Film KPIs

Film Converting KPIs and Benchmarks: OEE, Yield, Gauge, and Web Break Targets

OEE, material yield, gauge and coat weight capability, web breaks, changeover, barrier pass rate, energy and solvent recovery: how to measure each film KPI, what moves it, and which figures have a cited source.

A film or converting plant needs about ten numbers on the wall: OEE, door to door material yield, scrap rate, gauge 2 sigma, coat weight capability, web breaks per 100 roll changes, changeover time, first pass barrier pass rate, energy per kg and solvent recovery efficiency. Use the ranges below as reference points for spotting a gap, not as targets. Typical and world class plants differ by a factor of 2 to 4 on most of them no cited source.

Every figure here shows its basis. A superscript number links to a public source in the Sources list at the end, and the sentence states that source's scope. A figure marked no cited source is kept exactly as originally published because it has not been verified against a public source, so treat it as illustrative.

At a glance

Specialty film and converting KPI benchmarks at a glance
KPITypicalStrongBasis
OEE, cast and blown film lines55 to 70%85% or higher (world-class, all manufacturing)85%: Raju; Gopalakrishnan1, 2; 55 to 70% no cited source
OEE, coating and lamination lines45 to 60%70 to 75% (world class)no cited source
Door to door material yield82 to 90%93 to 96% (the best)no cited source
Edge trim, share of web widthNot stated< 4% (should stay under)no cited source
Startup scrap, jobs over 5,000 kgNot stated< 2% of run weightno cited source
Unavoidable scrap reground or resold< 40%> 70% (world class)no cited source
Gauge 2 sigma5 to 8% blown; 3 to 4% modern cast< 2% (world class)no cited source
Coat weight Cpk≥ 1.33 (minimum)1.67 (best stations)1.33: Minitab3; 1.67 no cited source
Web breaks, thin gauge or high tension1 per 5 to 10 rolls< 1 per 50 rolls (world class)no cited source
Coating job changeover60 to 120 min20 to 40 min (world class)no cited source
Slitter set changeNot stated< 15 min (should finish under)no cited source
First pass barrier pass rate92 to 96%> 99% (world class)no cited source
Barrier release turnaroundNot stated< 48 hours (hold under)no cited source
Film energy intensity, polyethylene0.9 to 1.4 kWh/kg0.74 HDPE; 0.97 LLDPE kWh/kg (state of the art)DOE bandwidth study4
Dryer energy per kg of solvent evaporated> 12 MJ/kg (signals air leaks)< 6 MJ/kg (strong, with heat recovery)no cited source
Carbon bed solvent removal> 95% (should exceed)98 to 99% (world class)EPA cost manual5
Retained solvent, food contact laminateNot stated< 5 mg/m2 (must stay under)no cited source
Figures are as originally published unless a source is cited. The cited OEE and Cpk figures are cross-industry benchmarks, the energy figures are DOE on-site values per unit of resin for all film production, and the carbon bed figure is removal efficiency, not line capture. Where the original used a word other than typical or strong, that word is kept in the cell. Not stated means the original gave no figure for that column.

Method: How the figures in this guide are sourced

A figure with a superscript number is stated by the cited source, listed under Sources with its publisher and access date, and the sentence says what the source covers. A figure marked no cited source is kept exactly as originally published because no public source stating it has been verified. It is illustrative, not measured industry data.

Overall equipment effectiveness

Overall equipment effectiveness (OEE) for cast and blown film lines typically runs 55 to 70 percent no cited source. The world-class mark is 85 percent or higher, a general manufacturing benchmark that traces to Seiichi Nakajima's total productive maintenance work rather than a film-specific measurement1, 2.

Coating and lamination lines run lower, at 45 to 60 percent typical and 70 to 75 percent world class, because changeovers and drying limited speeds punish both availability and performance no cited source.

The single biggest OEE lever in converting is changeover. Plants that cut job changes from 90 minutes to 35 minutes typically gain 5 to 8 OEE points at normal run lengths no cited source.

How to measure

  • Multiply availability, performance and quality for each line.
  • Score performance against a demonstrated rate per structure, not nameplate, so a 40 micron nylon structure is not judged against LDPE speeds.
  • Report film lines separately from coating and lamination lines.

What moves it

  • Changeover time, the biggest single lever.
  • Drying limited speeds on coating and lamination lines.

Set a demonstrated rate standard per structure with the Extrusion Throughput calculator.

Door to door material yield and scrap

Door to door material yield is salable kg shipped over raw material kg consumed. It runs 82 to 90 percent at typical converters and 93 to 96 percent at the best no cited source.

Measurement method matters as much as the target. A plant reporting 97 percent yield measured only at the slitter is usually an 85 to 88 percent plant when measured from resin receipt to shipped roll no cited source.

Edge trim should stay under 4 percent of web width, and startup scrap under 2 percent of run weight on jobs over 5,000 kg no cited source. World class plants regrind or resell more than 70 percent of unavoidable scrap; typical plants manage under 40 percent no cited source.

How to measure

  • Measure from resin receipt to shipped roll, not at the slitter.
  • Track yield by structure.
  • Set scrap targets in kg per changeover rather than percent, or short runs always look bad while long runs hide waste.

What moves it

  • Edge trim width.
  • Startup scrap on each job.
  • Regrinding or reselling the scrap you cannot avoid.

Put a cost on scrapped rolls by structure with the Roll Scrap Cost calculator.

Gauge and coat weight capability

Gauge 2 sigma of 5 to 8 percent is typical for blown film, 3 to 4 percent for modern cast lines with automatic dies, and under 2 percent is world class no cited source. Every point of gauge variation is roughly a point of resin giveaway no cited source.

At that rate, a 2 point improvement on a 10,000 tonne per year line saves about 200 tonnes of resin.

Coat weight should hold a process capability index (Cpk) of at least 1.33 against spec limits, the benchmark value many industries use according to statistical software maker Minitab3. That is a cross-industry convention, not a coating-specific standard.

The best stations hold 1.67 with sigma under 3 percent of target no cited source.

How to measure

  • Gauge 2 sigma: two standard deviations of thickness as a share of nominal thickness, from weekly scanner data.
  • Coat weight Cpk: from cut and weigh data against the spec limits.

What moves it

  • Automatic die control on cast lines.
  • Weekly review of scanner and cut and weigh data, so drift is caught early.

Turn scanner and cut and weigh data into capability numbers with the Film Gauge Variation calculator and the Coating Weight Yield calculator.

Web breaks

Typical converters see 1 break per 5 to 10 rolls on thin gauge or high tension products, while world class operations run below 1 per 50 rolls no cited source.

Log every break with web position and suspected cause. Of those, 60 to 70 percent usually trace back to splice quality and slit edge defects, both fixable within a quarter no cited source.

How to measure

  • Count breaks per roll, split by product and gauge.
  • Record web position and suspected cause for every break.

What moves it

  • Splice quality.
  • Slit edge defects.
  • Maintenance effort ranked by break cost, so it follows the money.

Rank products by break cost with the Web Break Cost calculator.

Changeover time

For a coating job change, 60 to 120 minutes is typical, and 20 to 40 minutes is world class with staged tooling and premixed adhesive no cited source. Slitter set changes should finish in under 15 minutes no cited source.

How to measure

  • Time each change from the last good roll of one job to the first good roll of the next.
  • Track coating and slitter changes separately.

What moves it

  • Staged tooling.
  • Premixed adhesive.

See what faster set changes are worth in slitter hours with the Slitting Capacity calculator.

First pass barrier pass rate

For barrier products, first pass barrier pass rate is the share of lots that meet oxygen transmission rate (OTR) and water vapor transmission rate (WVTR) spec on the first test. Typical plants pass 92 to 96 percent first time; world class holds above 99 percent no cited source.

World class plants get there by controlling the upstream drivers: EVOH layer uniformity and bond strength above 2.5 N per 15 mm no cited source.

Instrument time is a hard constraint, because an OTR cell needs 4 to 24 hours per specimen no cited source. Plan lab capacity for it and hold release turnaround under 48 hours no cited source. Plants that let turnaround drift to a week end up either shipping at risk or sitting on 100 tonnes of unreleased inventory.

How to measure

  • Divide lots that meet OTR and WVTR spec on the first test by lots tested.
  • Track release turnaround from sample pull to release.

What moves it

  • EVOH layer uniformity.
  • Laminate bond strength.
  • Lab capacity planned against specimen test time.

Energy intensity

Polyethylene blown film plants typically run 0.9 to 1.4 kWh per kg of film4. In the Department of Energy's 2017 bandwidth study, on-site current typical energy intensity for film production in 2010 was 1,626 Btu per lb of resin for HDPE film and 2,126 for LLDPE film, about 1.05 and 1.37 kWh per kg4.

The band does not fit every resin. The same study puts LDPE film at 4,127 Btu per lb and polypropylene film at 5,420, about 2.67 and 3.50 kWh per kg4. Its figures cover on-site energy for all film production per unit of resin, not blown film alone.

Efficient plants cut energy with variable speed drives, insulated barrels and optimized cooling. The study's state of the art, meaning the best commercially available practice, is 1,146 Btu per lb for HDPE film and 1,498 for LLDPE film, about 0.74 and 0.97 kWh per kg4.

Coating lines should track MJ per kg of solvent evaporated instead. Below 6 MJ/kg is strong with heat recovery, and above 12 signals air leaks or excessive exhaust volume no cited source.

How to measure

  • Film lines: kWh per kg of film, from metered electricity and fuel.
  • Coating lines: MJ per kg of solvent evaporated in the dryer.

What moves it

  • Variable speed drives.
  • Insulated barrels.
  • Optimized cooling.
  • Dryer heat recovery, and fixing air leaks and excessive exhaust volume.

Solvent recovery and retained solvent

Solvent removal by a carbon bed system should exceed 95 percent, with 98 to 99 percent world class5. EPA's Air Pollution Control Cost Manual puts properly designed, operated and maintained carbon adsorbers at 95 to 99 percent VOC removal at inlet concentrations of 500 to 2,000 ppm5.

Removal by the bed is not the same as capture from the line. EPA's 2006 Control Techniques Guidelines for flexible package printing note that since around 1990 many vendors have guaranteed capture efficiency of 85 to 90 percent without a permanent total enclosure6. Overall control, capture times removal, is therefore lower than the bed's efficiency.

For solvent-based flexible package printing presses, those guidelines recommend 65 to 80 percent overall VOC control, depending on when the press and control device were installed6. The 80 percent level rests on 85 percent capture and 95 percent control device efficiency; coating and laminating lines fall under separate state rules6.

Retained solvent in finished laminate must stay under 5 mg/m2 for food contact work no cited source. No regulatory text stating that limit has been verified, so confirm the limit that applies with your customer.

How to measure

  • Removal efficiency: solvent recovered or destroyed by the bed over solvent entering it.
  • Capture efficiency: solvent reaching the control device over solvent used on the line.
  • Retained solvent: mg per square meter in finished laminate, by lot.

What moves it

  • Carbon bed design, operation and maintenance.
  • Enclosure and exhaust design, which set capture.
  • Dryer performance, which sets retained solvent.

How to build your own baseline

  • Instrument first: automatic scrap weighing, break logging and per structure rate standards.
  • Collect 8 to 12 weeks of data before setting targets no cited source.
  • Then attack only the top two losses.
  • Review KPIs weekly at the line and monthly by structure.
  • Benchmark against your own best demonstrated performance.

Most converting plants find changeover time and gauge giveaway are worth 3 to 5 margin points combined, more than any capital project under $1 million no cited source.

The best week in the last 26 defines what the equipment can actually do, and closing half the gap to it within a year is a realistic target no cited source.

Sources

  1. Anatomization of the overall equipment effectiveness (OEE) for various machines in a tool and die shop. Journal of Intelligent Manufacturing and Special Equipment, Vol. 3 No. 1, pp. 97-105 (Emerald, CC BY 4.0), DOI 10.1108/JIMSE-01-2022-0004. published 2022. p. 101 (PDF p. 5), Table 1 'The world-class OEE factor', and the preceding paragraph attributing the figures to Nakajima's Introduction to TPM. Accessed September 30, 2026.
  2. Machine criticality assessment for productivity improvement: Smart maintenance decision support. International Journal of Productivity and Performance Management 68(5):858-878 (Chalmers University of Technology repository copy). published 2019. Section 1 Introduction, p. 1 of article (PDF p. 3). Accessed September 30, 2026.
  3. Interpret the key results for Normal Capability Analysis. Minitab, LLC (Minitab Statistical Software support documentation). Step 'Evaluate potential capability (Cpk)'. Accessed September 30, 2026.
  4. Bandwidth Study on Energy Use and Potential Energy Savings Opportunities in U.S. Plastics and Rubber Manufacturing. U.S. Department of Energy, Advanced Manufacturing Office. published September 2017. Table 3-2 (on-site current typical energy intensity, Btu/lb resin, 2010) and Table 4-2 (on-site state-of-the-art energy intensity), Film Production rows. Accessed September 30, 2026.
  5. EPA Air Pollution Control Cost Manual, Section 3.1 Chapter 1: Carbon Adsorbers. U.S. Environmental Protection Agency, Office of Air Quality Planning and Standards. published October 2018. Section 1.1 Introduction (PDF p. 5). Accessed September 30, 2026.
  6. Control Techniques Guidelines for Flexible Package Printing (EPA 453/R-06-003). U.S. Environmental Protection Agency. published September 2006. Section IV Add-On Controls (capture and control device efficiency); Section VI.A Recommended control levels. Accessed September 30, 2026.

Published 2026-07-02.