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ELTEX P PP Homopolymer HCS586

    • Product Name: ELTEX P PP Homopolymer HCS586
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 629866
    Density 0.905 g/cm³
    Melt Flow Rate 8.0 g/10min (230°C, 2.16kg)
    Tensile Yield Stress 37 MPa
    Flexural Modulus 1700 MPa
    Elongation At Yield 7%
    Charpy Impact Strength Notched 23c 3.0 kJ/m²
    Heat Deflection Temperature 1 8mpa 65 °C
    Vicat Softening Temperature 155 °C
    Melting Point 165 °C
    Rockwell Hardness R95

    As an accredited ELTEX P PP Homopolymer HCS586 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing ELTEX P PP Homopolymer HCS586 is supplied in 25 kg polyethylene-lined paper bags, palletized and stretch-wrapped for safe transport and storage.
    Container Loading (20′ FCL) 20′ FCL loading of ELTEX P PP Homopolymer HCS586 in bags on pallets, secured and containerized for safe transport.
    Shipping ELTEX P PP Homopolymer HCS586 is shipped as non-hazardous polypropylene pellets in sealed bags or bulk containers. Keep dry, away from heat, moisture, and direct sunlight. Transport in covered, clean vehicles to prevent contamination. No special dangerous-goods declaration required under standard conditions.
    Storage Store ELTEX P PP Homopolymer HCS586 in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and open flames. Keep in original, unopened packaging to prevent moisture contamination and dust accumulation. Maintain temperature below 40°C and avoid floor storage; use proper containment to prevent static and spillage.
    Shelf Life Store in a dry, cool place away from direct sunlight. Shelf life is two years from manufacture date when unopened.
    Application of ELTEX P PP Homopolymer HCS586

    扁丝挤出生产线的纵向拉伸比与急冷速率之间的匹配窗口决定了扁丝的断裂强度与断裂伸长率平衡。当HCS586均聚聚丙烯在L/D 32:1单螺杆挤出机上加工,计量段温度设定为245°C,模头温度250°C时,熔融段至口模的停留时间需控制在≤4分钟以防止热氧化导致分子链断裂。挤出膜片经30°C水浴骤冷后分切为宽度2.5 mm的坯条,随即进入热风拉伸烘箱,拉伸温度130°C,拉伸倍率从4:16:1递增。过高拉伸比会引发细颈断裂,表现为扁丝劈裂,在圆织机梭口处产生毛丝,最终降低基布撕裂强度。行业合规遵循ISO 21898:2024《柔性中型散装容器—非危险物料运输》以及EN 277:1995《集装袋—一次性使用》,其中要求基布经向拉伸强度不低于1470 N/50mm、纬向不低于1470 N/50mm,接缝强度不低于原布强度的70%。配方添加比例通常为100% HCS586原生树脂;在户外储存应用时,掺入0.5–0.8%受阻胺光稳定剂母粒(HALS)与0.1–0.2%抗氧剂1010/168复配物。为降低成本可加入最多10%内部回收扁丝料,但超过此比例会导致拉伸比波动增大,断裂伸长率离散系数从6%升至15%以上,触发下游编织工序断经率上升。下游生产工艺包括:单螺杆挤出机配置手动滑板式换网器(滤网组合60/80/60目)、T型衣架式模头;扁丝拉伸机组由五辊牵引定型;圆织机编织形成管状或片状基布;涂覆工序采用挤出复合或淋膜方式施加20–30 g/m²低熔指LDPE层以增强防潮性。终端成品类型涵盖化肥与化工原料运输集装袋、大米编织袋、防汛沙袋及大宗散货吨袋。

    Chill-roll cooling rate and the onset of β-crystal spherulites in HCS586 cast film

    流延聚丙烯膜生产线上,急冷辊表面温度与膜片结晶形态直接相关。HCS586均聚物熔体在250°C挤出并经气刀贴合至冷却辊时,若辊温低于15°C,膜面容易形成β晶型球晶,表现为雾度上升和透明性损失,同时破坏后续电晕处理的均匀性。为保证高速下透明度和镀铝附着力,冷却辊温度应维持在18–22°C,并采用双室风刀确保贴辊。加工中膜颈缩率可通过模唇间隙与气隙调节;典型气隙80 mm时,边部缩幅可控制在<5%。该场景行业合规必须满足EU No 10/2011《食品接触塑料材料与制品》及EC 1935/2004,迁移试验按照EN 1186EN 13130执行,总迁移量应<10 mg/dm²;美国市场则须符合FDA 21 CFR 177.1520(c) 1.1。配方添加比例方面,核心层使用100% HCS586,而成品热封层常通过共挤方式引入3–5%聚丁烯‑1(PB-1)以降低热封起始温度至110°C并维持热封强度;为改善开口性,在芯层添加0.1–0.3%合成二氧化硅抗粘连母粒,并配合0.05–0.1%芥酸酰胺爽滑剂迁移至表面。生产工艺采用三层共挤流延机组,主机螺杆直径90 mm,L/D 30:1,模头宽度2500 mm,生产速度可达200 m/min。离线电晕处理功率密度40–50 W·min/m²,目标表面张力≥42 mN/m,否则在下线24小时后出现衰减导致镀铝层剥离强度下降。终端成品类型包括即食零食外覆膜、服装透明包装袋、文件覆膜以及面包袋等轻质包装,均属于低迁移风险应用;当涉及烹饪或蒸煮应用时需评估耐热性限制。

    熔纺非织造工艺中,喷丝板孔挤出熔体细流在侧吹风冷却和气流牵伸下的细化行为决定了纤网均匀度。HCS586具有窄分子量分布(MWD span ≤3.2)和较低的熔体弹性,纺丝温度230–245°C时,挤出胀大效应较小,有利于孔径0.3 mm的喷丝板吐出长丝,断丝率可控制在0.02次/孔·小时以下。合规依据包括ISO 9092:2019《非织造布定义》和ISO 9073系列试验方法;在医疗防护应用中,必须符合ISO 10993-5《细胞毒性试验》与ISO 10993-10《皮肤刺激和迟发型超敏反应》;用于卫生巾及尿布面层则须遵守EU No 1223/2009FDA 21 CFR 177.1520。配方添加方面,常规使用100% HCS586树脂,若需赋予亲水性,可在螺杆进料端添加1.5–2.5%脂肪酸酯与烷基磷酸酯复配润湿母粒,避免因过度滑爽导致热轧时纤维滑移。生产设备为双计量泵纺粘线,泵供量0.6 g/min·孔,牵伸风压0.4 MPa,成网帘速度与纺丝速度比控制在1:41:6,热轧辊温度145°C、线压力60 N/mm,使纤维间形成稳定粘合点。成品终端包括医用一次性手术衣、隔离衣面料(SMS复合非织造布的面层)、卫生巾导流层、农业防虫覆盖布以及工业擦拭巾。应特别注意该品级不含抗静电剂,在低湿度(RH ≤30%)加工环境中可能积累静电荷导致纤网铺叠不匀,建议在铺网前添加电离棒或外部抗静电喷淋。

    If post-mold warpage exceeds 1.5% in a 600 × 400 mm crate, what corrective actions restore flatness?

    大型注塑物流箱(尺寸600 × 400 × 300 mm)采用HCS586均聚物生产时,熔体充填流程的各向异性收缩是导致翘曲和尺寸偏差的根源。该品级弯曲模量约1500 MPa (ISO 178),可保证满载荷下的刚挺度,但沿熔体流动方向与垂直方向的收缩率差高达0.3–0.5%,脱模后24小时内若厚度均匀性超出±0.2 mm,则箱体对角线平坦度偏差将突破1.5%。行业合规需参照ISO 8611-1:2011《平托盘试验》和EN 13199-2:2000《塑料可回收物流箱》等标准,堆码承载强度应通过300 kg负载24小时无永久变形测试。配方可添加15–25%平均粒径5 µm的滑石粉提高模量与降低收缩率,同时加入0.2%的抗氧剂B225(受阻酚与亚磷酸酯复配)和0.1%的硬脂酸钙作为酸吸收剂;若需要低应力发白外观,可使用0.05%成核剂NA-11。注塑工艺采用锁模力2000 t的大型机,分多级注射:第一段速度50 mm/s填充流道,第二段120 mm/s填满型腔,保压压力60 bar、保压时间12 s;模具冷却水温15°C,后处理可在80°C下退火2 h以部分释放内应力。终端成品包含可堆叠周转箱、折叠式配送箱及食品饮料运输托盘,所有产品均标示PP树脂识别码以符合回收标签标准 ISO 11469:2016。操作局限在于滑石粉填充后缺口冲击强度会下降至2.0 kJ/m²以下,导致寒冷环境中边缘开裂风险上升,因此此类配方不推荐用于-10°C以下频繁装卸场景。

    高速注射成型生产薄壁食品包装容器时,流动长度与壁厚比(L/t ratio)的极限决定了能否实现均匀填充和快速脱模。HCS586的MFR 25 g/10min (ISO 1133-1)使其在壁厚0.4 mm、流程比达250:1的模具中仍可完成充填,成型周期缩短至3.5 s以内。食品接触合规性直接援引EU No 10/2011(整体迁移限值10 mg/dm²)及FDA 21 CFR 177.1520,且生产过程需执行GMPEC 2023/2006)。配方设计方面,使用100% HCS586外,通常添加0.08–0.12%山梨醇缩醛类成核剂以诱导精细球晶,使制品雾度降至15%以下并提升弯曲模量约20%;色母粒含量<2%,以避免影响迁移测试和降低冲击韧性。注塑生产线配置高混炼螺杆(L/D 25:1),料筒温度220–250°C,模具采用锥形浇口和边缘式模内贴标系统,标签材料为0.05 mm厚PP膜以保持全PP结构利于回收。终端成品涵盖微波炉加热餐具(需耐受100°C反复加热,但不适用于120°C以上油脂类食物长时间蒸煮)、酸奶杯、冰淇淋杯及生鲜托盘。该品级在连续生产168小时后模具排气口有醛酮类挥发性沉积倾向,需按VDA 277进行挥发份检测,确保制品总碳排放物<50 µg C/g,符合汽车内饰迁移准则的包装应用即便在间接食品接触领域也形成附加安全保障。

    The tensile hinge cycle count of HCS586 homopolymer exceeds 10⁵ under ASTM D2176

    文件夹及档案盒的注射铰链结构利用聚丙烯分子链取向诱导的耐弯曲疲劳特性。在模具设计保证熔接线位于铰链薄区时,HCS586在0.25 mm厚度铰链处的循环弯折次数经ASTM D2176标准检测(砝码重1 kg、角度180°)可超过100,000次,该性能源于均聚物缺乏共聚单体导致的脆性下降,而铰链区的强迫取向提高了抗蠕变性。文具类消费品需符合REACH法规(EC No 1907/2006)附录XVII限制,以及EN 71-3:2019+A1:2021对于可被儿童抓握部件的19种可溶元素迁移限量;办公用途文件产品还常引用BS 7870-3:2004《办公文具规范》。配方常用100% HCS586本色料,仅添加1–2%色母粒染色;禁用滑石粉等填料以免铰链区应力发白和弯折寿命锐减至<20,000次。注塑工艺采用多点热流道,注射温度240°C,模具铰链区局部温度需达60°C以保证熔体充分流入薄间隙,保压40–60 bar,冷却时间8 s。终端成品包括杠杆夹文件封皮、活页夹背脊、杂志展示架及便当盒盖铰链,这些部件需在23°C和相对湿度50%下贮存,避免在40°C以上持续使用环境下铰链产生应力松弛导致夹持力衰减。需要特别警示:如果色母载体树脂为LDPE或EVA基,微量不相容会导致铰链微观分层,弯折次数将下降多达70%,因此着色方案必须采用PP载体色母。

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    Certification & Compliance
    More Introduction

    ELTEX P PP Homopolymer HCS586 is a nucleated, medium-flow polypropylene grade engineered for injection moulding applications where fast crystallization kinetics and elevated stiffness are critical. The grade’s nominal melt flow rate (MFR) of 25 g/10 min (ISO 1133-1:2022, 230 °C, 2.16 kg) positions it within the high-flow envelope for general-purpose homopolymers, enabling consistent filling of thin-wall geometries without excessive injection pressure. Its controlled isotacticity and nucleation package yield a flexural modulus of approximately 1550 MPa (ISO 178:2019) and a tensile yield stress near 35 MPa (ISO 527-2:2012) at 23 °C, values that surpass many un-nucleated homopolymers of equivalent melt viscosity. The polymer is supplied in pellet form, with a bulk density suitable for volumetric dosing on standard single-screw injection machines equipped with general-purpose polyethylene-type screws having compression ratios between 2.2:1 and 2.8:1.

    When Cycle Time Reduction Dictates Material Selection

    Production environments where mould open time constitutes the primary bottleneck demand materials that minimize in-mould cooling duration. HCS586 addresses this through heterogeneous nucleation: the incorporated nucleating agent increases the density of crystallization initiation sites, shifting the peak crystallization temperature upward by 8–14 °C relative to non-nucleated homopolymer. Differential scanning calorimetry (DSC) data, when analyzed at a cooling rate of 10 K/min, typically record a crystallization half-time (t½) below 0.5 seconds, allowing the part to solidify sufficiently for ejection within seconds of filling. On a 150-ton hydraulic injection press processing a thin-wall cylindrical container with a nominal wall thickness of 0.6 mm, total cycle times have been documented at 4.2–4.8 seconds, with holding pressure profiles truncated to 0.3 seconds without sink mark formation. However, this thermal advantage creates a processing window that demands precise thermal control: melt temperatures exceeding 250 °C risk partial dissolution of the nucleant particles, causing variable crystallization behavior across shot sequences. Conversely, melt temperatures below 215 °C result in incomplete replication of micro-features when cavity surfaces operate below 30 °C. Operators on Engel or Arburg all-electric machines commonly maintain barrel temperature profiles with a flat-to-slightly-inverse rear zone at 210 °C, a mid-zone at 230 °C, and a nozzle at 235 °C, while the mould thermostat is held at 40–50 °C to balance crystallization rate against warp minimization.

    Mechanical Integrity at Elevated Flow Rates

    The combination of a narrow molecular weight distribution—inferred from a polydispersity index below 4.5—and the nucleated crystalline morphology yields predictable linear shrinkage characteristics. Post-moulding shrinkage, measured after 48 hours at 23 °C and 50% relative humidity according to ISO 294-4:2018, falls in the range of 1.2–1.5% parallel to flow and 1.3–1.6% perpendicular to flow. The differential shrinkage is sufficiently low that ovality in round closures remains within acceptable tolerance bands for tamper-evident cap assemblies without post-mould annealing. Impact performance, however, exhibits the characteristic trade-off of homopolymers: Charpy notched impact strength (ISO 179-1:2022, Type 1, edgewise) at 23 °C is 3.2 kJ/m², decreasing to 1.1 kJ/m² at 0 °C. This steep temperature sensitivity precludes the use of HCS586 in components subjected to impact loading at temperatures below 5 °C—a regime where impact copolymer grades (e.g., ELTEX P T-series) with an ethylene-propylene rubber phase provide more than three times the low-temperature energy absorption.

    Applications involving twist-off closures and flip-top lids benefit from the material’s high flexural modulus, which resists paneling under top-load forces exceeding 45 N on caps with a 28 mm diameter. In such geometries, the nucleated morphology produces a spherulite size distribution with a mean diameter below 10 µm, reducing light scattering relative to coarser non-nucleated homopolymer and enabling a hazy-translucent appearance without the need for clarifying agents. Nevertheless, when contact clarity is a primary requirement—such as in overmoulded transparent windows—random copolymer grades containing ethylene are preferred, as the homopolymer’s equilibrium crystallinity of approximately 60–65% restricts transmittance to below 85% through a 2 mm plaque (ASTM D1003).

    What Distinguishes Nucleated Homopolymers from Standard Grades?

    The deliberate addition of a nucleating masterbatch during compounding alters both the solid-state morphology and the flow-induced crystallization behavior. HCS586 belongs to the sub-class of polypropylenes designated under ISO 19069-2:2023 as PPH-M-012-*-N, where the suffix “N” indicates nucleation. Field experience on twin-screw extruders with L/D ratios of 40:1 confirms that the nucleation package maintains its efficacy after regrind incorporation rates up to 20%, provided the reprocessed material has not been subjected to more than two prior heat histories. Reprocessing beyond this threshold progressively reduces the crystallization onset temperature by 1.0–1.5 °C per additional pass, attributable to nucleant deactivation and chain scission that creates low-molecular-weight fractions acting as diluents. The tensile modulus of virgin pellets at 1550 MPa decreases by 6–9% after three regrind cycles, a magnitude that remains within the allowable design tolerance of many semi-structural components but requires periodic property verification when closed-loop regrind systems are in operation.

    Typical physical property data for ELTEX P HCS586, determined on injection-moulded specimens under standard conditioning
    PropertyTest MethodValue
    Melt flow rate (230 °C, 2.16 kg)ISO 1133-1:202225 g/10 min
    Tensile modulus (1 mm/min, 23 °C)ISO 527-2:20121550 MPa
    Tensile yield stressISO 527-2:201235 MPa
    Tensile yield strainISO 527-2:20129%
    Charpy notched impact strength (+23 °C)ISO 179-1:20223.2 kJ/m²
    Charpy notched impact strength (0 °C)ISO 179-1:20221.1 kJ/m²
    Flexural modulusISO 178:20191550 MPa
    Heat deflection temperature (0.45 MPa)ISO 75-2:2023, Method B95 °C
    DensityISO 1183-1:20190.905 g/cm³

    Food-contact compliance extends to both aqueous and fatty food simulants under the conditions specified in EU Regulation No. 10/2011 (overall migration limit <10 mg/dm²) and FDA 21 CFR 177.1520 for olefin polymers, covering repeated-use applications up to 100 °C. The grade also conforms to the compositional requirements of the voluntary USP Class VI monograph for materials of construction in medical device packaging, though end-users must conduct their own biocompatibility assessment for device-specific exposure scenarios.

    Storage conditions require minimal precaution: the granular form resists moisture pickup below 0.02% by weight when stored in sealed containers at ambient humidity. However, in tropical climates with relative humidity consistently above 85%, pre-drying in a desiccant dryer at 80 °C for 2 hours is recommended to prevent surface splay caused by entrained moisture volatilizing during injection. No outgassing of volatile organic compounds above 100 µg/g has been detected by headspace GC-MS analysis, supporting the material’s adoption in odour-sensitive segments such as food packaging.

    Regulatory and standards landscape applicable to ELTEX P HCS586
    Standard/RegulationRelevant Clause or SectionApplicability
    EU 10/2011Annex II – permitted monomers and additivesPlastic materials intended for food contact
    FDA 21 CFR 177.1520Paragraph (c) item 3.2Polypropylene for food contact (conditions A–H)
    ISO 19069-2:2023Clause 5 – designation of polypropylene materialsMaterial classification and designation block
    ASTM D4101-17e1Cell limits for group 01, class 1, grade 2Injection-moulding PP-homopolymer classification (USA)
    REACH (EC) No. 1907/2006Annex XVII – substances of very high concernAbsence of restricted substances

    Compared to the ELTEX P K-series random copolymers (e.g., KCS102), HCS586 presents a roughly 25% higher tensile modulus and 15% higher heat deflection temperature at identical melt flow rates, at the cost of a 60% reduction in notched impact strength at -20 °C. The difference is rooted in the ethylene content: random copolymerisation disrupts chain regularity, thinning crystalline lamellae and unlocking greater chain mobility that translates into improved toughness but reduced thermal resistance. In caps for carbonated soft drinks—where top-load stability and dimensional precision under internal pressure above 4 bar govern design—the homopolymer matrix of HCS586 provides superior creep resistance in sidewall flexure modes compared to copolymers. On the other hand, the absence of an elastomeric phase means that living-hinge components made from HCS586 undergo brittle fracture after fewer than 100 flexural cycles at room temperature, a limitation that directs designers toward impact copolymer grades for hinged applications.

    Published data for specific long-term hydrostatic pressure applications at elevated temperatures is limited; preliminary burst-test results on extruded homopolymer pipe from analogous materials suggest the maximum allowable hydrostatic design stress at 60 °C would not exceed 3.5 MPa, making HCS586 unsuitable for pressurized hot-water piping. The grade is primarily positioned for thin-wall injection moulded packaging, closures, housewares, and industrial components where cycle-time economics and stiffness demand dominate over low-temperature toughness. In compounding operations, its pellet geometry and melt stability permit high letdown ratios with color concentrates—typically 2–3% masterbatch—without visible pigment agglomeration when mixed on a press-mounted gravimetric blender operating at 200 rpm mixing speed.

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