| Petrochemical processing | Hydrocarbons, solvents, and process liquids; exact fluid properties depend on the process. | The motor and pump are contained within a pressure boundary, avoiding a conventional shaft seal as a potential leak path. | Check liquid temperature, vapor pressure, viscosity, and the pump’s minimum-flow requirements against the proposed operating range. | Review bearing and winding temperature protection, motor current, minimum-flow provisions, and materials compatibility. |
| Heat-transfer systems | Thermal oils and other circulating heat-transfer fluids. | Contained construction can be useful where leakage of hot process liquid presents an operational or safety concern. | Confirm the fluid’s temperature and viscosity at start-up as well as at normal operation; thermal expansion and heat removal require design review. | Check temperature sensors, flow protection, cooling arrangements, and the specified operating limits of the motor and bearings. |
| Refrigeration and cooling | Refrigerants and other volatile liquids in suitable closed-loop systems. | Eliminating a dynamic shaft seal can reduce one potential fugitive-emission path; the full pressure boundary still requires appropriate design and testing. | Assess suction conditions, vapor formation risk, refrigerant properties, and the temperature range required for the duty. | Verify pressure and temperature ratings, motor protection, flow conditions, and compliance with applicable system requirements. |
| Ammonia service | Liquid ammonia in refrigeration or process applications designed for ammonia service. | A sealless configuration can help limit leakage at the shaft, but connections, casing, and other pressure-retaining parts remain relevant. | Account for ammonia properties, operating pressure, temperature, and the potential for flashing or inadequate liquid supply. | Confirm material suitability, pressure-boundary documentation, temperature protection, and the supplier’s stated service limitations. |
| Cryogenic liquid transfer | Low-temperature fluids such as liquefied gases, where the pump design is specifically qualified for cryogenic duty. | Contained construction may reduce shaft-seal leakage paths, but does not remove the need to assess all joints and containment boundaries. | Thermal contraction, cold-start conditions, insulation, and heat ingress can affect clearances and operating performance. | Ask for the qualified minimum temperature, cold-start procedure, insulation details, and temperature-monitoring arrangement. |
| Corrosive chemical transfer | Selected acids, alkalis, and other corrosive liquids, subject to material compatibility. | Seal-free containment can be advantageous when external leakage is undesirable; wetted materials must still resist the specific chemical. | Corrosion behavior and fluid properties can change with concentration and temperature, so evaluate the full operating envelope. | Request compatibility data for the exact concentration and temperature, plus inspection and condition-monitoring recommendations. |
| Toxic or hazardous fluids | Process liquids for which release control is important, subject to the site’s hazard assessment and applicable regulations. | The design removes the conventional shaft-seal interface, but total-system containment depends on casing, joints, piping, and installation. | Check heat generation, cooling path, permitted operating range, and the consequences of loss of flow. | Review leakage detection where required, temperature and motor protection, alarm settings, and emergency response provisions. |
| High-purity process service | Clean process liquids in applications where contamination control and cleanability requirements are defined. | A sealless arrangement avoids a shaft seal contacting the process boundary; it does not by itself guarantee cleanliness or purity. | Confirm allowable temperature, fluid cleanliness, and whether the process requires special flushing, cleaning, or validation procedures. | Check wetted-material certificates, surface-finish or cleanliness requirements, monitoring options, and documentation scope. |
| Boiler-feed and condensate systems | Water and condensate duties where pressure, temperature, and system configuration suit the selected pump. | Contained construction may be considered where seal maintenance or leakage control is a priority. | Evaluate suction pressure, liquid temperature, cavitation margin, and the pump’s required minimum flow. | Verify operating-point coverage, temperature protection, bearing monitoring, and provisions for low-flow or dry-running conditions. |
| General industrial circulation | Closed-loop circulation of compatible process liquids in chemical, energy, and manufacturing facilities. | Seal-free containment can reduce routine shaft-seal leakage concerns, while overall reliability still depends on correct selection and operation. | Check continuous and intermittent duty, ambient conditions, heat dissipation, fluid viscosity, and start-up requirements. | Compare available temperature, current, vibration, and flow monitoring with the plant’s alarm, maintenance, and control systems. |