| Primary sealing function | Select a mechanical seal that creates a controlled interface between the rotating shaft and stationary housing. | Designed to reduce leakage while allowing shaft rotation with low friction. | Helps limit product loss, emissions, contamination, and exposure to hazardous or corrosive fluids. |
| Fluid identification | Document the exact liquid composition, concentration, temperature, viscosity, solids content, crystallization tendency, and toxicity before specifying the seal. | Do not select a seal from the chemical name alone; concentration and operating temperature can change compatibility. | The same chemical may require different materials at different concentrations or temperatures. |
| Seal arrangement | Use a single seal for relatively clean, non-hazardous services when limited leakage is acceptable. Consider a double seal for hazardous, volatile, toxic, abrasive, or crystallizing fluids. | Single seal: one sealing interface. Double seal: two interfaces with a barrier or buffer fluid system. | A double arrangement can provide additional containment and protect the primary seal faces from difficult process conditions. |
| Seal face materials | Match the face combination to fluid chemistry, lubrication quality, pressure, temperature, and solids. | Common face materials include carbon, silicon carbide, and tungsten carbide. Typical pairings should be confirmed by the seal designer. | Face selection affects wear rate, heat generation, chemical resistance, and resistance to dry running or abrasive particles. |
| Elastomer selection | Choose the O-ring or secondary sealing material using a verified chemical-compatibility chart and actual operating conditions. | Common elastomer families include EPDM, FKM, and perfluoroelastomer compounds; suitability varies by chemical, temperature, and concentration. | Elastomer swelling, hardening, cracking, or extrusion can cause rapid leakage even when the seal faces are suitable. |
| Metal and spring materials | Use corrosion-resistant metal components suitable for the process liquid and cleaning chemicals. | Frequently used options include stainless steels and higher-alloy materials for more demanding chemical environments. | Corrosion of springs, clips, pins, or gland components can weaken the seal and make maintenance unsafe. |
| Pressure rating | Specify the maximum operating pressure, pressure fluctuations, suction conditions, and pressure direction. | Use the manufacturer’s certified pressure limit for the exact seal design; do not rely on a generic rating. | Excessive pressure can deform faces, overload secondary seals, and cause leakage or face separation. |
| Temperature rating | Base the selection on the highest continuous temperature, start-up temperature, shutdown temperature, and transient excursions. | Consider both the process temperature and heat generated at the seal faces. | Temperature affects elastomer life, lubricant viscosity, face distortion, vapor formation, and chemical compatibility. |
| Shaft speed and size | Provide shaft diameter, rotational speed, shaft runout, sleeve condition, and equipment type. | Seal performance depends on speed, face diameter, balance ratio, and available cooling or lubrication. | High speed increases heat generation and may require improved face materials, cooling, or a different seal design. |
| Solids and abrasives | Identify suspended solids, crystals, fibers, and polymerizing material. Use a suitable flushing or separation arrangement where necessary. | Hard solids can damage faces; crystallizing fluids may require controlled flushing or heating. | Contamination between the seal faces can create scoring, leakage paths, and accelerated wear. |
| Flush and barrier systems | Use clean flush, quench, buffer, or barrier systems when required by the process and seal arrangement. | Maintain the specified flow, pressure, cleanliness, and temperature for the selected system. | Proper fluid management removes heat, prevents crystallization, and keeps hazardous process fluid away from the atmosphere. |
| Installation inspection | Check shaft runout, sleeve condition, gland alignment, face cleanliness, gasket placement, and spring orientation before start-up. | Use equipment and seal tolerances supplied for the specific design; avoid metal tools on precision sealing faces. | Misalignment, scratches, dirt, or incorrect compression can cause leakage from the first operating cycle. |
| Start-up procedure | Confirm that the pump is primed, the seal chamber is filled, the flush or barrier system is operating, and the shaft rotates freely. | Never intentionally run a conventional liquid-lubricated mechanical seal dry. | Dry running can generate destructive heat and damage seal faces within a short period. |
| Routine monitoring | Record leakage, temperature, vibration, pressure, flush flow, barrier pressure, and changes in operating sound. | Establish baseline readings after commissioning and trend deviations over time. | Small changes often indicate face wear, plugged flush lines, cavitation, misalignment, or process upset. |
| Leakage response | Investigate increasing leakage promptly. Isolate, depressurize, drain, and decontaminate the equipment before attempting repair. | Do not tighten gland fasteners as a substitute for diagnosis unless the seal design specifically permits adjustment. | Excessive tightening can distort the seal, overload the faces, and create a more serious failure. |
| Maintenance interval | Use condition-based maintenance whenever reliable monitoring is available, supported by scheduled inspections during planned shutdowns. | There is no universal replacement interval; service life depends on chemistry, speed, temperature, pressure, installation, and operating practice. | Replacing seals only by calendar time may waste serviceable parts or miss failures developing under severe conditions. |
| Replacement criteria | Replace damaged faces, hardened or swollen elastomers, corroded springs, worn drive components, and distorted gaskets. | Inspect mating faces for scoring, chipping, blistering, uneven wear, and thermal damage. | Reusing compromised components can produce repeat leakage and unplanned downtime. |
| Safety and documentation | Maintain chemical safety information, seal specifications, installation records, inspection results, and maintenance history. | Use the current safety data sheet and site isolation procedures before opening chemical equipment. | Accurate records support safer maintenance, faster troubleshooting, regulatory compliance, and better future seal selection. |