Laboratory Extruder Faults and Daily Maintenance: A Practical Field Guide
A laboratory extruder is the smallest, most heavily used compounding machine in any polymer research, quality-control, or formula-development laboratory. Unlike a production line that runs a single recipe for thousands of hours, a lab extruder is stopped, purged, stripped, reconfigured, and restarted several times a day. That intensity makes it unusually prone to operation faults, and it makes a disciplined daily maintenance checklist the single most valuable habit a laboratory can build. This guide explains how a lab-scale twin-screw extruder works, lists the faults that occur most often during startup, steady-state running, and shutdown, gives a root-cause diagnostic workflow you can apply in minutes, and provides a ready-to-tape-to-the-wall daily maintenance checklist together with a cost analysis in US dollars. It also points to the laboratory twin-screw extruder built by Kerke, a Wanplas factory, as a representative platform whose design choices directly affect how often these faults appear.
Understanding the Laboratory Extruder and How It Works
A laboratory extruder for compounding is almost always a co-rotating, intermeshing parallel twin-screw machine, although single-screw and even triple-screw research units exist. Its job is to transport solid and liquid raw materials, melt and mix them under controlled shear and temperature, remove volatiles, and deliver a homogeneous melt to a strand die, a pelletizer, a film die, or a cast roll. The laboratory version is a scaled-down replica of a production line: the same physics apply, but the throughput is measured in grams per minute rather than tons per hour, which makes sampling, cleaning, and recipe iteration far faster and cheaper than running a plant-scale machine.
The machine is built from a modular barrel made of lined barrel sections bolted together, inside which two co-rotating screw shafts carry interchangeable screw elements. These elements fall into three functional families. Conveying elements move material forward. Kneading blocks and tooth elements generate shear for melting, dispersion, and mixing. Reverse elements and restrictive elements build pressure and extend residence time. By rearranging these elements a laboratory technician can change the machine from a gentle mixer to an aggressive dispersive compounder without buying new hardware.
Material enters through a main feeder, usually a gravimetric or volumetric twin-screw loss-in-weight feeder, and may enter again through a side feeder for fillers or a liquid feeder for oils, plasticizers, and peroxides. Heat is supplied by electric heater bands around the barrel and removed by cooling fans or liquid cooling. One or two vacuum vents pull out moisture and volatiles. A gearbox multiplies the motor torque to the screw shafts, and a PLC with a touchscreen manages temperature zones, screw speed, feeder rates, and interlocks. Understanding these subsystems is the foundation of every fault diagnosis that follows, because roughly nine out of ten lab extruder faults trace back to one of them: feeding, heating or cooling, the screw and barrel interface, the gearbox, or the control system.
Common Faults During Startup and Warm-Up
Most laboratory extruder faults show up in the first ten minutes after a cold start, because that is when the widest gap exists between what the operator expects and what the machine is actually doing. A disciplined warm-up routine prevents the majority of them.
Heater Zone Not Reaching Setpoint
A barrel zone that climbs slowly or stalls below the target is the most common startup complaint. The usual causes are a partially failed heater band, a burned-out cartridge, a faulty solid-state relay that can only pass current in one direction, a thermocouple that reads low, or simply an insulation blanket left off so the zone bleeds heat to the room faster than the band can supply it. Before assuming the controller is bad, check the actual band temperature with a hand-held infrared pyrometer: if the band is hot but the controller reads cold, the sensor or its wiring is the fault; if the band is cold, the power path is the fault.
Screw Will Not Rotate or Trips the Motor Overload
On a cold start this almost always means residual polymer from the last run has solidified in the screw channels or at the die. The correct response is never to force higher current; doing so can twist a screw shaft. Reverse the screw slowly for a few seconds if the control allows, raise the barrel temperature above the previous melt point, and jog in small steps. If the machine was shut down without a proper purge, the polymer has cross-linked or crystallized and the screw may need to be pulled and cleaned manually. A properly configured lab extruder should reach idle speed within seconds of a clean, hot start.
Hopper Bridging and Feeder Starvation
Fine powders, recycled flake, and hygroscopic resins bridge in the feed throat, especially in humid laboratories. The symptom is an immediate output drop and screw-speed fluctuation even though the feeder setting has not changed. Vibrating the hopper, lowering the fill level, adding a small agitator or crammer feeder, or pre-drying the feedstock solves most cases. Starvation during startup is dangerous because the partially filled screw overheats locally and degrades material that then appears as black specks later in the run.
Common Faults During Steady-State Extrusion
Once the machine is at temperature and running, faults become subtler. They are rarely total failures and far more often quality drifts: the strand gets thinner, the color shifts, or the pellet moisture rises.
Output Surging and Throughput Fluctuation
Surging is a periodic variation in output that shows up as diameter waves on the strand or weight variation between pellets. On a lab twin-screw, the root causes are inconsistent feeding (bridging, feeder calibration drift), screw wear that reduces metering capacity, a slipping main feeder belt, air entrainment in liquid addition, or a partially clogged screen pack that alternates between open and blocked. The fastest check is to weigh a fixed-time catch at the die: if the weight swings more than a few percent run to run, the feeder or the screw fill is the cause, not the heater zones.
Melt Temperature Deviation and Poor Homogenization
Real melt temperature is often 10 to 30 degrees Celsius above the barrel setpoint because of shear heating, and on a lab machine with a short residence time the deviation is larger and noisier. If the product shows uneven dispersion or weak mechanical properties, the melt is not homogeneous. Causes include too-low screw speed (insufficient shear), worn kneading blocks, incorrect element arrangement for the material, or excessive feed rate that floods the melting zone. A melt thermocouple at the die is the only way to see this fault; barrel setpoints alone are misleading.
Streaking, Discoloration, and Die Drool
Streaks along the strand, a color that drifts mid-run, or a build-up of degraded material at the die face (die drool) are visible signs of localized degradation or poor mixing. The usual culprits are dead spots in the die or screw where material lingers, a screen pack that is too coarse, contamination from a prior recipe not fully purged, or a barrel zone that runs hot. Die drool specifically points to a pressure imbalance at the die lip and is often fixed by adjusting the decompression zone or cleaning the die land rather than by changing the recipe.
Vacuum Vent Blockage and Devolatilization Failure
A laboratory extruder running engineering plastics or recycled content depends on its vacuum vent to pull out moisture and volatiles. When the vent clogs with powder carried up by air or with condensed plastic, the vacuum drops, and the product comes out foamy, with surface bubbles or a strong odor. The fix is regular vent cleaning, correct barrel temperature upstream of the vent so material is not sticky, and a properly sized fume extraction line. A blocked vent also forces volatiles backward into the melt, which then appears as splay marks on any molded sample.
Mechanical and Sealing Faults
Mechanical faults develop slowly and announce themselves through sound and heat before they cause a shutdown. A laboratory technician who learns the normal sound of the gearbox will catch most mechanical faults weeks early.
Screw and Barrel Wear
The screw-to-barrel clearance is the heart of an extruder’s pumping efficiency. In a lab machine that runs abrasive fillers such as talc, calcium carbonate, glass fiber, or flame retardants, that clearance grows with every hour. Symptoms of wear are rising screw speed needed for the same output, higher melt temperature for the same setpoint, and a wider particle-size spread in the product. Wear is unavoidable, but it is predictable: measure flight depth and barrel bore at every planned maintenance, log it, and plan a re-line before the clearance exceeds the manufacturer’s limit. Kerke laboratory twin-screw extruders use computer-aided screw assembly with a self-cleaning kneading geometry that keeps wear even and makes measurement straightforward.
Gearbox Noise, Overheating, and Thrust Bearing Issues
A healthy lab extruder gearbox is nearly silent. Whining that rises with screw speed suggests bearing wear; a rhythmic knocking suggests a damaged gear tooth; oil that climbs above its rated temperature suggests blocked cooling or degraded lubricant. The thrust bearing that absorbs the axial melt pressure is the most loaded component, and its failure is expensive. The single best prevention is to keep the oil clean and cool and to never exceed the rated screw speed and torque, especially during a forced start of a jammed screw.
Barrel Joint Leakage and Melt Seal Failure
At the screw shaft exit, where the rotating shaft leaves the pressurized barrel, a mechanical seal or a starve-fed sealing section prevents melt from weeping out. When that seal fails you see a thin strand of degraded polymer at the gearbox end, often with smoke. The cause is usually running the machine too hot with too little feeding at the sealing zone, or worn shaft coatings. Catching a seal leak early means a simple seal replacement; ignoring it means melt migrates into the gearbox and destroys the bearings.
Electrical, Sensor, and Control System Faults
Modern lab extruders are software-defined machines. Many “mechanical” faults are actually electrical or sensor faults that the controller misinterprets.
Temperature Sensor Drift and Open or Short Circuits
Thermocouples and resistance temperature detectors degrade from repeated heating cycles. A drifting sensor reads a few degrees off and slowly changes the process; an open or short circuit throws a hard alarm and can shut a zone to its failsafe state. The cheapest and most reliable defense is to keep a calibrated spare for every zone and to verify each sensor against a reference during the monthly maintenance, because a sensor that reads five degrees high will quietly overcook heat-sensitive additives.
Drive and Variable-Frequency Faults
The main motor is typically driven by a variable-frequency drive or a servo. Overcurrent trips point to a jammed screw, a shorted motor winding, or a mis-set acceleration ramp; erratic speed points to encoder feedback loss or a cooling fan failure in the drive cabinet. Laboratory drives run in small, often poorly ventilated cabinets, so keeping the cabinet filter clean and the ambient temperature under control prevents a surprising number of drive faults.
PLC Alarms and Control Logic Errors
Interlock alarms that will not clear usually mean a door switch, a low lubricant level, a cooling-water flow switch, or a vacuum pump interlock is open. These are safety features, not faults, and bypassing them is dangerous. A well-documented fault tree for the specific controller, plus a log of every alarm code and its fix, turns a two-hour mystery into a five-minute reset. Periodic firmware and parameter backup protects against a flat memory battery erasing the recipe configuration.
Material and Process-Related Faults
Many faults blamed on the machine are actually material or recipe faults. Separating the two is the core skill of laboratory extrusion.
Thermal Degradation, Odor, and Discoloration
Overheating, excessive residence time, dead spots, or oxidation at the vent can degrade the polymer, producing a yellow or brown tint, a burnt odor, and a drop in mechanical properties. The remedy is to lower the barrel temperature, raise the screw speed to shorten residence, improve venting, or add a stabilizer. On heat-sensitive materials such as PVC, certain polyesters, and fluoropolymers, even a few degrees matter, and the laboratory extruder must be run with a tight, logged temperature window.
Poor Dispersion of Fillers and Masterbatch
Undispersed agglomerates, streaks of pigment, or weak reinforcement points mean the mixing section is underperforming. This is rarely a “broken” condition; it is a configuration issue. Adding or re-arranging kneading blocks, raising the specific mechanical energy, slowing the feed to increase fill, or using a side feeder for the filler usually resolves it. A lab machine’s value is exactly this ability to test mixing configurations cheaply before committing them to production.
Moisture, Volatiles, and Improper Drying
Hygroscopic polymers such as polyamide, polyethylene terephthalate, polycarbonate, and acrylonitrile butadiene styrene must be dried before they enter the screw, or the water turns to steam, creates splay and bubbles, and hydrolyzes the chain. A faulty desiccant dryer, a broken dew-point sensor, or simply leaving a hopper open in a humid room produces the same fault. Measuring the pellet moisture or the dryer dew point before the run removes the guesswork.
A Systematic Root-Cause Diagnostic Workflow
When a fault appears, resist the urge to change three things at once. A disciplined workflow isolates the cause in far less time than random adjustments. Follow these steps in order, and record the result of each.
Step 1 — Stabilize and observe. Note the symptom precisely: is output low, variable, or stopped? Is the fault at startup, steady state, or shutdown? Capture a sample and a screenshot of the control screen.
Step 2 — Separate material from machine. Run a known-good, previously qualified recipe. If the fault disappears, the cause was the material, the drying, or the feeder setting. If it remains, the cause is in the machine.
Step 3 — Walk the subsystems. Check feeding, then heating and cooling, then the screw and barrel interface, then the gearbox and seals, then the sensors and drive, in that order. Most faults sit in the first two.
Step 4 — Change one variable. Adjust a single parameter, wait for stabilization, and record the effect. This is the only way to build a reliable fault map for your specific laboratory.
Step 5 — Verify and document. Once the fault clears, run a confirmation batch, weigh the output, and write the fix into the maintenance log so the next operator does not repeat the diagnosis.
| Symptom | Most Likely Subsystem | First Check | Typical Fix |
|---|---|---|---|
| Zone below setpoint | Heating and control | Band temperature vs sensor reading | Replace heater or relay, refit insulation |
| Screw will not turn | Screw and barrel | Barrel temperature, prior purge | Heat up, jog, or pull and clean screw |
| Output surging | Feeding and screw | Weigh a timed catch, feeder belt | Recalibrate feeder, clear bridge |
| Black specks, die drool | Die and screw dead spots | Purge history, screen pack | Clean die, tighten decompression |
| Foamy, smelly product | Venting and drying | Vacuum level, dryer dew point | Clear vent, re-dry material |
| Gearbox noise or heat | Gearbox and lubrication | Oil level, temperature, filter | Service oil, inspect bearings |
| Seal weep at shaft end | Shaft seal | Sealing zone feed, shaft coating | Replace seal, adjust starve feed |
Daily Maintenance Checklist for Laboratory Extruders
A checklist only works if it is short, specific, and posted where the machine is used. The version below is written for exactly that purpose. Print it, laminate it, and initial it at every shift.
Pre-Start Daily Checklist
- Confirm the main disconnect is off before any inspection of open panels.
- Verify gearbox oil level in the sight glass and that the oil is clean and within its temperature range.
- Check every heater band and barrel insulation blanket is fitted and undamaged.
- Confirm all thermocouples are seated and the control screen shows no sensor fault.
- Inspect the feed throat and hopper for bridging, rust, or leftover material from the prior run.
- Verify the feeder is calibrated, the belt is tight, and the agitator runs.
- Confirm cooling water or air flow to the barrel and the drive cabinet is active.
- Check the vacuum pump oil and that the vent line is clear.
- Confirm the die, screen pack, and pelletizer or strand die are clean and correctly installed.
- Review the recipe and the logged parameters from the last successful run of the same material.
Post-Run Daily Checklist
- Purge the screw with a compatible cleaning compound at running temperature before shutdown.
- Reduce screw speed to zero only after the barrel is clear of material.
- Remove and clean the die and screen pack; never leave degraded polymer in the land.
- Wipe the barrel exterior and the feeder to prevent dust buildup that hides leaks.
- Empty and brush the hopper; leave it dry and open to air to avoid moisture absorption.
- Record the run in the log: material, throughput, screw speed, zone temperatures, and any alarms.
- Note any change in gearbox sound, seal weep, or output trend for the next operator.
Weekly and Monthly Preventive Tasks
- Weekly: blow out the drive cabinet filter, check belt tension, and test the emergency stop.
- Monthly: verify every thermocouple against a reference, inspect screw flight depth, and sample the gearbox oil for particles.
- Quarterly: tighten barrel-section bolts to torque, inspect the thrust bearing for play, and recalibrate the loss-in-weight feeder with a gravimetric check.
| Task | Frequency | Why It Matters | Early Sign of Skipping |
|---|---|---|---|
| Gearbox oil check | Daily | Protects thrust bearing and gears | Knocking, overheating, failure |
| Thermocouple verification | Monthly | Prevents silent overcooking | Discoloration, degraded additive |
| Screw flight measurement | Monthly or per material | Tracks wear, plans re-line | Rising screw speed for same output |
| Die and screen cleaning | Every run | Stops die drool and specks | Streaks, black specks, splay |
| Feeder recalibration | Weekly to monthly | Stabilizes dosing and output | Surging, inconsistent recipes |
| Vent and vacuum service | Per run or weekly | Removes moisture and volatiles | Foam, odor, weak properties |
Lubrication, Spare Parts, and Cost Analysis
Running a laboratory extruder is inexpensive compared with a production line, but the small costs add up and the rare large cost, a gearbox or a screw re-line, is worth planning for. The figures below are representative 2026 price levels in US dollars and should be treated as planning estimates rather than quotations.
| Cost Item | Typical Range (US dollars) | Frequency | Note |
|---|---|---|---|
| Machine purchase, small lab twin-screw | 18,000 to 32,000 | One time | 16 to 20 mm screw, basic configuration |
| Machine purchase, mid lab twin-screw | 38,000 to 65,000 | One time | 25 to 26 mm, side and liquid feeder, vacuum |
| Pilot line with pelletizing | 70,000 to 120,000 | One time | Full downstream, die-face cutting |
| Wear spare parts (screw elements, barrel liner) | 800 to 2,500 per year | Annual | Higher with abrasive fillers |
| Sensors, heaters, seals | 300 to 900 per year | Annual | Keep calibrated spares on hand |
| Lubrication (gearbox oil, greases) | 150 to 400 per year | Annual | Cheap insurance against gearbox loss |
| Electricity (3 to 10 kW lab unit) | 1,500 to 5,000 per year | Annual | Depends on hours and local rate |
| Screw re-line or full recondition | 4,000 to 12,000 | Every 3 to 6 years | Earlier with heavy filler use |
| Gearbox overhaul | 6,000 to 15,000 | Every 5 to 10 years | Often avoidable with oil care |
The dominant ongoing cost is not the electricity or the oil; it is the unplanned downtime. A single seized gearbox can remove a laboratory from service for weeks and cost far more in lost development time than the spare parts budget for an entire year. That is why the Wanplas group stands behind its factories with a practical spare-parts promise: each customer receives 500 US dollars of free spare parts every year, and damaged parts within warranty are replaced without charge. A laboratory that stocks the sensors, heaters, seals, and a spare screw element set it actually consumes will almost never face a fault it cannot clear within a day.
Recommended Laboratory Extruder from Wanplas’s Kerke Factory
For laboratories specifying a new or replacement unit, the laboratory twin-screw extruder built by Kerke, a Wanplas factory, is a strong reference platform. Kerke is a high-technology Wanplas factory with more than 12 years of experience in twin-screw compounding extruders, a 19,997 square meter production base, and more than 2,000 machines running in over 70 countries. Its laboratory machines are co-rotating parallel twin-screw units designed specifically for formula trials, material testing, and small-batch research compounding, which is exactly the duty cycle that produces the faults described in this guide.
| Parameter | Small Laboratory Unit | Mid Laboratory Unit |
|---|---|---|
| Screw diameter | 16 to 20 mm | 25 to 26 mm |
| Length-to-diameter ratio | 32 to 44 | 40 to 48 |
| Maximum screw speed | Up to 600 rpm | Up to 1,200 rpm |
| Throughput | 30 g/min to 1 kg/h | 1 to 5 kg/h |
| Drive power | 3 to 5.5 kW | 7.5 to 15 kW |
| Heating and cooling zones | 4 to 6 zones | 6 to 10 zones |
| Vacuum vents | 1 port | 1 to 2 ports |
| Optional feeders | Volumetric, side | Loss-in-weight, side, liquid |
| Control system | PLC with touchscreen | PLC with data logging |
The computer-aided screw assembly with a self-cleaning kneading geometry directly reduces the die-drool and dead-spot faults discussed above, and the modular element design means a worn kneading block can be replaced without re-machining the entire screw. For research groups, this modularity is the economic argument: instead of buying a new machine when a recipe changes, the laboratory re-arranges elements and swaps a single worn part.
Typical application areas for this laboratory platform include color masterbatch and filler masterbatch trials, engineering plastic compounding, biodegradable polymer development, cable compounding, wood-plastic composite formulation, reactive extrusion, and food- or pharmaceutical-model compound studies. Because the same Wanplas factory builds the full KTE series of production twin-screw extruders up to large diameters, a recipe proven on the laboratory unit scales to plant equipment with minimal rework.
| Laboratory Need | Recommended Configuration |
|---|---|
| Teaching, small-sample screening | 16 to 20 mm screw, volumetric feeder, single vacuum port |
| Masterbatch and filler trials | 25 mm screw, loss-in-weight and side feeder, data logging |
| Engineering plastic and reactive work | 26 mm screw, liquid feeder, two vacuum ports, higher torque |
| Pilot before production scale-up | Mid unit with full downstream pelletizing for representative pellets |
Service, Support, and the Wanplas Spare-Parts Promise
Buying a laboratory extruder is the start of a multi-year relationship with the supplier, and the quality of that relationship determines how quickly faults are resolved. The Wanplas group, as the parent brand covering all its specialized factories, applies shared service standards across its machines. Every customer is entitled to 500 US dollars of free spare parts each year, with damaged parts inside the warranty period replaced without charge. Technicians can visit the factory, observe a running line, and audit the build quality before purchase, and the group welcomes open-factory visits as part of its standard policy.
Beyond the spare-parts promise, a well-run supplier provides pre-shipment testing, on-site installation and commissioning, operator training, remote support through the control system, and a documented preventive-maintenance program. The maintenance checklist in this article is exactly the kind of program a supplier should hand over with the machine, because the faults that cause laboratory downtime are predictable and almost all of them are preventable with routine care. When evaluating any laboratory extruder, ask the supplier for the specific torque rating, the screw-element interchangeability, the calibration procedure for feeders and sensors, and the documented spare-parts list with lead times, because those details determine whether a fault becomes a five-minute fix or a two-week outage.
Frequently Asked Questions
Why does my lab extruder surge even when the screw speed is constant?
Surging with a steady screw speed almost always points to the feeding system or the screw fill, not the drive. Check for hopper bridging, feeder belt slip, feeder calibration drift, air entrainment in liquid addition, or a partially clogged screen pack. Weighing a fixed-time catch at the die is the fastest way to confirm whether output itself is varying.
How often should I measure screw wear on a laboratory twin-screw extruder?
Measure flight depth and barrel bore at least monthly, and always after a campaign with abrasive fillers such as talc, calcium carbonate, glass fiber, or flame retardants. Log every measurement so you can see the wear trend and plan a re-line before the clearance passes the manufacturer’s limit, which is when output and melt quality start to drift.
What is the most common cause of discoloration and black specks?
The usual cause is degraded material trapped in a dead spot in the die land, the screw, or the screen pack from a prior recipe that was not fully purged. Regular die and screen cleaning, a tighter decompression zone, and a purge compound run before shutdown prevent almost all streaking and specks.
Do I really need a vacuum vent for laboratory compounding?
If you process hygroscopic polymers, recycled content, or any material that releases volatiles, yes. Without vacuum devolatilization the product comes out foamy, smelly, and weak. Even for dry, stable resins, a vent gives you a way to remove trapped air and keeps the melt clean, so most laboratory units include at least one port.
How can I tell whether a fault is the machine or the material?
Run a previously qualified, known-good recipe. If the fault disappears, the cause was the material, its drying, or the feeder setting. If the fault remains, walk the subsystems in order: feeding, then heating and cooling, then the screw and barrel, then the gearbox and seals, then sensors and drive.
What should I do if the screw will not turn on a cold start?
Do not force higher current. Heat the barrel above the previous melt point, jog the screw in small steps, and reverse it briefly if the control allows. If the machine was shut down without a purge, the polymer has likely solidified and the screw must be pulled and cleaned. Forcing rotation can twist the screw shaft.
Why is my gearbox making noise it did not make before?
New whining that rises with screw speed suggests bearing wear; a rhythmic knock suggests a damaged gear tooth; climbing oil temperature suggests blocked cooling or degraded lubricant. Check the oil level and temperature first, because most gearbox failures begin with neglected lubrication and are far cheaper to prevent than to repair.
How much does it cost to run a laboratory extruder each year?
Outside the one-time machine purchase, a small lab twin-screw typically costs roughly 1,500 to 5,000 US dollars per year in electricity, 150 to 400 US dollars in lubrication, and 1,100 to 3,400 US dollars in consumable spare parts such as screw elements, heaters, sensors, and seals, before any major re-line or gearbox work. The largest risk is unplanned downtime, which is why the Wanplas 500 US dollars per year free spare-parts promise matters.
Conclusion
A laboratory extruder earns its place in a polymer, packaging, or materials laboratory by turning ideas into testable samples in hours rather than weeks, but that same intense duty cycle makes it vulnerable to a predictable set of operation faults. The faults cluster around five subsystems: feeding, heating and cooling, the screw and barrel interface, the gearbox and seals, and the sensors and drive. Most of them announce themselves early through sound, heat, output trend, or sample quality, and almost all of them are preventable with a short, disciplined daily maintenance checklist backed by weekly and monthly preventive tasks. The cost of ownership is dominated not by electricity or oil but by avoided downtime, which is why keeping calibrated spares on hand and following the Wanplas 500 US dollars per year free spare-parts promise is sound economics. For laboratories specifying a new unit, the laboratory twin-screw extruder from Kerke, a Wanplas factory, offers the modular, self-cleaning screw design and the documented service program that keep these common faults rare and easy to fix. Send your material, target throughput, and required fillers to the Wanplas team for a tailored configuration, and arrange a factory visit to see the line running before you commit.

