| 1. Match the operating temperature | Required setpoint, normal operating range, start-up temperature, and maximum allowable temperature. | Water-based systems commonly operate from approximately 5°C to 95°C under atmospheric conditions. Pressurized water systems can operate above 100°C. Oil systems are commonly selected for approximately 100°C to 350°C service, depending on the heat-transfer fluid. | Choose a temperature range that covers the process with operating margin, while ensuring that the fluid, seals, heater, hoses, and sensors are rated for the maximum temperature. | An unsuitable fluid or temperature rating can cause boiling, oxidation, seal damage, unstable control, or reduced equipment life. |
| 2. Size the heating and cooling capacity | Product mass, mold or vessel mass, material specific heat, temperature change, cycle time, heat loss, and cooling demand. | A basic heating estimate is: Q = m × Cp × ΔT ÷ t. Actual sizing should also include heat losses and the heat released by the process. Cooling capacity may be limited by plant-water temperature and available flow. | Select a heater and cooler with sufficient capacity for the required ramp rate and peak process load, rather than sizing only for the final holding temperature. | Undersizing produces slow warm-up and recovery. Oversizing may increase cost, cycling, and temperature overshoot if control is not properly tuned. |
| 3. Compare pump flow with circuit resistance | Required flow through the mold, jacket, platen, heat exchanger, or reactor, including pipe length, fittings, filters, valves, and narrow passages. | Small and medium temperature-control circuits may require approximately 10–80 L/min. Larger or low-resistance circuits can require more than 100 L/min. The required value depends on heat load and the allowable temperature difference across the process. | Use the pump curve to verify that the pump can deliver the required flow at the actual system resistance, not only at zero pressure or free discharge. | Adequate flow improves heat transfer and reduces temperature gradients. Excessive flow can increase energy use, noise, erosion, and stress on fittings. |
| 4. Check pump pressure and available head | Total dynamic head, elevation changes, pressure drop through the process equipment, and the minimum pressure required to prevent flashing or cavitation. | Many compact TCU circuits operate with pump discharge pressures of roughly 2–6 bar, while the exact pressure depends on flow, piping, temperature, and component resistance. Pressure is not interchangeable with flow. | Select a pump whose operating point falls within the stable portion of its performance curve at the required flow and pressure. Include a safety margin without exceeding the pressure rating of the process circuit. | Insufficient pressure causes low flow and poor temperature uniformity. Excessive pressure can damage hoses, seals, molds, jackets, or heat exchangers. |
| 5. Select materials for fluid compatibility | Heat-transfer fluid type, operating temperature, additives, water quality, corrosion potential, and cleaning chemicals. | Stainless steel wetted parts are commonly used for water circuits because of their corrosion resistance. Carbon steel may be suitable in controlled closed-loop systems. Copper, brass, elastomers, and plastics must be checked for compatibility with the selected fluid and temperature. | For clean water or aggressive fluids, consider stainless steel piping, pump components, heater chambers, and heat exchangers. Specify gasket and seal materials separately rather than judging compatibility by metal selection alone. | Material incompatibility can lead to corrosion, contamination, leakage, blocked passages, and premature failure of seals or pump components. |
| 6. Verify connection size and hydraulic layout | Inlet and outlet size, hose length, pipe diameter, return-line arrangement, drain location, venting, and available installation space. | Common connections for compact systems range from approximately ½ inch to 2 inches, but connection size alone does not determine actual flow. Long hoses, sharp elbows, undersized fittings, and restrictive filters increase pressure loss. | Keep supply and return lines as short and direct as practical. Match the connection size to the required flow and confirm that the piping pressure rating exceeds the maximum pump pressure and operating temperature. | A poor layout can make a correctly sized pump perform like an undersized pump and can create air pockets, unstable flow, or difficult maintenance access. |
| 7. Confirm control accuracy and protection functions | Required temperature tolerance, sensor position, response time, alarm limits, pressure limits, and process safety requirements. | Many industrial applications target control stability around ±0.5°C to ±1.0°C, although actual performance depends on sensor location, heat load, flow, insulation, and controller tuning. | Specify a calibrated process sensor, high-temperature cutout, low-level protection, overpressure protection, pump overload protection, leak detection where needed, and alarms for inadequate flow or cooling water. | Protection functions reduce the risk of product defects, heater damage, dry running, unsafe pressure, overheating, and unplanned downtime. |