| HS Code | 203504 |
| Productname | Braskem HDPE HDI2061 |
| Polymertype | High Density Polyethylene (HDPE) |
| Density | 0.954 g/cm3 |
| Meltindex | 0.20 g/10 min (190 C/2.16 kg) |
| Tensilestrengthatyield | 27 MPa |
| Tensilestrengthatbreak | 31 MPa |
| Elongationatbreak | 600% |
| Flexuralmodulus | 1240 MPa |
| Notchedizodimpactstrength | 80 J/m |
| Shoredhardness | 66 |
| Vicatsofteningtemperature | 126 C |
| Meltingpoint | 131 C |
| Heatdeflectiontemperature | 71 C at 0.45 MPa |
| Brittlenesstemperature | -70 C |
| Environmentalstresscrackresistance | >1000 h |
| Waterabsorption | <0.01% |
| Moldshrinkage | 2.0% |
| Processingmethod | Blow Molding |
| Processingtemperature | 190-210 C |
| Form | Pellets |
| Color | Natural |
As an accredited Braskem HDPE HDI2061 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Braskem HDPE HDI2061 is typically packaged in 25 kg polyethylene bags, stacked on pallets and stretch-wrapped for secure transport. |
| Container Loading (20′ FCL) | 20′ FCL loading for Braskem HDPE HDI2061: palletized 25 kg bags, shrink-wrapped, dry container, secured, roughly 22–25 MT payload. |
| Shipping | Braskem HDPE HDI2061 is typically shipped as non-hazardous high-density polyethylene resin pellets in 25-kg bags, octabins, or bulk containers. It is not DOT/IMDG/IATA regulated, with no UN number or hazard class. Keep packages dry, sealed, and protected from sunlight, moisture, and contamination during transport and storage. |
| Storage | Store Braskem HDPE HDI2061 in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and flames. Keep original packaging sealed and palletized to prevent moisture, dust, and contamination. Avoid prolonged UV exposure and excessive stacking. Maintain ambient storage temperatures, observe first-in, first-out stock rotation, and follow supplier safety data sheet recommendations. |
| Shelf Life | Shelf life: 24 months from production when stored in original unopened packaging, cool, dry, protected from direct sunlight. |
In high-speed tamper-evident closure production, HDI2061 is processed at melt temperatures between 180 °C and 230 °C, with mould temperatures maintained between 10 °C and 30 °C to control shrinkage and tamper-band geometry. The grade’s nominal melt flow rate of 20 g/10 min under ISO 1133-1:2022 at 190 °C/2.16 kg permits filling of 48-cavity hot-runner tools without excessive injection pressure, but the same flow behaviour reduces melt strength at the parting-line shutoffs, which must be managed through valve-gate timing rather than elevated hold pressure alone. Food-contact status for closures is evaluated under 21 CFR 177.1520 for olefin polymers and EU No 10/2011 with overall migration limits of 10 mg/dm² using aqueous, acetic acid, and ethanol simulants; organoleptic testing is addressed through end-use water-contact panels because HDPE can carry low molecular weight oligomers that affect taste at sub-ppm thresholds. Formulations for high-speed beverage caps typically comprise 96–99 wt% HDI2061, 1–3 wt% pigment masterbatch based on a compatible high-flow HDPE carrier, and 0.2–0.5 wt% erucamide slip masterbatch. Slip-masterbatch loadings above 0.5 wt% should be avoided where torque retention under hot-fill or carbonated conditions is a specification item because surface migration can reduce removal torque below the lower cap-feel threshold. Production-scale lines use reciprocating-screw injection machines with clamp forces of 3,000–4,500 kN for 48-cavity cold-runner or hot-runner closure tools; barrel temperature profiling from 170 °C at the feed throat to 210 °C at the nozzle, screw back pressure of 5–15 bar, injection velocity above 150 mm/s, and cycle times of 4.5–7.5 s are observed when the mould has conformal cooling cores and side-entry valve gates. Closures are seated under controlled torque and tested for tamper-band break behaviour according to internal specifications because no single ISO standard covers all closure geometries. Finished components include single-piece water bottle closures with tamper-evident bands, still and carbonated beverage caps, and lightweight dairy snap-screw caps. For carbonated soft drink applications, HDPE does not provide CO₂ barrier, and a liner or barrier insert is required to meet headspace loss specifications.
When lower-flow HDPE is replaced by HDI2061 in thin-wall injection moulding, the filling pressure profile changes because the material’s melt flow rate is higher than conventional blow-moulding or extrusion grades. In moulding a 0.7–1.0 mm wall thickness round dairy container, peak hydraulic injection pressure is typically 800–1,200 bar for a 4+4-cavity stack mould, while a low-flow HDPE of 3 g/10 min may require pressures above 1,400 bar and gate temperatures that create label film distortion. The pressure advantage disappears if the injection speed is below 200 mm/s because the flow front freezes prematurely at the rim and thickens the sidewall, producing visible flow lines under in-mould labels. Material compliance for dairy tubs and lids is controlled by EU No 10/2011 and 21 CFR 177.1520; specific migration of stabilisers and processing aids must be below the limits listed in Annex II of the EU regulation. In-mould label constructions must meet EU 1935/2004 for food-contact materials, and migration test methods follow EN 1186-1. Formulations for dairy tubs are normally 92–98 wt% HDI2061, 1–5 wt% white masterbatch with titanium dioxide, and 1–3 wt% LLDPE if sidewall splitting occurs at low ambient temperatures. LLDPE addition above 5 wt% reduces the nominal MFR to below 14 g/10 min and raises gate blush on the rim; therefore addition is used only when environmental stress crack resistance or hinge tear resistance is the limiting specification. IML production uses robot-placed polypropylene labels in the injection tool; the melt temperature is maintained at 200–220 °C, coolant temperature at 8–12 °C, and hold pressure is set at 45–60% of peak injection pressure. Clamp force for a 4+4 stack tool is generally 3,500–5,000 kN. In-mould label reheat and shrinkage cause curl if the label film thickness exceeds 80 µm or if the label has an oriented layer; the fast filling of HDI2061 reduces heat transfer into the label, but poor label adhesion is normally traced to under-packing at the container bottom rather than melt temperature. Terminal products include round dairy tubs for butter, margarine, soft cheese, and dessert portions, as well as thin-wall lids with tear-back tabs.
| Regulatory anchor | Scope | Test condition |
|---|---|---|
| 21 CFR 177.1520 | Olefin polymers for food contact | End-test extraction under simulated use |
| EU No 10/2011 | Plastic food-contact materials | Overall migration 10 mg/dm²; simulant A/B/D2 as per food type |
| EN 1186-1 | Migration test methods | Total immersion or pouch method at 40 °C for 10 days or equivalent |
| EU 1935/2004 | Framework regulation | Traceability and good manufacturing practice under Article 3 |
Across 16–32-cavity cosmetic cap tools, polypropylene is not the only material used for flip-top and disc-top caps; HDI2061 is moulded into snap-fit caps where lower creep and higher density provide a different tactile response than polypropylene. The main production defect on cold-runner tools is gate vestige protrusion above the cap top deck, because the high melt flow of HDI2061 permits the screw to decompress too aggressively, drawing air into the melt pool at the end of plasticating. A decompression setting above 8–12 mm can produce splay and gate blush in clear or pearlescent caps, especially when the nozzle body is run above 230 °C. Cosmetic packaging shell materials are assessed under EU 1223/2009 for product safety by the responsible person; polyolefin caps must also meet EU No 10/2011 if the product is applied around the mouth or food-like, and U.S. packaging falls under 21 CFR 174.5 general indirect food additive requirements when appropriate. Heavy-metal migration is controlled by EU 94/62/EC packaging directives with a sum limit of 100 mg/kg for lead, cadmium, mercury, and chromium VI, and by CONEG state legislation in the United States. Cosmetic cap formulations commonly contain 93–99 wt% HDI2061, 1–5 wt% pearlescent or custom color masterbatch, and 0.1–0.3 wt% antistatic masterbatch for dust-resistant clear caps. Metallic pigment loadings above 2 wt% tend to increase melt viscosity locally and cause flow lines; lower-viscosity carriers are selected to maintain MFR above 18 g/10 min. High-speed closure machines for cosmetic caps use direct-gated cold-runner tools with 16 or 32 cavities, melt temperatures of 180–210 °C, mould temperatures of 12–20 °C, and cycle times of 8–12 s when wall thicknesses are between 1.0–1.5 mm. Stacking force in logistic automation is measured as top-load resistance on finished closures under ASTM D2659, with pass values dependent on cap diameter and thread geometry. Finished products include disc-top caps, snap-fit lids for cream jars, fragrance overcaps, and duplex caps where HDPE forms the inner shell. For clear caps, the absence of nucleating agents in HDI2061 produces higher haze than polypropylene, so clarity specifications must be lower than those applied to clarified PP.
In the 5–25 L open-top pail segment, HDI2061 is used where the high-flow behaviour shortens cycle time, but the grade must be evaluated against ASTM D1693 environmental stress crack resistance before it is used with aggressive fill goods such as surfactants, chlorinated solvents, or essential oils. Published data for ESCR of HDI2061 in concentrated surfactant exposure is limited, and field validation on a finished pail under 40 °C storage is required because laboratory bent-strip tests do not reproduce pail stress at the handle boss and bottom corner. UN-certified pails for dangerous goods must pass the drop test and stack test provisions of the UN Model Regulations Chapter 6.1.5, including drop on the most critical chimb or handle boss at −18 °C after conditioning. Food-grade pails must comply with 21 CFR 177.1520 and EU No 10/2011; for fatty foods, migration simulant D2 is used under the applicable time-temperature conditions. Pail formulations are 94–99 wt% HDI2061, 0.5–2.0 wt% UV/HALS masterbatch for outdoor storage, and 1–3 wt% colour masterbatch. Antistatic packages of 0.5–1.0 wt% are used for dry powder pails; conductive carbon black formulations should not exceed 5 wt% because low-temperature drop performance degrades. Production uses accumulator-assisted injection moulding machines with clamp force from 8,000–12,000 kN for a single-cavity 25 L pail tool, with injection pressure between 1,000–1,300 bar, hold pressure 500–700 bar, and cooling time 25–35 s. The fast-flow grade reduces melt cushion fluctuation; however, if the machine uses a shutoff nozzle with a material decompression above 10 mm, the sprue can string and create a deformable area at the gate dome. Handling arms demould the pail at 55–65 °C surface temperature; ejection below that range causes the pail sidewall to stick on the core due to shrinkage of HDPE. Terminal articles include black and white pails for paints, construction chemicals, detergent powders, and sealed food ingredients, plus lids with integral tear-strip access.
At −20 °C, impact failure in household storage totes moulded from HDI2061 is controlled by the orientation of the weld line rather than by the base resin alone. These articles have thinner nominal walls than extrusion-blow-moulded alternatives, with sidewall thicknesses of 1.2–2.0 mm, and a weld line at the handle root that freezes at a nozzle melt temperature below 190 °C will fracture under a lower drop height than a part moulded at 215 °C. HDI2061 has limited published notched impact data, and finished-item drop testing should be performed in accordance with ASTM D5420 at the intended service temperature, because laboratory notched specimens do not capture the orientation and internal stress state of the moulded tote. Household storage totes that are coloured or marketed as toy-adjacent articles must meet EN 71-3 migration limits for certain heavy metals; REACH Annex XVII restrictions apply to phthalates and PAHs; U.S. testing under 16 CFR 1303 for lead in surface coatings is relevant only if painted. Formulations contain 95–99 wt% HDI2061 and 1–5 wt% colour masterbatch; clarified grades may use 0.5–1.5 wt% of a clarifying masterbatch, although HDI2061 does not deliver the transparency of clarified polypropylene. Impact modifiers are generally unnecessary for indoor household articles; if outdoor storage is required, 0.3–0.8 wt% hindered amine light stabiliser masterbatch and 0.1–0.2 wt% UV absorber are compounded, not dry blended, to prevent streaking. Manufacturing lines use standard hydraulic injection machines with clamp forces of 4,000–8,000 kN, single-cavity or two-cavity family tools, melt temperature set between 190–220 °C, and mould temperature 15–25 °C. Fast injection ramps above 180 mm/s fill the base and rim without jetting, but pack pressure must be reduced to 30–40% of peak before gate freeze to avoid overpacking the lid hinge and increasing breakage during the first closing cycle. Finished products include underbed storage totes, stackable wardrobe boxes, cleaning caddies, pantry containers, and modular drawer inserts.
Because HDI2061 has a melt flow rate of 20 g/10 min, the use in returnable bottle crate sleeves is marginal, and the grade is only suitable when the sleeve wall is reduced to 1.8–2.2 mm to save material. The high flow allows lower injection pressure, but cycle time becomes limited by the gate area rather than filling. Field observations on hot-runner four-drop tools show that using a gate diameter below 2 mm with HDI2061 can cause premature gate freeze during holding, which produces sink marks at the crate rim and reduces stack load resistance. Returnable transport packaging is not directly food-contact but must comply with REACH Article 33 communication obligations for substances of very high concern and with EU 94/62/EC heavy-metal limits. If the crates transport unpeeled agricultural produce, plastic packaging may be evaluated under EU 1935/2004 as a food-contact material in an application-specific way; published migration data for HDI2061 in this configuration is limited. Formulations for thin-wall crate sleeves can include 80–95 wt% HDI2061 and 5–20 wt% recycled HDPE from closed-loop bottle crates; the higher recyclate content lowers MFR and improves stiffness but increases die drool and gate blush. Recyclate addition above 20 wt% is not recommended without a multi-stream dosing audit because viscosity variation shifts the fill time enough to alter weld-line position at the handle cut-out. Crate sleeves are moulded on machines with 12,000–16,000 kN clamp force; melt temperature is set at 200–225 °C, mould temperature at 10–20 °C, and holding pressure at 500–800 bar. The cycle time is typically 18–25 s; lowering coolant temperature below 8 °C does not further shorten cycle time because the gate freezes first, and condensation on the mould surface can create surface blush on the textured crate flutes. Terminal products are low-weight crate sleeves over-moulded or welded to separately moulded frames, stack-nest beverage crates, and reusable agricultural trays.
| Property / failure mode | Reference method | Validation condition |
|---|---|---|
| Notched impact resistance | ISO 180/1A | −20 °C, finished-wall specimen where possible |
| Drop impact | ASTM D5420 | Boss and rim impact at −20 °C |
| Environmental stress crack resistance | ASTM D1693 Condition B | 10% Igepal CO-630, 50 °C |
| Stack load | Internal or UN 6.1.5.3 | 40 °C, 28 days or transport-specific |
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Braskem HDPE HDI2061 is an injection-moulding high-density polyethylene grade supplied as pelletized ethylene homopolymer. The product designation HDI2061 identifies a high-flow injection-moulding resin; it is not a pipe, film, or blow-moulding grade. The nominal melt flow rate is 20 g/10 min when measured at 190°C under a 2.16 kg load in accordance with ASTM D1238, and the nominal density is 0.956 g/cm³ when measured by ASTM D792. Equivalent international test designations for these properties include ISO 1133-1 and ISO 1183-1. The high flow places the material in the thin-wall rigid packaging, closure, and housewares segment. Published datasheet values for laboratory-moulded test specimens include a tensile yield strength near 26 MPa (ASTM D638), flexural modulus near 1,350 MPa (ASTM D790), and Vicat softening temperature near 126°C (ASTM D1525). These values are nominal and should not replace batch-specific certificate data for production release. The material’s processability is governed by fast solidification, low melt pressure drop, and the need to control gate geometry, cooling balance, and regrind history.
| Property | Typical value | Test designation |
|---|---|---|
| Melt flow rate | 20 g/10 min | ASTM D1238 |
| Density | 0.956 g/cm³ | ASTM D792 |
| Tensile yield strength | 26 MPa | ASTM D638 |
| Flexural modulus | 1,350 MPa | ASTM D790 |
| Vicat softening temperature | 126°C | ASTM D1525 |
| Elongation at break | 12% | ASTM D638 |
| Notched Izod impact | 30 J/m | ASTM D256 |
These test values are obtained from standard specimens moulded under controlled conditions. The presence of colourant, masterbatch, or regrind at production scale will shift flow and impact response.
At injection shear rates commonly encountered in thin-wall filling—1,000–10,000 s-1—the apparent viscosity of a 20 g/10 min HDPE is lower than that of an 8 g/10 min general-purpose injection HDPE. This lowers the pressure drop along the flow path and permits shorter fill times or reduced clamp force in the same tool. On production-scale hydraulic toggle-clamp machines with 18:1–22:1 L/D general-purpose polyolefin screws and compression ratios of 2.5:1–3.0:1, melt temperatures for HDI2061 are normally maintained between 200°C and 240°C. Mould temperatures of 20–40°C are used because rapid solidification is needed to prevent sticking and stabilize ejection in high-cavitation tools. Back pressure is limited to 0.3–0.7 MPa to avoid excessive shear heating and screw recovery variation. First-stage injection pressure in thin-wall tools is typically observed between 70 MPa and 110 MPa, with transfer to holding pressure at 50–75% of peak fill pressure. Quantitative reductions in pressure are tool-specific and should be established by short-shot studies and in-mould pressure transducers when wall thickness is below 1.0 mm.
Because the grade solidifies quickly, holding pressure is applied for short periods. In thin-wall containers, hold time of 2–5 s is common, while cooling time is determined by part thickness and mould temperature. Mould shrinkage for this class of HDPE is generally between 1.5% and 2.0% in flow and cross-flow directions, but cavity-to-cavity temperature imbalance above 2°C produces warpage. For hot runner systems, manifold temperatures of 220–230°C and tip temperatures of 230–240°C are used. Lower tip temperatures create cold slugs at the gate, while higher temperatures accelerate oxidation of the melt stream.
Gate geometry and venting define the practical lower wall thickness for HDI2061. In closure tools with nominal wall thickness of 0.8 mm, subgates of 0.8 mm diameter and 0.6 mm land length are commonly used. Reducing the gate diameter below 0.5 mm may still fill the cavity because of the high flow, but shear heating at the gate can cause surface melt fracture, gate blush, or streaks. Vent depths in high-flow HDPE tools are usually specified between 0.015 mm and 0.025 mm, with land lengths of 0.8–1.2 mm. Vents deeper than 0.03 mm are avoided because the low melt viscosity allows rapid penetration and flash. Insufficient venting produces burn marks at flow fronts, particularly in rectangular containers with flow length-to-wall-thickness ratios above 150:1. Raising injection speed alone does not correct venting defects and can introduce more gas at the flow front.
High-flow HDPE is selected for closure and thin-wall packaging tools when cavity count exceeds 24 and projected area is large relative to available clamp force. The lower filling pressure of HDI2061 can permit the same part to be moulded on a smaller clamp force than a lower-MFR HDPE, because clamp force requirement is a function of cavity pressure and projected area. For a thin-wall cylindrical container with wall thickness 0.9 mm, a high-flow HDPE may show peak cavity pressure at the end of fill of 25–40 MPa, while a general-purpose HDPE may require 35–50 MPa under identical fill time. These differences are not guaranteed; they depend on gate number, flow length, melt temperature, and injection velocity profile. Process engineers should use in-mould pressure sensors to avoid overpacking near the sprue and underpacking at the last cavity. Balanced runner layout is required because viscosity differences across the cavity can shift fill order and produce part-weight variation above ±0.05 g in closures.
Compared with a lower-flow injection HDPE, HDI2061 reduces screw recovery torque, but the lower molecular weight also reduces melt strength. In hot runner systems, filament drooling from valve gates is controlled by decompression stroke of 3–6 mm; excessive decompression pulls air into the melt and creates silver streaks. On injection units with 20:1 L/D screws, shot sizes of 30–60% of rated barrel capacity are recommended for the grade. Shots below 20% of barrel capacity increase residence time and may degrade the resin; shots above 60% can reduce melt temperature uniformity.
Regrind use introduces the largest lot-to-lot variation in HDI2061. Because the grade flows easily, repeated heat history reduces viscosity further and can cause black specks, yellowing, and inconsistent cushion control. Converters producing non-food housewares generally tolerate 10–15 wt% internally generated regrind when screw speed is held between 80–120 rpm and melt temperature is kept below 240°C. Above 20 wt% regrind, shot-weight variation and splay become measurable in high-cavitation tools. For food-contact closures, regrind use must be validated under the packaging producer’s food-safety plan and may be restricted by end-use specifications of FDA 21 CFR 177.1520 or EU Regulation 10/2011. The addition of colour masterbatch at 2–4 wt% can increase melt flow and may require a 5–10°C reduction in rear barrel temperature to prevent over-flow and flash.
Below 1.0 mm wall thickness, HDI2061 can fill high-cavitation moulds only if gate size, venting, and mould temperature are controlled within narrow limits. A hot runner with valve gate tips of 0.8–1.2 mm diameter is preferred for closures. Gate diameters below 0.5 mm may cause shear-induced degradation at the gate. Cooling time for a 0.8 mm wall is often 8–12 s at a mould temperature of 30°C, but coolant-channel placement, inlet coolant temperature, and mould steel conductivity influence the result. The maximum mould temperature differential across a cavity should not exceed 2°C to prevent differential shrinkage and warpage. Shrinkage measurements after 24 h at 23°C and 50% relative humidity are used to verify dimensional stability; at least 10 consecutive shots should be measured after stable cycle conditions are achieved.
Wall-thickness transitions are a source of jetting and hesitation lines. HDI2061, because of its high flow, is less prone to hesitation than lower-flow HDPE, but jetting can occur if the gate enters an open cavity without contacting a nearby wall. To avoid jetting, the gate should be placed so the melt impinges on a wall within 2–3 mm of the gate. In deep-draw containers, injection velocity profiling is used: a slow initial velocity of 30–50 mm/s establishes flow-front integrity, followed by fast fill at 150–250 mm/s for thin-wall sections, and a short packing phase. Shot-to-shot cushion should remain 2–5 mm; larger cushions increase residence time, and smaller cushions introduce pressure loss at the screw tip.
Differences between HDI2061 and other HDPE products are expressed mainly in melt flow rate, notched impact, environmental stress-crack resistance, and targeted processing. High-flow injection grades have lower molecular weight than blow-moulding and pipe grades, which reduces impact and ESCR. The following table shows representative class values for high-flow injection HDPE, general-purpose injection HDPE, and blow-moulding HDPE; the HDI2061 column uses the typical published values from Table 1, while the other columns are representative published class data and must be confirmed against specific product datasheets.
| Property | HDI2061 high-flow injection | General-purpose injection HDPE | Blow-moulding HDPE |
|---|---|---|---|
| Melt flow rate | 20 g/10 min | 7–10 g/10 min | 0.2–0.5 g/10 min |
| Density | 0.956 g/cm³ | 0.960 g/cm³ | 0.955 g/cm³ |
| Flexural modulus | 1,350 MPa | 1,500 MPa | 1,200 MPa |
| Notched Izod impact | 30 J/m | 50 J/m | 160 J/m |
| Typical ESCR | Not specified or limited | Low to moderate | High |
| Processing method | Thin-wall injection moulding | General injection moulding | Extrusion blow moulding |
The comparison shows the operational boundary of HDI2061. Its 20 g/10 min melt flow rate reduces viscosity and improves filling in thin sections, but the lower molecular weight implied by high flow reduces notched impact and environmental stress-crack resistance. HDI2061 is therefore not specified for pressure pipe, fuel tanks, or aggressive ESCR bottle applications; published data for those configurations under ASTM D1693 condition B is limited or absent from converter datasheets. For rigid housewares and thin-wall closures, the stiffness and dimensional consistency of the higher-density grade are more important than ESCR. Compared with linear low-density polyethylene of density 0.918 g/cm³, the HDI2061 density of 0.956 g/cm³ gives higher flexural modulus and better stackability but lower dart drop impact; the change in density alone is not a substitute for ESCR screening when chemical contact is involved.
Food-contact converters using HDI2061 should verify compliance through the supplier’s letter of assurance. High-density ethylene homopolymers of this class are generally evaluated under FDA 21 CFR 177.1520 and EU Regulation 10/2011, but overall migration and organoleptic performance must be confirmed on the finished package because masterbatch, regrind, and processing aids alter the final compliance status. The grade is not recommended for long-term outdoor exposure unless UV stabilizers are added; unstabilized HDPE loses elongation and develops surface oxidation under accelerated weathering tests such as ASTM D4329. In UL 94 testing, the material is a combustible polyolefin and is not rated for flame-retardant applications. REACH documentation is maintained under Regulation EC 1907/2006, and converters must maintain lot traceability for SVHC communication under Article 33. Material substitution into an existing tool should include mould-flow simulation, physical property verification, and production trials at the actual machine clamp force and barrel size.