| Temperature Operating Range | Water-based units commonly cover approximately 5–95 °C. Oil-based units are commonly selected for temperatures above the practical limit of water systems, often up to approximately 200–350 °C, depending on the heat-transfer fluid. | Confirm the guaranteed operating range, fluid type, maximum allowable temperature, and system pressure at the required temperature. | The selected fluid and temperature range determine heater design, pump selection, seals, piping, safety controls, and maintenance requirements. | Technical datasheet, operating-limit chart, fluid compatibility statement, and application-specific quotation. |
| Temperature Control Accuracy | A practical specification is often stated as approximately ±0.1 to ±0.5 °C at steady state, but actual performance depends on sensor location, heat load, flow, and process dynamics. | Ask whether accuracy means controller display accuracy, steady-state control stability, or total process temperature deviation. | Tighter control is important for molding, testing, crystallization, viscosity control, and processes sensitive to thermal variation. | Factory test report, calibration certificate, control trend data, and defined test conditions. |
| Heating Capacity | TCU heater ratings are commonly selected from several kilowatts to tens or hundreds of kilowatts. Required power depends on mass, specific heat, startup time, temperature rise, heat loss, and continuous process load. | Require a heat-load calculation rather than selecting only by nominal heater size. | Insufficient heating power causes slow startup and temperature recovery; excessive power can increase cost and control overshoot. | Heat-balance calculation showing startup time, process load, ambient losses, and recommended safety margin. |
| Cooling Method and Capacity | Cooling may use plant water, a closed-loop cooling circuit, air cooling, or a refrigeration system. Cooling capacity is normally specified in kW or kcal/h at a stated inlet temperature and flow rate. | Check cooling-water temperature, minimum and maximum flow, allowable pressure, heat rejection, and whether a separate chiller is required. | Cooling performance controls cycle time, ramp-down speed, process stability, and energy consumption. | Cooling-capacity curve, utility requirement sheet, piping diagram, and site-condition calculation. |
| Pump Flow and Pressure | Flow and pressure must be evaluated at the process connection, not only at the pump outlet. Actual requirements depend on channel size, hose length, fittings, viscosity, and elevation. | Request pump curves showing flow versus pressure and confirm the operating point at process temperature. | Adequate flow improves heat transfer and temperature uniformity; inadequate pressure can create hot spots and slow response. | Pump curve, calculated system resistance, connection-size drawing, and measured flow-test data. |
| Process Temperature Uniformity | Uniformity is application-specific and should be defined as a maximum temperature difference across the tool, mold, tank, or test fixture under actual operating conditions. | Confirm sensor arrangement, circuit design, flow distribution, and whether multi-zone temperature control is available. | Poor uniformity can cause dimensional variation, inconsistent material properties, product defects, or inaccurate test results. | Application test report, thermal mapping results, piping schematic, and recommended sensor locations. |
| Fluid Compatibility | Common heat-transfer fluids include treated water, demineralized water, thermal oils, and specialty fluids. Compatibility depends on temperature, pressure, materials, additives, and oxidation conditions. | Verify compatibility of fluid with pump seals, hoses, valves, heaters, sensors, gaskets, and tanks. | Incorrect fluid selection can cause corrosion, seal failure, deposits, reduced heat transfer, or fluid degradation. | Material list, fluid compatibility table, recommended fluid specification, and maintenance instructions. |
| Control Interface and Integration | Common industrial interfaces include digital inputs and outputs, alarm contacts, analog signals such as 4–20 mA or 0–10 V, and communication protocols such as Modbus RTU or Ethernet-based communication. | Confirm electrical drawings, communication protocol, data points, remote setpoint functions, alarm handling, and PLC compatibility. | Reliable integration supports automated recipes, remote monitoring, traceability, and coordinated machine operation. | I/O list, communication manual, sample register map, wiring diagram, and integration test procedure. |
| Safety Protection | Typical protections include over-temperature shutdown, low-fluid-level protection, pump overload protection, over-pressure protection, phase-loss protection, leakage detection, and emergency stop integration. | Check whether each protection is monitored, latched, resettable, and documented in the risk assessment and electrical design. | Safety functions reduce equipment damage, fluid leakage, process interruption, and operator risk. | Risk assessment, safety-circuit diagram, alarm list, functional test record, and operating manual. |
| Electrical Configuration | Industrial TCU systems may use single-phase or three-phase power, commonly at regional supply voltages such as 200–240 V or 380–480 V, subject to local electrical standards. | Confirm voltage, frequency, total connected load, short-circuit rating, breaker requirements, grounding, and cabinet dimensions. | Correct electrical matching prevents installation delays, nuisance trips, overheating, and non-compliance. | Electrical load list, single-line diagram, terminal schedule, nameplate data, and compliance documentation. |
| Energy Efficiency | Energy use is influenced by insulation, pump efficiency, heater control method, cooling strategy, standby operation, heat recovery, and the actual process duty cycle. | Compare measured or calculated energy consumption at the same temperature, load, cycle time, and utility conditions. | Lower energy demand reduces operating cost and cooling-water consumption over the equipment lifecycle. | Energy test report, heater duty profile, pump motor data, insulation specification, and annual operating-cost estimate. |
| Maintenance and Serviceability | Routine service commonly includes fluid inspection, filter or strainer cleaning, leak checks, sensor verification, electrical inspection, and periodic replacement of wear components. | Evaluate access to filters, pumps, heaters, valves, sensors, drain points, and electrical components. | Accessible components reduce planned downtime and simplify troubleshooting. | Preventive-maintenance schedule, spare-parts list, exploded drawings, troubleshooting guide, and service response procedure. |
| Documentation and Compliance | Documentation should reflect the destination market and may include declaration documents, electrical test records, pressure-related documentation where applicable, manuals, and material information. | Confirm applicable legal requirements, language requirements, labeling, technical-file availability, and document revision control. | Complete documentation supports installation approval, audits, operator training, and future maintenance. | Compliance checklist, risk assessment, user manual, electrical drawings, inspection records, and certificates where applicable. |
| Factory Acceptance Testing | A meaningful FAT should test temperature rise, temperature stability, cooling response, alarms, interlocks, pump performance, leakage, electrical safety, and communication functions. | Require agreed acceptance criteria, test instruments, test conditions, responsibilities, and procedures for handling deviations. | Testing before shipment reduces commissioning risk and identifies performance gaps while corrections are still practical. | Approved FAT protocol, calibrated instrument list, signed test report, inspection photographs, and punch-list closure record. |
| Total Cost of Ownership | Total cost includes purchase price, installation, utilities, fluid, filters, spare parts, maintenance labor, downtime, and end-of-life disposal—not only the initial equipment price. | Compare suppliers using the same duty cycle, operating hours, energy prices, service assumptions, and warranty terms. | A lower purchase price may result in higher operating cost if efficiency, reliability, or service support is inadequate. | Five-year or ten-year lifecycle-cost model, utility assumptions, warranty terms, spare-parts pricing, and service rates. |