select face, metal, and elastomer materials from a compatibility chart. Consider chemical concentration and temperature at the seal faces. |
| 6 |
Pressure, Speed, and Operating Limits |
Confirm maximum pressure, rotational speed, shaft runout, vibration, and whether the pump operates continuously or intermittently. |
Seal limits are design-specific. Pressure and speed should be checked together because higher speed increases heat generation and face load. Shaft runout and misalignment can prevent stable face contact. |
Provide the supplier with operating pressure, speed, temperature, shaft size, and pump duty cycle rather than requesting a seal by size only. |
| 7 |
Leakage and Acceptance Requirements |
Define whether the application permits visible leakage, vapor emission, or only a controlled microscopic fluid film at the seal faces. |
A mechanical seal is designed to minimize leakage, but a microscopic lubricating film is necessary between faces. The acceptable leakage level must be defined according to the fluid, safety requirements, environmental rules, and site test method. |
Specify the required leakage criterion, pressure-test method, test duration, and acceptance standard before ordering. Use a dual seal or containment arrangement when leakage cannot be tolerated. |