Table of Contents
Vice President, Sales & Marketing of Zhejiang Haifeng Automation Equipment Co., Ltd
- Member of the Polyurethane Equipment Professional Committee, China Polyurethane Industry Association
- Member of the Expert Committee on Footwear and Apparel Equipment, China Leather Association
- Executive Vice President, Wenzhou Footwear Machinery Chamber of Commerce, China
By 2026, many of the rotary PU shoe production lines that were installed prior to 2020 are now structurally challenged in relation to cycle stability, thermal uniformity, and automation. Even the lines that run well will possess hidden deficiencies of process such as slight thermal drift in the moulds, change in the viscosity of the polyol, due to environmental humidity, demoulding delays which aggregate to 8 to 15% reduction in output, against design capacity, in an average environment.
Key parameters to inspect:
- Mixing head condition.Worn, uneven flow or residual curing process. A partially blocked high-pressure nozzle may lead to 20-25% lost casting precision.
- Mould temperature stability.Newer dual-density PU shoes should be stable to ±2°C across 12 to 18 cavities – old heaters were ±5-7°C.
- Automation interface.Older PLCs may not have the capability to be plugged into an IoT and may not be designed for remote monitoring and when required for predictive maintenance. Retrofits may not be possible.
- Another example, older lines were only capable of processing solvent based PU, switching to solvent free or bio based polyols may involve feeding system retrofit.
Even if heaters or pumps are being retrofitted, overlooking the aspect of flow uniformity in a dual-density mould may leave manufacturers with uneven midsoles. This is a low key slight defect, a flaw that will rarely trigger an alarm on quality control however will show less than desirable long term wear characteristics.
Retrofitting Ideas for Big Gains
1) Mixing Head and Metering System Changes
The mixing head in combination with BASF Haptex should be changed or installed.
- Metering:Given actual field metrics from a 2025 retrofit in Jiangsu that used process metering that retrospectively metering did not make up for operator error with either increased polyol or isocyanate, even if deglazing two drops to the output valves should be taken on to reach the correct volumes in proportion to control a faster cycle. Recalibration cut deviation a full percentage midsole density from ±7% to ±2.5% and resulted in greater output without increasing cycle time.
2) Demoulding and Thermal Optimisation
Older moulds may need to be retrofitted with embedded thermocouples and individually controllable heating zones. Lessons learned so far from data gathered in 2026 show:
- if unsubstantially hot spots do not heat the centre of the cavity faster hotfoot in the edges, there are going to be blisters outside.
- if subsequentially uncentred moulds, tend to mould that is hotter on one side than the other and require longer on the hot side later. That adds up to 3 to 4% more that is scrapped.
- Mould makers might have been unduly conscientious; slightly less cycle time, but better moderating and process adjustments, such invariably allows for an improvement.
3) Remote Diagnostics and Automation
One success story that proves their worth is in 2026, where integrating a remote monitoring system for legacy PU lines installed one for edge ware by about 4% per cycle. Was able to remotely monitor one in New York City easily prevent that dropped down to the room in the process.
4) New Material System
Cans have to reuse air, moisture in the effective ground, design to use the thinner and faster and feel to whip is on sight in heavy-duty shoes and OTR tires to discharge the material custom polymer.
- That moisture swings investing if foaming in winter coats lines not purely made in a low-medium.
Layout and Production Flow Improvements
- Cavity numbering and blind sequencing:Overhead waternaturally numbers of moulds and coupled brings about in reduced idled time in a dual-density line from 6% to 8%.
- Inline inspection and midway to collapse stage:Putting a central sensor and inline thickness into hone pours staggered make in stages at the gout and running reaches the trext.
- Energy recovery:Updating an efficiency award for fine air right fill method; design and connect energy costs cut 12 to 15% outmoded blindsPU, andas well as the size of the hot JPA needed.
Investment Priority for Upgrade
Upgrade Area | Investment | Impact | Applicability Condition |
Mixing head & pumps | Medium | High | 5–10 year-old heads, dual-density moulds |
Thermal control & demoulding | Medium | High | ±5 °C temperature on a soil scale |
Remote monitoring | Low | Medium | Low a line without IoT |
Material system conversion | Medium–High | High | Not Green light gas systems |
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Manufacturer Implementation and Endorsement
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FAQ
Q1: Is it possible to upgrade my 10+ year old rotary PU shoe line without replacing moulds?
At-least mould replacement isn’t necessary. Retrofitting embedded thermocouples, upgrading the heaters for a more uniform cavity temperature within each midsole during the production run, and recalibrating/adjusting the mixing head can readily restore or obtain production quality. However if you have a mold with really severe wear or a warped cavity profile, you’ll still need to replace the mould to maintain the required precision in your dual-density midsole.
Q2: I’m considering converting an old shoe line to solvent-free or bio-based PU; is that doable?
Yes, but your usual feeding systems might need some significant alteration. Closed loop polyol and isocyanate feeding, upgraded vacuum pumps, and controlled heating zones for foaming and material mixing and processing are generally advisable. Otherwise you risk getting erratic foaming and that promise of not having trapped air pockets might not hold up especially wanting it for heavy-duty footwear or readymade OTR shoes.
Q3: Will retrofit automation for my PU line really lower our labour expense?
It will reduce the operator intervention often required, but not eliminate it entirely. For a PU line operational pre-2015, your labour cost might drop by 10–15%, and on the throughput side, it could go up by 8–12% because of fewer unforeseen stoppages.
Q4: What kind of investment am I looking at generally for a moderate “high-impact” PU retrofit?
Depending on the scope:
- Mixing head and the metering system: medium investment, high impact
- Thermal/demoulding optimization: medium investment, high impact
- Remote monitoring and automation: low to medium investment, medium impact
- Material system conversion: medium to high investment, high impact
For full coverage most users would begin with the mixing head recalibration and thermal retrofit that typically returns the best ROI.
Q5: Are there restrictions for upgrading very ‘old’ PU lines?
Yes, lines older than 15+ years and in which the rotary systems received mechanical wear or outdated PLCs/development cards present integration hurdles. In these cases, retrofits may still lower the quality concerns, as opposed to achieving the throughput obtained by modern high-speed lines. Use our structured decision table to evaluate the correct time to take the partial route as opposed to going for outright ‘new’ line.
Q6: How long does retrofitting a PU line take?
Slightly ‘high-impact’ minor upgrades (mixing head, metering recalibration etc) can be completed in 2 to 4 weeks with minimal line downtime. Full automation plus operator removal for the solvent free material system can take 6 to 10 weeks depending on line size and complexity.
Q7: If we upgrade our PU line for less, can the new method deliver high capacity dual-density or OTR shoe production?
Yes, so long as you upgrade remodelling the metering accuracy, thermal properties and the material feeding system. In the 2025-2026 field cases, a 12-18 cavity dual-density and also foam filled rather heavy OTR footwear cases proved that the final metering quality remain intact, but “skipping” thermal or even flow calibration results in uneven midsole density even if the cycle time remains unchanged.