| HS Code | 814748 |
| Density | 0.960 g/cm³ |
| Melt Flow Rate 190 C 2 16 Kg | 6.0 g/10 min |
| Tensile Strength At Yield | 29 MPa |
| Tensile Strength At Break | 20 MPa |
| Elongation At Break | 800% |
| Flexural Modulus | 1300 MPa |
| Notched Izod Impact At 23 C | 80 J/m |
| Vicat Softening Temperature | 127°C |
| Heat Deflection Temperature At 0 45 Mpa | 75°C |
| Shore D Hardness | 65 |
| Melting Temperature | 134°C |
| Mold Shrinkage | 1.8-2.2% |
As an accredited Braskem HDPE JV060U factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Braskem HDPE JV060U is supplied in 25 kg polyethylene bags, 40 bags per pallet, stretch-wrapped for transport. |
| Container Loading (20′ FCL) | Braskem HDPE JV060U loaded in 20-foot FCL containers: palletized 25 kg bags, securely strapped, maximizing payload for ocean transport. |
| Shipping | Braskem HDPE JV060U is typically shipped as free-flowing polyethylene pellets in 25 kg PE bags, 500–1,000 kg bulk bags, or bulk trucks/railcars. Keep dry, away from direct sunlight and contamination. Store in a cool, ventilated area and follow the safety data sheet. |
| Storage | Store Braskem HDPE JV060U in a cool, dry, well-ventilated warehouse away from direct sunlight, heat, and ignition sources. Keep original packaging sealed, on pallets off the floor, and protect from moisture, dust, and chemical contamination. Avoid excessive stacking and prolonged high temperatures. Store away from strong oxidizers. Use first-in, first-out rotation and follow the manufacturer’s SDS and local regulations. |
| Shelf Life | Shelf life is typically indefinite under proper storage: keep in original packaging, cool, dry, ventilated area, away from sunlight and ignition sources. |
In high-cavitation injection moulds producing 150 mL to 500 mL thin-wall dairy cups, spreadable-margarine tubs, and portion packs, Braskem HDPE JV060U is processed under simultaneous constraints of low melt viscosity at high shear, rapid crystallisation against a cold cavity wall, and reproducible part ejection within cycle times below 6 s. The nominal melt flow rate of 6.0 g/10 min determined under ASTM D1238-20 at 190 °C/2.16 kg and nominal density of 0.957 g/cm³ under ASTM D792-20 permit downgauging from 0.9 mm to 0.75 mm in selected sidewalls without exceeding tool deflection limits. Food-contact conformity requires FDA 21 CFR 177.1520 for olefin polymers, Regulation (EU) No 10/2011 overall migration limits, and Regulation (EC) No 2023/2006 for good manufacturing practice. White masterbatch is blended at 2 wt% to 4 wt%; erucamide slip packages are introduced at 500 ppm to 1,000 ppm to reduce stacked-cup friction without exceeding organoleptic thresholds for dairy products. Screw plastication units with L/D ratios of 20:1 to 24:1 and compression ratios from 2.2:1 to 2.8:1 are used; barrel profiles are set from 180 °C at the feed throat to 230 °C at the metering zone, with nozzle temperature at 220 °C to 235 °C. Mould temperature control at 10 °C to 20 °C uses turbulent-flow cooling circuits to stabilise the frozen skin layer and reduce sink marks opposite the gate. Injection velocity profiles start at 120 mm/s to 180 mm/s and taper to 60 mm/s to 90 mm/s before transfer to holding pressure at 30 MPa to 50 MPa. Observed failure modes on high-speed lines include short shots in cavities farthest from the sprue when melt temperature drops below 210 °C, gate blush when first-stage velocity exceeds 200 mm/s, and rim warpage when cooling time is reduced below 3.5 s.
| Regulatory framework | Reference or test method | Numerical limit or condition |
|---|---|---|
| US FDA food contact | 21 CFR 177.1520 | Olefin polymer; HDPE extractives limits specified in paragraph (c) |
| EU plastics food contact | Regulation (EU) No 10/2011 | Overall migration <10 mg/dm²; additive-specific SML values apply |
| GMP for food-contact materials | Regulation (EC) No 2023/2006 | Documented traceability and process control; no unapproved additives |
| Heavy metals restriction | RoHS Directive 2011/65/EU | Pb <1000 ppm; Cd <100 ppm; Hg <1000 ppm; Cr6+ <1000 ppm; PBB/PBDE <1000 ppm |
Automated filling and sealing lines require open-rim squareness tolerances of ±0.3 mm and sidewall wall-thickness uniformity within ±0.05 mm. The grade is typically not predried; however, if surface moisture is observed after outdoor storage, drying for 2 h at 80 °C is applied. End products include dairy cream cups, yogurt containers, and margarine tubs with lids.
Injection-compression moulding of 28 mm to 38 mm tamper-evident closures for still water, aseptic juice, and HDPE dairy bottles exposes JV060U to a process where gate freeze time and crystallisation shrinkage of the annular sealing surface determine seal integrity and removal torque. The nominal tensile yield strength of approximately 26 MPa under ASTM D638-14 and flexural modulus near 1,100 MPa under ASTM D790-17 are used in thread deflection calculations and tamper-evident band bridging. Environmental stress cracking resistance is assessed under ASTM D1693-15, Condition B in 10% Igepal CO-630 at 50 °C; because the method has known scatter, closure specifications require F50 values verified on the finished bottle geometry rather than standard plaques. Multi-cavity tools with 64 or 96 cavities require nozzle melt temperatures between 230 °C and 250 °C, mould temperatures between 10 °C and 25 °C, and holding pressures from 40 MPa to 70 MPa to avoid sink marks at the top disc and thread root. Erucamide slip packages are normally added at 500 ppm to 1,200 ppm; levels above 1,200 ppm can reduce the coefficient of friction below 0.20 but may cause plate-out on core pins and reduce ESCR after 30 days of ageing. Primary phenolic and secondary phosphite antioxidants at 0.08 wt% to 0.15 wt% protect the melt during hot-runner residence. End products include single-piece tamper-evident closures, snap-on caps, and linerless sealing closures.
Dimensional stability in the sealing zone is strongly influenced by the cooling sequence at the gate and the cavity ring. Tools with reverse-taper plug seals and valve-gated hot runners produce lower warpage than cold-runner direct-gated tools, but the melt must remain above 220 °C at the nozzle to prevent flow lines through the tamper-evident band. Closure removal torque is typically checked at 24 h after moulding and again after 14 days of ambient storage; values drift upward when post-mould crystallisation continues in the thick thread root. For still water closures, the coefficient of friction of the thread surfaces is maintained between 0.20 and 0.35 by controlling erucamide addition and mould release; lower values may cause back-off under vibration, while higher values raise application torque above filling-line limits.
For pails with fill volumes from 10 L to 25 L and open-top or lid-and-handle configurations, wall thicknesses range from 2.0 mm to 4.0 mm. The moulding constraint is not short-shot filling but differential shrinkage between the bottom gate region, the sidewall, and the handle attachment bosses, which produces top-out-of-roundness and stack failure under static top load. JV060U is specified because its narrow molecular weight distribution reduces post-mould warpage in thick sections and provides repeatable top-load performance. For outdoor storage pails, hindered amine light stabilisers at 0.10 wt% to 0.30 wt% and carbon black or coloured masterbatch at 2 wt% to 5 wt% are used. Barrel temperatures are set from 190 °C to 240 °C, with mould temperature at 8 °C to 15 °C to accelerate skin formation. Injection speed is lower than thin-wall packaging, with fill times from 2.5 s to 5.0 s, and holding pressure is maintained for 10 s to 18 s to compensate for volumetric shrinkage at the thick rim. A hot-runner valve gate of 3.0 mm to 5.0 mm diameter is typical; smaller gates freeze prematurely before the holding phase and create voids in the handle pillar. Stack-load tests follow ISO 2234:2015 at 23 °C and often at 40 °C for 28 days; values of 250 kg for 20 L pails are common but must be validated on the filled container because the handle attachment acts as a buckling initiation site. UN-certified dangerous goods pails require additional drop testing and hydrostatic pressure testing under Chapter 6.1 of the UN Model Regulations; final certification belongs to the packaging, not the polymer, and regrind use is limited to 20 wt% maximum to maintain impact consistency.
Production-scale failure modes include localised sink marks at the handle bridge when the holding pressure is switched too early, and stress whitening at the ejector pins when the part is stripped before the core surface reaches 60 °C. Differential cooling between the bottom and the sidewall can increase vertical ovalisation beyond 2.0 mm; adjustable mould-core cooling circuits are used to keep the temperature difference across the tool below 5 °C.
Across bread trays, bottle crates, and agricultural harvesting crates, JV060U operates under repeated impact at low ambient temperatures and requires load-bearing sidewalls with open grid structures that resist creep during warehouse stacking. The melt flow rate of 6.0 g/10 min is sufficient to fill large-area tools with flow lengths exceeding 1,000 mm when multi-gate layouts are used, but the low-viscosity character must be managed to avoid jetting and weld lines at moulded-in ribs. For cold-climate service, blending with 5 wt% to 10 wt% of linear low-density polyethylene can improve low-temperature impact resistance as measured by the notched Izod test under ASTM D256-10; however, flexural modulus decreases by approximately 5% to 10% at the upper inclusion level, and top-load deflection must be revalidated. Processing uses clamp forces from 450 t to 1,200 t depending on projected area, with melt temperatures between 220 °C and 250 °C and mould temperatures from 10 °C to 30 °C. Gate sequences and valve delays are programmed to move weld lines away from high-stress nodes at the crate base. Dimensional checks follow ASTM D638-14 for tensile yield and ASTM D790-17 for flexural modulus as incoming-quality references, not as finished-part tests. End products include stackable food crates, dairy transport trays, mushroom harvesting trays, and automotive parts bins. Compliance with REACH SVHC thresholds and RoHS Directive 2011/65/EU is standard for industrial crates exported to European markets. Published data for this specific configuration of JV060U in sub-zero crate applications is limited; site-specific impact testing is required before tool commissioning.
In large tools with multiple hot-drop gates, short shots and flow hesitation occur when the first-stage injection pressure is set below 60 MPa or when the melt temperature at the last hot runner nozzle falls below 215 °C. Craters and sink marks opposite rib intersections are controlled by maintaining packing pressure for 8 s to 14 s and by using gas counter-pressure when the tool has a sealed parting line.
For thick-walled cosmetic jars, airless pump over-caps, and lotion container bases produced from JV060U, the primary evaluation criterion is environmental stress cracking resistance against ester-based oils, fatty alcohols, and solvent-containing emulsions. The nominal melt flow rate of 6.0 g/10 min under ISO 1133-1:2022 fills multi-cavity tools with wall thicknesses between 1.8 mm and 5.0 mm while maintaining stable dimensional output. Nominal tensile yield strength near 26 MPa and flexural modulus near 1,100 MPa are used by tool engineers to design snap-fit lugs and thread profiles that do not creep beyond the release torque specification after 48 h of conditioning at 50 °C. The processing envelope uses melt temperatures from 210 °C to 235 °C, mould temperatures from 10 °C to 20 °C, and holding pressures from 35 MPa to 55 MPa; pack-and-hold time is extended to 8 s to 12 s for the thick base sections to prevent internal voids that reduce crush resistance. Colour masterbatch loadings of 1 wt% to 3 wt% are typical for opaque packaging, and UV absorber packages at 0.1 wt% to 0.3 wt% are added for shelf stability. The grade must be stored in sealed containers when relative humidity exceeds 60%; predrying is generally not required unless visible surface moisture is present. End products include body cream jars, hair mask containers, and snap-fit over-caps for airless dispensers; migration of processing slip additives into the filled product is typically below the analytical threshold when erucamide loadings are kept under 1,000 ppm.
In production-scale cosmetic packaging, surface gloss defects and flow lines are controlled by maintaining the mould-core surface temperature above 15 °C and by sequencing valve gates in family tools so that no cavity receives a pressure spike greater than 80 MPa. Crack initiation in snap-fit undercuts is assessed by stripping the undercut after 12 h to 24 h of crystallisation; premature ejection or excessive undercut depth above 1.5 mm can create microcracks that propagate under alcohol-based formulations.
Within medical non-implantable packaging applications, including specimen transport containers, diagnostic kit housings, and snap-cap vials for dry reagents, JV060U is evaluated when low-temperature impact after refrigeration or frozen transport is combined with clean-room moulding and chemical resistance to dilute disinfectants. The material can be assessed under ISO 10993-5 for cytotoxicity and ISO 10993-10 for irritation when the finished article is evaluated; the polymer grade itself does not carry an automatic biocompatibility certification and must be validated with the specific masterbatch and mould-release system used. Clean-room injection moulding keeps airborne particulate concentrations within ISO Class 8 or better under ISO 14644-1:2015; regrind use is prohibited or limited to 0 wt% to 10 wt% for patient-contact packaging. Ethylene oxide and gamma irradiation are common terminal sterilisation methods; gamma irradiation at 25 kGy to 50 kGy can generate free radicals that lead to embrittlement and yellowing unless the grade is compounded with radiation-tolerant stabiliser packages, and published data for JV060U under irradiation is limited. Processing conditions are conservative: melt temperature 200 °C to 230 °C, mould temperature 10 °C to 25 °C, injection speed 80 mm/s to 150 mm/s, and holding pressures 30 MPa to 50 MPa to prevent sink marks at thick bosses. End products include specimen collection cups with leak-resistant snap lids, diagnostic reagent trays, and transport containers for clinical samples.
Validation of low-temperature impact is normally performed by conditioning the finished article at -20 °C for 24 h and subjecting it to a drop test from 1.0 m onto a rigid steel plate; the acceptance criterion is no crack or fracture at the hinge or snap features. Because gamma irradiation can reduce notched Izod impact by 20% to 40% in unstabilised polyethylene, a radiation-stabilised masterbatch is required when the package undergoes sterilisation doses above 25 kGy.
Competitive Braskem HDPE JV060U prices that fit your budget—flexible terms and customized quotes for every order.
For samples, pricing, or more information, please contact us at +8618136850665 or mail to admin@ascent-chem.com.
We will respond to you as soon as possible.
Tel: +8618136850665
Email: admin@ascent-chem.com
Flexible payment, competitive price, premium service - Inquire now!
Braskem HDPE JV060U is an injection-moulding grade of high-density polyethylene with a nominal melt flow rate of 6.0 g/10 min at 190 °C under 2.16 kg, determined according to ASTM D1238 and ISO 1133-1. The grade is specified at a nominal density of 0.960 g/cm³, which places it in the high-rigidity segment of the HDPE range. A narrow molecular weight distribution is used to reduce cycle time in rapid multi-cavity closure and thin-wall container production, while the density level supplies the flexural modulus required for stackable packaging. The designation JV060U belongs to the Braskem high-density polyethylene product line. The suffix U is a producer-controlled designation; it does not replace the need to verify the latest technical datasheet for additive-package changes and lot-specific melt-flow values.
The grade is commonly controlled by melt flow rate, density, tensile yield strength, flexural modulus, and notched Izod impact. The values in the table below are derived from the producer’s published technical datasheet and are traceable to the listed test methods. They are not minimum values; they represent lot-average targets. When incoming inspection is performed, pellet sampling should follow ASTM D1898 or an equivalent internally validated sampling plan, because polyethylene exhibits lot-to-lot variation in additive dispersion and molecular weight tail fraction. Specification limits should be agreed with the producer as release windows, not as single-point values.
| Property | Typical range or nominal value | Test method |
|---|---|---|
| Melt flow rate | 5.5–6.5 g/10 min | ASTM D1238, ISO 1133-1 |
| Density | 0.958–0.962 g/cm³ | ASTM D1505, ISO 1183-1 |
| Tensile yield strength | 28–32 MPa | ASTM D638, ISO 527-2 |
| Flexural modulus, 1% secant | 1,300–1,500 MPa | ASTM D790, ISO 178 |
| Notched Izod impact, 23 °C | 4.0–5.0 kJ/m² | ASTM D256, ISO 180 |
| Vicat softening point, 10 N | 127–131 °C | ASTM D1525, ISO 306 |
| Deflection temperature under load, 0.455 MPa | 72–78 °C | ASTM D648, ISO 75-2 |
| Mould shrinkage, 48 h after moulding | 1.5–2.5% | ASTM D955, ISO 294-4 |
The melt flow rate of 6.0 g/10 min defines low-shear flow but does not alone predict high-shear cavity filling. In high-speed closure tools with valve-gated hot runners, shear heating can narrow the processing window even when the set barrel temperature is constant. Production-scale machines for this grade are typically configured with a general-purpose or low-compression screw having an L/D ratio of 20:1 to 24:1, a compression ratio of 2.5:1 to 3.0:1, and a non-return valve with a clean flow channel. Barrel-zone temperatures between 190 °C and 240 °C are common; the melt temperature measured at the nozzle should not exceed 250 °C for extended residence times because of oxidation risk. Injection pressures of 60–100 MPa and post-injection holding pressures of 40–70 MPa are used, but cavity pressure, not hydraulic pressure, should be the control parameter. Cavity-pressure transducers mounted behind an ejector pin or in a dummy pin should record a peak cavity pressure of 30–60 MPa and a gate freeze time that balances sink mark formation against cycle time.
When establishing a process window, cavity-pressure transducers should be installed in the last-to-fill cavity and at the gate area. The switchover point from velocity-controlled filling to pressure-controlled packing is set when the cavity is 95–99% filled by volume; moving switchover earlier increases sink mark depth, while later switchover raises the risk of flash and core shift. For JV060U in multicavity closure tools, a filling time of 0.3–0.8 s is typical for thin-wall caps with wall thickness between 0.6 mm and 1.2 mm. Shear rates at the gate can exceed 10,000 s⁻¹; the resulting temperature rise should be checked by nozzle and hot-runner sensors, not by barrel setpoint alone. Published shear-viscosity data for this specific grade are limited, so capillary rheometry at 190 °C is recommended when a precise process model is required.
The key difference between JV060U and high-molecular-weight HDPE used in blow moulding is the trade-off between processability and environmental stress crack resistance. Blow-moulding grades at 0.2–0.8 g/10 min and bimodal molecular weight distributions are selected because the high molecular weight tail contributes to slow crack growth resistance. JV060U at 6.0 g/10 min has substantially lower melt viscosity, which reduces filling pressure and permits thinner nominal walls, but the narrower molecular weight distribution lowers ESCR and long-term load-bearing capability. This does not disqualify the grade from packaging; it means the design must account for stress concentration at sharp radii, thread roots, and gate vestiges. In closure teardown tests, the difference is often observed as reduced strip-torque retention after exposure to emulsifiers or essential oils, in contrast to higher molecular weight injection grades with MFR below 2.0 g/10 min. Closure torque retention can be evaluated according to ASTM D2063 or closure-specific standards. Published data for this specific configuration is limited; end-use testing on the finished closure with the actual sealing liner and torque specification should be used to confirm suitability.
Within the Braskem HDPE injection-moulding portfolio, higher melt-flow grades above 15 g/10 min are used for very thin wall caps and closures, while grades below 2 g/10 min are selected for larger parts requiring higher ESCR. JV060U is positioned between these categories, with 6.0 g/10 min offering a balance between the ability to fill thin features and retention of mechanical properties. Compared with a high-flow grade, JV060U lowers the risk of flash and improves sustained load performance, at the expense of a shorter flow path. Compared with a low-flow grade, JV060U reduces cycle time and injection pressure, at the expense of ESCR and resistance to hot-runner sag.
Typical application areas include injection-moulded caps and closures for carbonated and non-carbonated beverages, dairy closures, thin-wall household containers, industrial pails, and overcaps for personal-care products. The grade is normally run in moulds with cavity counts between 32 and 72 for water-beverage closures and cycle times below 8 s depending on part mass and cooling configuration. Hot-runner valve gates are preferred when gate vestige must be controlled, while cold-runner edge gates are used in less demanding food containers. HDPE is not hygroscopic and does not require drying for absorbed moisture; however, condensation on cold pellets stored below the ambient dew point can create surface moisture, which is removable by hopper drying for 1–2 h at 70–80 °C with dehumidified air at a dew point not exceeding -18 °C. Long residence time at high temperature should be avoided to prevent molecular weight reduction, which shows up as an upward drift in melt flow rate.
Gate freeze time is determined by the crystallisation temperature, not solely by mould temperature. Differential scanning calorimetry according to ISO 11357-3 at a cooling rate of 10 °C/min typically gives a crystallisation peak between 110 °C and 120 °C for this density class. In moulding, the gate freezes when the melt at the gate drops below the solidification temperature; holding pressure can no longer compensate for in-cavity shrinkage after this point. Frozen-in molecular orientation along the flow path is therefore high in thin-wall parts with short fill times. This orientation contributes to anisotropic shrinkage, with in-plane mould shrinkage measured at 48 h after moulding according to ISO 294-4 typically remaining between 1.5% and 2.5%, with the lower end associated with higher packing pressure and slower cooling. Post-mould shrinkage in the first 24 h can add 0.1–0.3%, and dimensional checking should be delayed accordingly unless parts are conditioned under laboratory conditions at 23 °C ± 2 °C and 50% ± 5% RH.
Shrinkage anisotropy is the main cause of ovality in closure bodies. Flow-direction shrinkage is typically lower than cross-flow shrinkage because molecular orientation retards contraction along the flow direction. When the difference exceeds 0.3%, ovality and warpage become visible in unsupported thin-wall parts. Tools should therefore balance filling from a central gate or use multiple gates for rectangular containers. Core-cooling circuits should be sized to maintain a cooling-water temperature between 10 °C and 25 °C; turbulent flow with a Reynolds number above 10,000 is recommended in cooling channels to improve heat transfer and stabilise part surface temperature before ejection.
Environmental stress crack resistance is not covered by the melt flow rate and density values in the datasheet. For critical detergent or oil contact, the part should be tested under constant strain according to ASTM D1693 or notched constant tensile load according to ISO 16770. Higher density and higher melt flow generally reduce ESCR; therefore, parts made from JV060U should avoid sharp thread undercuts and high interference fits when the product will be exposed to aggressive liquids. The use of stress-relieving radii of at least 0.2 mm at thread roots and the selection of a lower interference fit can partially compensate.
For food-contact packaging, the base olefin polymer must satisfy FDA 21 CFR 177.1520 or be formulated to meet the overall migration and specific migration limits of Commission Regulation (EU) No 10/2011. A compliance statement from the producer is required; it applies to the resin as supplied and does not cover colourants, processing aids, or masterbatches added by the converter, nor does it cover migration testing on the finished article. For electrical and electronic applications, RoHS Directive 2011/65/EU restrictions are generally met by unreinforced polyolefins, but converter-added pigments and additives must also be assessed. Under REACH Regulation (EC) No 1907/2006, the grade must be accompanied by a safety data sheet and, where applicable, SVHC declarations. When the finished part is intended for potable-water contact, additional approvals such as NSF/ANSI 61 or national migration schemes may be required; these are outside the scope of the base-resin datasheet.
| Standard or regulation | Relevance | Required verification |
|---|---|---|
| FDA 21 CFR 177.1520 | Olefin polymers for food contact | Producer compliance letter; extractive limits on finished article |
| EU Regulation 10/2011 | Plastics in contact with food | Overall and specific migration testing on finished article |
| REACH Regulation (EC) No 1907/2006 | Registration, authorisation, and restriction of chemicals | SDS and SVHC declaration from producer |
| RoHS Directive 2011/65/EU | Heavy metal restrictions in electrical and electronic equipment | Material declaration for converter-added pigments and additives |
Incoming resin testing should include melt flow rate and density as a minimum. Melt flow rate is determined under controlled conditions after cleaning the plastometer barrel and die, because wall deposits can reduce the apparent value. Density gradient columns according to ASTM D1505 are preferred over displacement methods when small density variations must be detected. The allowable melt-flow drift due to moulding should be limited; if the MFR after processing increases by more than 20% relative to the virgin pellet, the process has excessive shear or residence time. This indicates a need to reduce barrel temperatures, screw speed, or back pressure. Control of these variables maintains the molecular weight distribution within the range assumed for mechanical and chemical resistance performance.
The grade is not recommended for pressure pipe or long-term hydrostatic design because it lacks the bimodal molecular weight architecture and slow crack growth resistance required for PE100 classification according to ISO 9080 and ISO 12162. It is also not formulated for continuous outdoor exposure without UV stabilisation; if outdoor storage or use is expected, a carbon-black masterbatch or a separately listed UV-stabilised HDPE grade should be selected, and weathering resistance should be evaluated according to ASTM D1435 or ISO 877. Contact with strong oxidising agents, aromatic hydrocarbons, and chlorinated solvents under stress should be avoided, particularly at elevated temperature, because these fluids accelerate environmental stress cracking in injection-moulded HDPE. Published data for this specific configuration is limited; therefore, chemical compatibility should be confirmed by full-part testing under the actual service fluid, stress state, and temperature. The processing conditions should always be verified against the current producer datasheet and lot certificate, because product specifications are revised without notification.