What is a baseline, and why one number is not enough
A baseline is not a single figure copied from a commissioning sheet. It is a controlled reference state tied to a specific machine, its configuration, its operating mode and the conditions at the time. A screw compressor running fully loaded at 7 bar on a 25 °C morning behaves differently from the same machine unloading at 8 bar on a 44 °C afternoon. Both can be healthy.
So a useful baseline records the reading together with its context: which machine (by serial), which configuration, what load and speed, what discharge pressure, what ambient and room temperature, which measurement point, which instrument and what date. Machines that run in several states – loaded, unloaded, VSD at low and high speed – need a baseline for each state that matters.
This page covers how to create trustworthy baselines. How condition information is then used to plan maintenance is covered in predictive and condition-based maintenance.
When to take a baseline
- After commissioning and run-in of a new or relocated compressor
- After a major overhaul, airend exchange, motor replacement or cooler cleaning
- After a significant configuration change, such as a new pressure set point or controller replacement
- When monitoring starts on an existing machine – recorded as a “current state” reference, not assumed to be healthy
- Seasonally, where summer and winter conditions differ enough to need separate references
Mark each baseline with a revision. When a new one replaces an old one, keep the old one and the reason for the change.
What to measure
| Parameter | Typical point | What a change may indicate |
|---|---|---|
| Discharge (airend) temperature | Controller reading, verified with a contact or infrared check | Cooler fouling, thermostatic valve fault, low oil, high ambient (typical oil-injected screw about 75–95 °C) |
| Delivery pressure and set points | Package outlet and reference header point | Control changes, separator or filter restriction |
| Separator differential pressure | Across the separator element | Element loading, oil degradation |
| Motor current and power | Motor terminals or panel meter | Mechanical load increase, airend wear, electrical issues |
| Specific power | kW input per m³/min delivered | Overall efficiency change; compare only at matching pressure and load |
| Vibration | Marked points on motor and airend bearings, three directions | Bearing wear, misalignment, looseness, imbalance |
| Cooler approach temperature | Air outlet versus ambient or cooling water | External fouling, fan problems, ventilation loss |
| Load/unload pattern | Controller hours and cycles | Demand change, leaks, control band problems |
| Dryer PDP | Dryer outlet sensor | Dryer deterioration (typical refrigerated about +3 °C) |
| Oil condition | Sample from the specified point | Oxidation, contamination, wear metals |
Measurement discipline: making readings comparable
Most “trends” that alarm people are measurement differences, not machine changes. Control the method:
- Fixed points – mark vibration and temperature points physically so every reading is taken in the same place and direction.
- Known instruments – record which sensor or portable meter was used, its range and when it was last verified.
- Stable state – take readings after the machine has reached steady temperature, not just after start-up.
- Same load and pressure – note load percentage, VSD speed and discharge pressure; compare like with like.
- Time stamps – synchronise clocks between controllers and loggers, or note the offset.
- Manual readings – use a standard sheet with units printed on it; a “6.8” with no unit is useless later.
- Data-quality flags – mark readings taken during faults, maintenance or sensor problems.
Portable measurements by a technician are fine for baselines if the method is repeatable. Permanent sensors give continuous data but still need periodic verification.
Context that must be recorded with every baseline
Record ambient and room temperature, humidity where relevant, cooling-water temperature for water-cooled machines, ventilation state, system pressure, production state, and whether dryers and filters were in normal service. In Hyderabad and across Telangana and Andhra Pradesh, compressor-room temperatures in April and May can be far above the design ambient if hot air is not ducted out. A summer reading compared with a December baseline will always look worse; that is a ventilation and seasonal effect, not necessarily a failing machine.
How to set up a baseline: step by step
- Identify the machine by make, model, serial and site tag; record its role (base, trim, standby).
- Confirm it is in a known good state: recent service, clean coolers, correct oil level, no active alarms.
- Record the configuration: set points, unload band, VSD limits, controller version.
- Mark measurement points and list the instruments to be used.
- Run to steady state in each operating mode you want to baseline.
- Take readings with full context: load, speed, pressure, ambient, time.
- Calculate derived values such as specific power and approach temperature, stating the formula.
- Store the baseline with a revision number, date and the name of the person who approved it.
- Set review limits for change from baseline, based on manufacturer guidance and engineering judgement, not generic charts.
Using the baseline: reading change correctly
| Observed change | Check context first | Then check the machine |
|---|---|---|
| Discharge temperature up | Ambient, ventilation, load | Cooler fins, fan, thermostatic valve, oil level and condition |
| Power up at same pressure | Pressure set point, supply voltage | Separator restriction, intake filter, airend wear, motor condition |
| More load/unload cycles | Production demand, leaks | Control band, receiver size, inlet valve behaviour |
| Vibration rising | Speed and load during reading, point used | Bearings, alignment, belts or coupling, foundation bolts |
| Dryer PDP rising | Inlet temperature and flow | Condenser cleanliness, refrigerant circuit, drain operation |
The goal is a trend, not a single alarming reading. One high value should prompt a repeat measurement under controlled conditions before any work is ordered.
Baselines for different compressor types
The principles are the same across technologies, but the emphasis changes.
- Oil-injected screw – discharge temperature, separator differential pressure, oil condition, specific power and airend bearing vibration are the core set.
- Oil-free screw – stage temperatures and pressures, intercooler and aftercooler approach, and bearing vibration matter most; record each stage separately.
- Reciprocating – valve temperatures, stage pressures, crankcase oil condition, vibration and noise, and running time per start.
- VSD machines – baselines at several defined speeds, plus drive temperature and motor current at each speed.
- Portable diesel compressors – engine oil pressure, coolant temperature, discharge temperature, fuel use at a stated load and chassis vibration; on hire jobs, readings at each 300-hour service build a useful history.
- Dryers – PDP, inlet temperature, pressure drop and, for desiccant units, purge behaviour and tower switching.
Keep the same reading sheet format across brands so a mixed compressor house can be compared machine by machine.
Common baseline mistakes
- Treating the first reading as healthy – a machine already running hot with fouled coolers gives a false reference. Service it first, or label the reading as current state.
- Losing the context – readings without load, pressure or ambient cannot be compared later.
- Changing the measurement point – a vibration reading taken on the cover instead of the bearing housing is a different number, not a trend.
- Overwriting the old baseline – after an overhaul, keep the previous reference so the improvement can be shown and the next decline measured.
- Ignoring the system – a rise in compressor power may come from a raised pressure set point or new leaks; each extra bar costs roughly 7% more power.
Avoiding these costs nothing and makes every later reading worth more.
How Reddy Compressors helps
Reddy Compressors, Tarnaka, Secunderabad, is an independent multi-brand compressed-air specialist serving industry since 2002. We sell new and used compressors, rent from our own fleet, and provide service, AMC, overhauls, audits and spares for ELGi, Atlas Copco, Ingersoll Rand, KAESER, Chicago Pneumatic, Sullair, Doosan, Kirloskar, Gardner Denver and many other brands. We are not an authorised dealer of any brand. We have tie-ups with all major and reputed brands.
- Record baseline readings after commissioning, overhaul or airend work, with full operating context
- Take consistent readings at every visit under our compressor AMC so trends are comparable
- Log power and flow to establish specific power and demand baselines
- Investigate deviations: coolers, thermostatic valves, separators, bearings, alignment and controls
- Supply spares identified from make, model, serial or the old part, with fit confirmed before quoting
Our service team covers all of Telangana and Andhra Pradesh, and we supply equipment and spares across India.
What to send us
- Make, model, serial and nameplate photo of each compressor
- Running hours, last service date and parts changed
- Current pressure set points and typical load pattern
- Any readings or controller logs you already have
- Photos of the compressor room showing ventilation and layout
Frequently asked questions
What is a baseline in compressor condition monitoring?
It is a set of readings taken when the compressor is known to be healthy, recorded with its load, speed, pressure, ambient temperature, measurement points and instruments. Later readings are compared with this reference to spot deterioration. Without the context, a reading cannot tell you whether the machine has worsened or is simply operating in a different state or season.
When should I take a new baseline for my compressor?
Take one after commissioning and run-in, after any major overhaul, airend exchange, motor replacement or cooler cleaning, and after significant configuration changes such as new set points. Keep the previous baseline with its revision and reason for replacement. For existing machines starting monitoring, record a current-state reference rather than assuming the machine is healthy.
What is a normal discharge temperature for a screw compressor?
For oil-injected screw compressors it is typically about 75–95 °C in steady operation, depending on design, load and ambient. The machine’s own baseline matters more than a general range. A steady rise over weeks usually points to cooler fouling, a thermostatic valve fault, low oil or ventilation problems, and should be checked before it reaches the trip level.
Why does my compressor show higher readings in summer?
Higher intake and room temperatures raise discharge and oil temperatures and reduce cooler and dryer performance. In a Telangana or Andhra Pradesh summer, room temperatures can exceed design ambient if hot air is not ducted away. Compare summer readings with a summer baseline, or correct for ambient, and improve ventilation before assuming the compressor itself is deteriorating.
Can I use controller readings for a baseline or do I need separate instruments?
Controller readings are a good starting point and are often all that is available. Verify key values, such as discharge temperature and pressure, with a calibrated portable instrument at least once, and note any offset. Vibration and power usually need separate instruments. Record which source was used so future comparisons use the same basis.
Does Reddy Compressors record baselines for all compressor brands?
Yes. As an independent multi-brand specialist we take and record baseline readings on ELGi, Atlas Copco, Ingersoll Rand, KAESER, Chicago Pneumatic and many other brands, using the same format across a mixed fleet. This is done after commissioning, overhaul or airend work, and as part of routine service visits under an AMC.
Related pages
Calculators and worked examples
These tools give indicative figures for screening, comparison and for preparing an enquiry. They run in your browser and send nothing. No prices or tariffs are assumed: enter your own to see costs. Efficiencies and other figures shown are example values: replace them with your own. Results are not a performance guarantee or a design certificate; final selection is confirmed by a service engineer against the machine data sheet and the site.
Cooler approach and margin against a baseline
Compare a cooler reading now with a baseline taken at the same load, pressure and fan state. The tool splits the rise in leaving temperature into the part caused by a hotter cooling medium and the part caused by a worse cooler approach, and shows the margin to the limit.
The worked example below shows the method with fixed numbers. Turn on JavaScript to change the inputs.
Worked example
Inputs
- Baseline: cooling medium entering (°C): 30
- Baseline: fluid leaving the cooler (°C): 40
- Now: cooling medium entering (°C): 38
- Now: fluid leaving the cooler (°C): 54
- Applicable limit for the leaving temperature (°C): 55
- Measurement uncertainty of the comparison (K): 1
Result
- Approach: baseline: 10 K
- Approach: now: 16 K
- Change in leaving temperature: +14 K
- of which hotter cooling medium: +8 K
- of which change in approach: +6 K
- Margin to limit: baseline: 15 K
- Margin to limit: now: 1 K
- Investigation direction: Approach has risen: look at the cooler core, fan, belt and airflow (or water-side fouling), and at the thermostatic valve and oil condition.
Method. Approach = fluid leaving the cooler − cooling medium entering it (for an air-cooled oil cooler: oil out − cooling air in). Rise in leaving temperature = change in cooling-medium inlet + change in approach. Margin = applicable limit − leaving temperature. A change in approach larger than the measurement uncertainty points to the cooler core, fan or airflow; an unchanged approach with a hotter outlet points to a hotter heat sink (ventilation, recirculation). Readings must be at matched duty.
What to take from it. An unchanged approach clears the cooler but does not restore lost margin. A hot room can still trip a healthy machine.
Technical content reviewed by D. Srinivas Reddy, Managing Partner and service engineer, Reddy Compressors. Last updated 17 October 2026. How our engineering content is reviewed.
Specific power comparison
Compare two compressors on what matters over life: the electrical power needed per unit of air delivered, and what that costs a year.
The worked example below shows the method with fixed numbers. Turn on JavaScript to change the inputs.
Worked example
Inputs
- Machine A: input power (kW): 75
- Machine A: delivered flow (m³/min): 11.5
- Machine B: input power (kW): 80
- Machine B: delivered flow (m³/min): 12.6
- Running hours per year: 6000
- Air actually needed (m³/min): 11
Result
- Machine A specific power: 6.52 kW per m³/min
- Machine B specific power: 6.35 kW per m³/min
- Energy to deliver the air needed: A: 4,30,435 kWh per year
- Energy to deliver the air needed: B: 4,19,048 kWh per year
- Energy difference: 11,387 kWh per year in favour of B
- Cost difference: Enter your electricity tariff (cost per kWh) above
Method. Specific power = input kW ÷ delivered flow (m³/min) at the same pressure and reference conditions. Annual cost = kW × hours × tariff. Use the full-load input power on the same test basis for both machines.
What to take from it. A small gap in specific power is multiplied by thousands of running hours. Compare on the same pressure and reference conditions.