| RO Feed-Water Flow | 1–100 m³/h for small to medium industrial RO systems | Use the maximum continuous flow, not only the average daily flow. | The flow rate directly determines the amount of water that must be cooled and affects evaporator, pump, piping, and control-valve sizing. | Confirm the rated feed-flow range from the RO system design and verify it with a calibrated flow meter. |
| Inlet Water Temperature | Approximately 15–35 °C, depending on climate, source water, and process conditions | Size the chiller for the highest expected inlet temperature during the hottest operating period. | Higher inlet temperatures increase the cooling load and can reduce RO membrane performance if the process temperature is not controlled. | Record temperature continuously for at least one representative operating period, including the seasonal high. |
| Target Process-Water Temperature | Commonly 20–25 °C for controlled RO feed-water operation | Use the membrane manufacturer’s approved operating-temperature range as the governing limit. | Temperature influences water viscosity, permeate flow, salt passage, and the pressure required to achieve the target production rate. | Review membrane design software results, operating manuals, and historical product-water quality data. |
| Required Water Temperature Reduction | Typically 3–15 K, depending on the source-water temperature and target temperature | Calculate the maximum temperature drop from the hottest inlet condition to the required outlet condition. | A larger temperature reduction produces a higher refrigeration load and may require a larger compressor, condenser, and heat exchanger. | Use the measured inlet temperature and the specified outlet temperature under peak production conditions. |
| Cooling-Duty Calculation | Cooling load (kW) ≈ 1.163 × flow (m³/h) × ΔT (K) | Add the heat load from pumps, motors, piping, tanks, and the surrounding environment. | This provides a practical first estimate for water cooling. It is based on the specific heat and density of water near normal process temperatures. | Calculate the duty at maximum flow and maximum inlet temperature, then validate it with a thermal-load assessment. |
| Example Cooling Load | For 20 m³/h cooled by 8 K: approximately 186 kW | 1.163 × 20 × 8 = 186.1 kW | The example represents sensible cooling of water only; actual chiller capacity must also include system heat gains. | Recalculate using actual plant flow, measured temperature difference, and confirmed operating hours. |
| Design Capacity Margin | Typically 10–20% above the calculated peak cooling load | Use the lower end where operating data is reliable and the upper end where conditions are variable. | A reasonable margin helps the chiller handle fouling, seasonal temperature changes, gradual performance degradation, and short-term load fluctuations. | Document the calculation assumptions and avoid excessive oversizing, which can cause short cycling and poor humidity control. |
| Chilled-Water Supply Temperature | Commonly 7–12 °C for a secondary chilled-water loop | Select the highest supply temperature that still allows the required process-water outlet temperature. | A higher chilled-water supply temperature can improve chiller efficiency, while a lower temperature may be required for a compact heat exchanger or difficult heat load. | Confirm the required approach temperature of the process heat exchanger and the minimum allowable process temperature. |
| Chilled-Water Return Temperature | Often 12–17 °C when designed for a 5 K temperature rise | Define supply and return temperatures together with the required secondary-loop flow. | The temperature difference affects chilled-water flow, pump energy, pipe size, and the required evaporator capacity. | Verify the heat exchanger design and measure supply and return temperatures during peak load. |
| Heat-Exchanger Approach Temperature | Commonly 2–5 K for a properly selected liquid-to-liquid heat exchanger | Use the exchanger supplier’s certified performance data at the actual flow rates and fouling allowance. | A smaller approach temperature generally requires more heat-transfer surface and can increase equipment cost, but it may reduce the required chiller temperature. | Check the exchanger duty, pressure drop, material compatibility, and cleanability requirements. |
| RO Feed-Water Pressure | Often 10–25 bar for brackish-water RO; seawater RO is typically much higher | Use the actual pump discharge pressure and allow for pressure losses through the cooling circuit. | The chiller is normally connected through a heat exchanger or separate loop. Pressure rating and pump selection must match the RO process. | Review the pump curve, piping layout, design pressure, relief-protection requirements, and operating transients. |
| Water Quality and Fouling Risk | Depends on hardness, alkalinity, suspended solids, iron, silica, and biological activity | Use pretreatment and filtration suitable for the selected heat exchanger and the RO feed-water quality. | Scaling and fouling reduce heat transfer, increase pressure drop, and can cause unstable outlet temperatures. | Use a current laboratory water analysis and establish cleaning frequency, filtration level, and chemical-treatment requirements. |
| Heat-Exchanger Material | Common choices include titanium, 316 stainless steel, or other corrosion-resistant materials | Select materials based on chloride concentration, pH, temperature, cleaning chemicals, and design pressure. | Material compatibility is critical because concentrated or chemically treated water can accelerate corrosion and shorten equipment life. | Compare the water analysis with material-resistance data and obtain written confirmation from the equipment designer. |
| Ambient Design Temperature | Usually 35–45 °C for outdoor installations, depending on local climate | Use the site’s recorded design summer temperature rather than a generic average. | Air-cooled chillers lose capacity and efficiency as ambient temperature rises, which may require a larger condenser or a water-cooled configuration. | Check local weather design data and evaluate condenser performance at the peak ambient condition. |
| Cooling Method | Air-cooled or water-cooled chiller | Choose according to water availability, ambient conditions, maintenance capability, noise limits, and energy objectives. | Air-cooled units are simpler where cooling water is limited; water-cooled units can be more efficient but require a cooling tower or another heat-rejection system. | Compare total lifecycle cost, water consumption, available space, seasonal performance, and maintenance requirements. |
| Control Accuracy | Typically ±1 °C for a stable process-water temperature loop | Use a modulating capacity-control system, variable-speed pump, or three-way control valve where the process load varies significantly. | Stable temperature control helps maintain consistent permeate production and reduces unnecessary compressor cycling. | Define the acceptable temperature band, sensor location, response time, and alarm limits in the control philosophy. |
| Operating Schedule | Continuous, batch, or variable-shift operation | Size for peak duty and evaluate turndown for the minimum expected load. | A chiller that is too large for low-load operation may cycle frequently, while insufficient turndown can cause temperature fluctuations and excess energy use. | Review production schedules, start-up sequences, shutdown periods, and expected daily and seasonal load profiles. |
| Energy-Use Review | Compare cooling capacity, input power, and seasonal efficiency at actual operating conditions | Evaluate performance at full load and part load, not only at the nominal rating point. | Compressor efficiency, condenser temperature, pump power, and control strategy strongly influence the total operating cost. | Request certified performance data and calculate annual energy use from the site’s operating hours and load profile. |
| System Protection | Flow switch, high/low pressure protection, freeze protection, temperature alarms, and overload protection | Interlock the chiller with the RO feed pump and stop the system when minimum flow or safe temperature limits are not met. | Protection devices prevent evaporator freezing, pump damage, loss of cooling, and operation outside the RO process limits. | Review the cause-and-effect diagram, alarm set points, emergency-stop logic, and restart sequence. |