| 1 | Match the compressor to the real air demand | Review the minimum, average, peak, and operating hours of compressed-air demand. Avoid sizing only from the connected load. | Record a 7-day demand profile where possible. Select a VSD unit whose efficient control range covers the normal load rather than only the short-term peak. | A VSD compressor can reduce unloaded running and pressure fluctuation when demand varies, but an incorrectly sized unit may operate near its inefficient low-load limit or fail to meet peak demand. | Flow meter data, pressure-logger records, shift schedules, and a load profile showing minimum, average, and maximum demand. |
| 2 | Verify pressure and air-quality requirements | Confirm required pressure at the point of use, pressure losses in the distribution system, and the required oil, moisture, and particle quality. | Common plant-air systems operate around 7–10 bar(g), but the correct set point must be based on the application. Specify the required ISO 8573-1 air-quality class and dryer pressure-dew-point requirement. | Higher discharge pressure generally increases energy consumption. A compressor alone cannot guarantee clean or dry air without correctly selected filtration, separation, and drying equipment. | Process specifications, pressure measurements at the farthest user, air-quality classification, and a complete compressor–dryer–filter proposal. |
| 3 | Evaluate the installation environment | Check ambient temperature, altitude, ventilation, dust, humidity, available floor space, access clearance, noise limits, and electrical supply. | Confirm the unit's rated ambient-temperature and altitude limits. Provide adequate cooling-air intake and hot-air discharge, and keep service access clear according to the installation manual. | High ambient temperature, restricted airflow, dust, or an unsuitable electrical supply can reduce capacity, shorten component life, and cause protective shutdowns. | Site survey, room-layout drawing, ventilation calculation, electrical single-line diagram, and written confirmation of operating limits. |
| 4 | Compare energy performance using specific power | Compare input power against delivered free air delivery at the same pressure, including the VSD, motor, and compressor package. | Use specific power in kW per m³/min or kW per 100 cfm. Compare test conditions, rated pressure, measurement method, and whether auxiliary equipment is included. | Electricity is usually the largest part of compressor life-cycle cost. A lower purchase price can be offset by higher energy consumption over several operating years. | ISO 1217 performance data or an equivalent independent test report, guaranteed flow and power values, and a load-weighted energy model. |
| 5 | Calculate total cost of ownership | Include purchase price, installation, electrical work, ventilation, dryer and filters, maintenance, consumables, downtime, and electricity. | Annual energy cost = average input power × annual operating hours × electricity tariff. Simple payback = additional investment ÷ annual operating-cost saving. | The lowest quoted price does not necessarily provide the lowest cost over the equipment life. Use the same demand profile and tariff assumptions for every quotation. | Five- to ten-year cost model, itemized quotation, maintenance schedule, spare-parts pricing, warranty terms, and documented energy assumptions. |
| 6 | Check electrical compatibility and control functions | Verify voltage, frequency, short-circuit rating, harmonics, motor-cable requirements, starting current, communications, and remote-control interfaces. | Confirm compatibility with the site's nominal electrical supply and control system. Review harmonic limits and power-quality requirements with the electrical engineer. | A VSD changes the electrical and control characteristics of the package. Poor integration can cause nuisance trips, interference, overheating, or process-control problems. | Electrical datasheet, harmonic assessment where required, protection-coordination review, communication protocol list, and functional test plan. |
| 7 | Assess supplier support and service capability | Evaluate commissioning, technician availability, preventive maintenance, spare-parts access, remote monitoring, training, warranty response, and emergency support. | Set measurable service requirements, such as response time, parts lead time, commissioning scope, training hours, and guaranteed availability of critical consumables. | Fast technical support and planned maintenance reduce production risk, especially when the compressor is a single point of failure. | Service-level agreement, local service coverage, escalation procedure, spare-parts list, reference installations, and commissioning acceptance criteria. |