Updated: 2026 Technical Guide · By Sailwin Engineering Team
Most PET lines are managed with a single number: bottles produced per shift. That number moves for a dozen different reasons and tells you which of them caused the movement only if you already know the answer. A shift that produced fewer bottles because of a mould change and a shift that produced fewer bottles because the heating lamps drifted out of specification look identical on the production report.
The consequence is that improvement effort gets aimed at the wrong target. Factories buy a faster machine when their downtime is the constraint, or add a second operator when the real loss is minor stops on the take-out. Overall Equipment Effectiveness exists to prevent exactly this: it breaks the gap between theoretical and actual output into three measurable parts, each of which has a different owner and a different fix.
Sailwin has built PET blow molding machines for more than 15 years, with 500+ machines delivered to 60+ countries under CE and ISO 9001:2015 certification. Our machines use Siemens or Mitsubishi PLCs monitoring 40+ parameters in real time, which means the data needed for a proper OEE calculation is usually already being collected — the work is in defining the losses, not in buying instrumentation. This article sets out the calculation, a worked example on a PET line, and which losses actually dominate in practice.
Key Takeaways
- OEE = Availability × Performance × Quality, and the three factors have different owners. Reporting only the combined figure hides which of the three is moving, which is the only information that changes what you do next.
- Performance must be measured against the machine’s rated output, not against the best shift ever recorded. On a PET line the rated figure comes straight from the model specification — for example 7,500 BPH on an SW-F6-2000.
- A mould change under 30 minutes is a competitive advantage only if it is counted. If changeover time is not in the loss data, it is invisible to improvement and gets blamed on the machine’s speed instead.
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1. The Three Factors, Defined Without Ambiguity
OEE is the product of three ratios. Each answers a different question, and each is calculated from data that must be collected separately.
| Factor | Formula | Question it answers |
|---|---|---|
| Availability | Run time ÷ Planned production time | Was the machine able to run when it was supposed to be running? |
| Performance | (Total count × ideal cycle time) ÷ Run time | When it ran, did it run as fast as it is designed to run? |
| Quality | Good count ÷ Total count | Of what it produced, how much was saleable on the first pass? |
Two definitions decide whether the number is useful or decorative. Planned production time excludes only planned stops — shift breaks, scheduled maintenance, planned cleaning. Everything else the machine did not run counts against availability, including changeovers, breakdowns and waiting for a downstream fault. And ideal cycle time must come from the machine’s published rating, not from your best recorded shift. Using the best shift as the baseline builds the current inefficiency into the target and makes every figure look healthy.
2. A Worked Example on a PET Line
The following figures are an illustration using a Sailwin SW-F6-2000 (6 cavity, 7,500 BPH, containers up to 1,800 ml). Substitute your own shift length, downtime and counts to run the same calculation.
| Input | Value | Source |
|---|---|---|
| Shift length | 480 min | Roster |
| Planned break and handover | 30 min | Planned stop — excluded from OEE |
| Unplanned downtime | 24 min | Two stoppages logged on the machine HMI |
| Mould change | 28 min | Changeover log |
| Total bottles produced | 44,000 | Counter |
| Rejected bottles | 1,100 | QC and in-line inspection |
| Machine rating | 7,500 BPH (125 bottles/min) | SW-F6-2000 specification |
Step 1 — Planned production time: 480 − 30 = 450 min
Step 2 — Run time: 450 − 24 (breakdowns) − 28 (changeover) = 398 min
Step 3 — Availability: 398 ÷ 450 = 88.4%
Step 4 — Performance: (44,000 × 1/125) ÷ 398 = 352 ÷ 398 = 88.4%
Step 5 — Quality: (44,000 − 1,100) ÷ 44,000 = 42,900 ÷ 44,000 = 97.5%
Step 6 — OEE: 0.884 × 0.884 × 0.975 = 76.2%
The interesting part is not the 76.2%. It is that availability and performance fell by almost identical amounts, which points to two separate losses that need two separate fixes. Changeover time is 28 of the 52 lost minutes — over half the availability loss — and it is the one loss that can be attacked with tooling and procedure rather than with maintenance or capital. Performance at 88.4% means the machine was running roughly 11% below its rated speed while it ran, which is a heating, mould or take-out question rather than a downtime question.
Which Loss Should You Attack First?
Send one shift of starts, stops and counts. We will calculate availability, performance and quality and tell you where the real constraint sits.
An OEE figure without a loss breakdown is a score, not a tool. Before you publish a number to the factory, agree in writing what counts as a planned stop, who records a minor stop, and which count is the “good” count. Most of the arguments about OEE are not about the arithmetic — they are about definitions, and the definitions have to be settled once, by the production manager, not negotiated shift by shift.
3. The Losses That Matter on a PET Blow Molding Line
The classic six big losses map onto a PET line in particular ways. Knowing where each one normally comes from shortens diagnosis considerably.
| Loss | Affects | Typical PET-line source |
|---|---|---|
| Breakdowns | Availability | Heating lamp element failure, blown valve or cylinder seals, take-out gripper faults, preform feeder jams |
| Setup and changeover | Availability | Mould change, heating profile recall, cooling circuit reconnection, first-off approval |
| Minor stops | Performance | Preform misfeed, bottle jam on the air conveyor, label or packer blocker upstream, sensors needing a wipe |
| Reduced speed | Performance | Heating zones running below profile to avoid defects, cooling time extended, mould temperature drift, blowing pressure instability |
| Startup rejects | Quality | Bottles produced while the heating section and mould reached steady state after a changeover or restart |
| Production rejects | Quality | Wall thickness out of tolerance, base deformation, haze, ovality, seal surface damage |
Two of these deserve particular attention on PET lines. Minor stops are systematically under-recorded because nobody logs a fifteen-second jam, yet twenty of them in a shift is five minutes of lost run time plus the speed loss either side of each restart. And reduced speed is often a symptom rather than a cause: the machine runs slower because the heating profile is conservative or the cooling time was extended to hide a defect. Those are process problems wearing a production costume, and they will not be fixed by asking operators to run faster.
4. What a Good Number Looks Like
Reference bands for OEE are published widely in manufacturing literature. As industry-typical guidance rather than a Sailwin specification: world-class performance is commonly quoted at around 85% OEE, a well-run plant typically sits in the 70–80% range, and 60% or below indicates a substantial and usually identifiable loss that has been accepted as normal.
On a PET blow molding line specifically, availability is where the quickest gains usually sit. A machine designed for mould changes in under 30 minutes delivers that advantage only if the change is genuinely completed inside the window — and if the time is recorded, because a changeover that is never measured never gets shortened. Sailwin machines are built for that target specifically: quick-release cooling connections, mould clamping hardware designed for the change, and recipe storage for heating profiles so the profile is recalled rather than rebuilt.
Performance gains are usually slower and come from process stability: PID temperature control held to ±1°C so heating zones do not drift out of profile, stable blowing pressure in the 25–40 bar range, and reliable mould cooling. Quality gains on a PET line are frequently already good — which is why a plant with 97% quality should not spend its improvement budget there.
5. Sailwin Case Study: Finding the Real Constraint
- A beverage plant running a multi-format PET line with frequent SKU changes
- Management believed the machine was too slow and was preparing a capital request
- No structured downtime recording — shift reports captured output only
- Shift data split into availability, performance and quality using the machine’s rated output as the performance baseline
- Changeover time recorded separately, showing mould change as the largest single availability loss
- Heating recipes stored per SKU so the profile is recalled rather than re-established after every change
- Capital request withdrawn — the constraint was changeover procedure, not machine speed
- Changeover and startup scrap became visible and therefore manageable
- OEE adopted as the shift-level reporting measure, with losses attributed by category rather than by operator
Scenario based on a Sailwin customer project; final configuration is confirmed against your production data during engineering review.
6. Machine Features That Make OEE Measurable
- Siemens or Mitsubishi PLC monitoring 40+ parameters in real time. Heating zone temperatures, blowing pressure, timings and cycle data are recorded continuously, which is the raw material of a loss breakdown.
- PID temperature control to ±1°C. Stable heating is what allows the machine to sustain its rated speed rather than being held back for defect avoidance — the largest single source of performance loss on a PET line.
- Mould changes under 30 minutes. Directly addresses the availability loss that dominates on multi-SKU sites.
- Servo drive with up to 30% energy saving and, separately, high-pressure exhaust recovery that reduces air compressor load by around 20%. Energy is not part of OEE, but on a high-speed PET line it is a large enough cost to track alongside it.
- Full-load FAT before shipment, 3–7 days on-site commissioning, common wear parts shipped within 48 hours, 7×24 remote support and a 2-year whole-machine warranty. Spare part response is an availability issue: a machine waiting three weeks for a valve is a permanent OEE loss.
The model range runs from SW-F2-650 (2 cavity, 2,800 BPH up to 650 ml) through SW-F4-2000 (4 cavity, 4,500 BPH up to 1,800 ml) and SW-F6-2000 (6 cavity, 7,500 BPH up to 1,800 ml) to SW-F6H-800 (6 cavity, 12,000 BPH up to 800 ml) and SW-F8H-800 (8 cavity, 16,000 BPH up to 800 ml). Whichever model you run, the rated output on the specification sheet is the baseline your performance factor should be measured against — and if your recorded performance is consistently below it, the loss data will tell you why.
Frequently Asked Questions
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Related Reading:
• PET Blow Molding Machines — up to 16,000 BPH
• Operator Training for a PET Blow Molding Line
• Critical Spare Parts List for a PET Line
• PET Mould Cooling Water: Temperature and Flow Control
• How Much Does a PET Blow Molding Machine Cost?




