| HS Code | 502317 |
| Productname | Polypropylene Thin-wall Injection Grade PP K1870 |
| Polymertype | Polypropylene |
| Gradetype | Thin-wall injection molding grade |
| Polymerstructure | Impact copolymer polypropylene |
| Processingmethod | Injection molding |
| Typicalapplication | Thin-wall packaging and disposable containers |
| Form | Pellets |
| Color | Natural |
| Density | 0.90-0.91 g/cm3 |
| Meltflowrate | 18 g/10 min at 230 C/2.16 kg |
| Tensilestrengthatyield | 24-26 MPa |
| Elongationatbreak | 200-500% |
| Flexuralmodulus | 1000-1200 MPa |
| Notchedizodimpactstrength | 50-80 J/m at 23 C |
| Heatdeflectiontemperature | 95-105 C |
| Vicatsofteningtemperature | 145-155 C |
| Moldingshrinkage | 1.2-1.8% |
As an accredited Polypropylene Thin-wall Injection Grade PP K1870 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Polypropylene Thin-wall Injection Grade PP K1870 is packaged in 25 kg moisture-proof woven bags, 40 bags per pallet. |
| Container Loading (20′ FCL) | 20′ FCL loaded with 25kg bags of Polypropylene Thin-wall Injection Grade PP K1870, palletized and shrink-wrapped, approx. 20 MT net. |
| Shipping | Polypropylene Thin-wall Injection Grade PP K1870 is shipped as non-hazardous, odorless thermoplastic pellets in 25-kg moisture-barrier bags or jumbo bags on pallets. Store dry and ventilated; avoid moisture, UV/direct sunlight, contamination, and ignition sources. Transport at ambient temperature in covered trucks/containers. Follow SDS. |
| Storage | Store Polypropylene Thin-wall Injection Grade PP K1870 in original, sealed packaging on pallets, off the floor, in a cool, dry, well-ventilated warehouse. Keep away from direct sunlight, heat, flames, sparks, and strong oxidizing agents. Prevent moisture, dust, and contamination; use first-in, first-out rotation. Avoid punctures or physical damage to bags and maintain clear labeling and good housekeeping. |
| Shelf Life | Polypropylene Thin-wall Injection Grade PP K1870 typically has a 24-month shelf life when stored dry, cool, ventilated, and away from direct sunlight in unopened original packaging. |
On high-speed thin-wall lines producing 150–200 mm diameter dairy cups and round deli containers, K1870 is positioned in the 60–75 g/10 min MFR band under ISO 1133-1:2022 at 230°C and 2.16 kg, and is typically processed at melt temperatures of 230–250°C with mold temperatures held at 15–30°C. Accumulator-assisted hydraulic injection machines in the 250–350 t clamp class with 16–32-cavity valve-gated hot runners are common; screw L/D of 20:1–22:1 and compression ratio of 2.0–2.5:1 deliver the shot weight with minimized residence time. The controlling parameter is flow-length-to-wall-thickness ratio: for sidewall thicknesses of 0.45–0.60 mm and cup heights of 80–120 mm, the ratio exceeds 200:1. Injection velocities above 150 mm/s and fill times below 0.30 s are required to prevent the melt front from freezing at the rim before cavity filling is complete. Pre-drying is not normally required below 60% RH; above that threshold, 2 h at 80°C suppresses splay. Food-contact documentation is required under FDA 21 CFR 177.1520, EU No 10/2011 with overall migration below 10 mg/dm², and GB 4806.7-2016. The usual formulation is 97–99 wt% K1870 with 1–3 wt% white masterbatch containing 60% TiO₂ in PP carrier; slip/antiblock masterbatch at 0.3–0.8 wt% is added only when automated filling lines impose a denesting-force limit, because excess slip can reduce sidewall ink adhesion after printing. Cycle times of 5–8 s are obtained with cooling times of 2–4 s and chilled water at 8–12°C. Terminal product types include 4–8 oz dairy cups, 250–500 ml delicatessen containers, and matching nested lids.
Sidewall uniformity in cold-beverage cups molded from K1870 is governed less by average melt temperature than by the pressure drop across a tall core and the resulting melt-front velocity gradient. A 300 ml cup with sidewall thickness 0.40–0.55 mm and height-to-diameter ratio above 1.5:1 can generate a filling pressure differential between gate and rim of 30–50 MPa; this differential produces hoop-direction orientation variations that appear as uneven shrinkage and poor stacking contact after ejection. The downstream process therefore uses servo-electric or hybrid injection machines with injection velocities of 150–220 mm/s, holding pressure of 40–65 MPa, and mold temperature held at 10–25°C to freeze the sidewall before core deflection becomes excessive. In multi-cavity production, flow balance is maintained with hot-runner valve gates and individually controlled drop temperatures; a gate vestige below 0.15 mm is targeted for rim stacking. Compliance for beverage contact is documented under FDA 21 CFR 177.1520 and EU No 10/2011, with additional migration testing under 10 days at 40°C for cold-fill applications where required by EU simulant conditions. When contact clarity is not specified, the formulation is 100 wt% K1870 run neat; where low-haze sidewalls are needed, 1.5–2.5 wt% of a sorbitol-based clarifier masterbatch is added, equivalent to 0.1–0.3 wt% active clarifier. Cold-impact performance at 4°C is not a primary data-sheet value for high-flow PP; converters distributing cups through refrigerated channels must verify finished-article Charpy impact per ISO 179-1:2010, because thin-wall orientation and storage temperature shift the ductile-to-brittle transition compared with 4 mm laboratory specimens. Terminal product types include 250–500 ml cold-beverage cups, 500 ml stadium cups, and stackable cold-drink tumblers.
Converters of non-sterile diagnostic labware specify K1870 primarily for consistent melt delivery on all-electric injection machines in ISO Class 8 cleanrooms, where process aerosols and external lubricants must be minimized. The processing window is narrower than in food packaging because degradation-related extractables, not only visual defects, determine lot acceptance. Melt temperature is held at 220–240°C, back pressure at 0.5–1.0 MPa, and mold temperature at 20–35°C; wall thicknesses of 1.0–1.2 mm yield cycle times of 8–12 s on all-electric machines with closed-loop injection speed. The cleanroom molding format typically runs 100 wt% K1870 without slip, nucleator, or external mold release; if demolding requires release, it is limited to a volatile, silicone-free external agent that is validated as a residue risk. Compliance is not automatically satisfied by the PP data sheet: K1870 is generally supplied with food-contact documentation under FDA 21 CFR 177.1520 and EU No 10/2011, but diagnostic labware requires final-article biological evaluation under ISO 10993-5:2009 and ISO 10993-10:2010, and the converter must maintain ISO 13485:2016 device-component QMS controls. The terminal product range includes 90–120 ml urinalysis cups, specimen collection containers, and non-sterile transport vials.
| Standard | Scope | Data Required from Converter | K1870-Linked Limitation |
|---|---|---|---|
| FDA 21 CFR 177.1520 | Olefin polymer food-contact compliance | Supplier food-contact statement and migration data | Does not cover clinical contact or device biocompatibility |
| EU No 10/2011 | Overall migration below 10 mg/dm² and specific migration | Laboratory migration testing under OM1/OM2 simulant conditions | Food simulant data do not replace clinical extraction evaluation |
| ISO 10993-5:2009 | Cytotoxicity | Extract testing on finished article | Not supplied by standard PP resin documentation |
| ISO 10993-10:2010 | Skin sensitization and irritation | Extract testing with polar/non-polar vehicles | Required where skin contact is prolonged or repeated |
| ISO 13485:2016 | QMS for medical device components | Cleanroom controls, batch traceability, change management | Converter QMS requirement; resin lot traceability must be maintained |
Microwaveable ready-meal trays molded from K1870 create a conflict between fast solidification and sealing-flange flatness that is rarely resolved by cavity pressure alone. The tray base and sidewall are thinned to 0.65–0.90 mm to reduce part mass, but the heat-seal flange is kept at 1.2–1.5 mm to withstand lidding-film sealing pressure; this differential thickness induces differential shrinkage, and warpage above 0.5 mm across a 170 mm side can cause seal failures on rotary vacuum lidding equipment. Melt temperatures of 240–260°C and mold temperatures of 35–50°C are used to reduce frozen-layer growth, while injection velocity is profiled from 80–150 mm/s to avoid jetting from the hot tip. Holding pressure of 50–70 MPa with a gate-seal time of 0.8–1.2 s is applied to pack the flange; sequential valve gating is preferred in two-cavity tools to balance filling of the long-flow rear wall and the flange. The formulation uses 96–99 wt% K1870, 0.5–1.5 wt% nucleating masterbatch to reduce post-mold shrinkage, and 0.5–2 wt% color concentrate; additive packages must not generate off-taste or odor above sensory thresholds after microwave reheating. Compliance is documented under FDA 21 CFR 177.1520 and EU No 10/2011 for repeated microwave reheating, but the trays are not suitable for conventional oven or grill use. Dimensional stability is verified on finished trays per ISO 294-4:2018; published data for K1870 with specific nucleating loadings in microwave tray geometry is limited, so converter-run shrinkage and heat-seal trials are required. Terminal product types include 500–1000 ml microwave-ready meal trays, compartment trays, and sealed ready-meal containers.
At 1.5 mm wall thickness, K1870 diverges from severe thin-wall food packaging and is processed with lower injection velocities of 50–100 mm/s and melt temperatures of 220–240°C. The high-flow profile permits fast filling of long drawer fronts without heavy packing pressure, but mold temperature is held at 20–40°C to limit sink marks opposite ribs. Compliance for non-food housewares is normally limited to REACH and RoHS 2011/65/EU; food-contact certification under FDA 21 CFR 177.1520 is not required unless the article is marketed for kitchen storage. The formulation is 98–100 wt% K1870 with 0–2 wt% PP-based color masterbatch; antistatic additives are not recommended for high-gloss surfaces because their migration can create visible bloom. The downstream process uses conventional single-face or stack molds with ribs at 60–80% of wall thickness to avoid sink marks. Terminal product types include stackable drawer organizers, small household bins, and translucent storage boxes.
Drainage holes in the base of horticultural pots molded from K1870 generate multiple weld lines that become primary crack initiation sites when filled pots are lifted by the rim. The weld-line condition is worsened by high-flow orientation: melt fronts traveling around hole pins cool and align before knitting, producing local strength below that of the adjacent oriented sidewall. For pots with base thickness 0.8–1.0 mm and drainage hole diameter 6–10 mm, mold temperature is held at 20–35°C; the practical mitigation is not higher holding pressure alone but relocation of gates so that weld lines are moved into high-curvature zones away from the rim. A hot-runner system with 4–6 valve gates on the base is used for 150–200 mm diameter pots, with injection velocity profiled from 120–150 mm/s during cavity filling to 40–60 mm/s as the melt passes hole pins; this reduces jetting at the pins while retaining fast cavity fill. Compliance is governed by REACH and, where decorated planters are marketed for child contact, heavy metal migration testing per EN 71-3:2019 on the finished article. The formulation for outdoor exposure includes 1–3 wt% of a HALS-based UV masterbatch and 0.5–2 wt% color concentrate in 96–98 wt% K1870; calcium carbonate filler is generally avoided in thin-wall drainage-hole configurations because increased melt viscosity reduces weld-line strength, and published data specific to K1870 with CaCO₃ in horticultural geometry is limited. Terminal product types include nursery pots, propagation trays with multiple drainage ports, and decorative balcony planters; converter-run impact testing per ISO 179-1:2010 on base sections is required before full tooling commitment.
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Polypropylene thin-wall injection grade PP K1870 is a controlled-rheology polypropylene supplied as pellets, positioned for high-speed injection molding of containers, cups, lids, and light packaging with nominal wall thickness below 1.0 mm. Under ISO 1133-1:2022, the melt mass-flow rate is typically 70 g/10 min at 230 °C and 2.16 kg, placing the grade above conventional injection-molding homopolymer PP but below some ultra-high-flow packaging grades. Density measured to ISO 1183-1 is normally 0.90 g/cm³. The difference from lower-flow PP grades is primarily rheological: the high MFR is achieved by controlled chain scission, which narrows the molecular-weight distribution and reduces pressure drop across thin-wall cavities; this simultaneously lowers the melt strength needed for extrusion blow molding or blown film. Published data for this specific K1870 configuration remain limited to the manufacturer’s technical datasheet and lot certificate, so typical values in this text are class-level envelope figures for high-flow thin-wall PP homopolymers and should be superseded by documentation supplied with the lot.
The primary specification parameters are melt mass-flow rate, density, tensile yield stress, notched impact resistance, Vicat softening temperature, and mold shrinkage. Each lot is normally controlled by the manufacturer’s certificate of analysis, not solely by a generic datasheet. Because the grade is peroxide-visbroken, the molecular weight distribution is narrower than that of a reactor-grade PP of the same MFR. Narrow distribution reduces die swell and improves surface gloss in thin sections, but it also depresses the zero-shear viscosity plateau and reduces room-temperature impact. Xylene-soluble content at 25 °C is typically below 4% for this class; this supports stiffness and migration resistance but limits low-temperature seal strength. Ash content is normally controlled below 0.03% unless nucleation or slip additives are specified in the formulation.
| Property | Test method | PP K1870 class envelope | Conventional 12 g/10 min reference |
|---|---|---|---|
| Melt mass-flow rate, 230 °C/2.16 kg | ISO 1133-1:2022 | 70 g/10 min | 12 g/10 min |
| Density | ISO 1183-1 | 0.90 g/cm³ | 0.90 g/cm³ |
| Tensile stress at yield | ISO 527-2 | 36 MPa | 36 MPa |
| Tensile modulus | ISO 527-2 | 1600 MPa | 1700 MPa |
| Notched Izod at 23 °C | ISO 180/A | 2.5 kJ/m² | 3.5 kJ/m² |
| Vicat softening temperature A50 | ISO 306 | 155 °C | 155 °C |
| Heat deflection temperature, 0.45 MPa | ISO 75-2/B | 95 °C | 95 °C |
| Mold shrinkage | ISO 294-4 | 1.2% | 1.4% |
The limiting factor is not barrel temperature alone but the combined effect of solidification layer growth and melt-pressure transmission. At wall thickness of 0.5 mm, the molten core must remain open long enough for cavity pressure to reach the end of flow. With an MFR near 70 g/10 min, injection speed is normally set between 200 mm/s and 350 mm/s. Below this window, short shots appear at the rim; above it, shear heating can generate local temperature overshoot and gate blush. The pack/hold window is narrower than for lower-MFR grades because the viscosity is low enough to permit rapid gate freeze after screw transition. Switchover set too early by 0.2 s can produce dimensional scatter in lids with a sealing groove depth of 0.35 mm.
Melt temperature is typically maintained between 230 °C and 260 °C. Mold temperature is held between 15 °C and 40 °C for fast cycles. The processing window narrows to approximately ±5 °C at wall thickness below 0.6 mm; higher melt temperature induces gloss differences and yellowing, while lower melt temperature causes unstable fill and warpage. Screws with L/D ratio 20:1 to 22:1 and compression ratio 2.0:1 to 2.5:1 are preferred. High-shear screw designs with excessive compression can cause melt-temperature inhomogeneity and batch-to-batch drift.
Cooling time is a bottleneck. At 0.6 mm wall thickness, cooling time can fall to 2–3 s, but ejection requires the core surface near 80 °C. Differential shrinkage between flow and transverse directions produces warpage; this is controlled by maintaining mold temperature within ±3 °C and by balancing gate diameters. Viscous dissipation can raise local melt temperature by 10–15 °C; barrel set point alone is not a reliable indicator of actual melt temperature at the hot tip.
Weld-line strength is often the limiting mechanical property in thin-wall containers because the gate design creates multiple flow fronts. For a high-flow homopolymer PP with MFR 70 g/10 min, weld-line tensile strength can be 20–30% lower than the bulk tensile strength; this is typically assessed by molding a double-gated plaque and testing to ISO 527-2. Products requiring top-load strength should avoid placing weld lines at the rim sealing surface.
For thin-wall food packaging, PP K1870 is specified in multi-cavity hot-runner tools for dairy cups, delicatessen containers, and disposable drink cups. These tools often run with 24 to 64 cavities and clamp forces between 1,800 kN and 4,000 kN; valve-gated hot runners minimize gate vestige. The grade’s principal advantage is the ability to fill wall stocks as low as 0.4 mm without excessive injection pressure, provided that the tool is stiff enough to avoid flash at cavity pressures above 50 MPa.
In food-contact applications, candidate compliance is assessed under FDA 21 CFR 177.1520 and EU Regulation (EU) No 10/2011 as amended. The overall migration limit for general food contact under the EU regulation is 10 mg/dm². Specific migration of primary aromatic amines and bisphenol A is not expected from polypropylene homopolymer, but the finished article must be tested under the intended food simulants. For sensory-sensitive dairy products, taint and odor evaluation is commonly carried out to ISO 13302:2003. The grade should not be used for hot-fill above 90 °C unless the part is redesigned or the material is independently validated for creep and head-space pressure.
The product differs from propylene-ethylene random copolymers primarily in optical and thermal performance. Random copolymers used for thin-wall cups may show haze below 15% at 1 mm, whereas a high-flow homopolymer of the same melt-flow class can exceed 25% haze. The homopolymer generally retains a higher tensile modulus and Vicat softening temperature under ISO 306, but it sacrifices low-temperature impact. Compared with heterophasic impact copolymers, PP K1870-class materials show lower notched impact at sub-zero temperatures but higher stiffness and faster solidification; this makes them suitable for thin-wall packaging that requires dimensional stability rather than freezer-impact ductility. When the product is evaluated against ultra-high-flow PP with MFR 100 g/10 min or higher, the difference is not simply melt flow; ultra-high-flow grades can reduce injection pressure further but may exhibit more visible flow marks and lower weld-line strength, so the 70 g/10 min class is often selected as a compromise between processability and mechanical integrity.
Table 2 summarizes the regulatory and mechanical test matrix used to benchmark the grade in thin-wall packaging projects.
| Topic | Standard or specification | Test condition or limit |
|---|---|---|
| Melt mass-flow rate | ISO 1133-1:2022 | 230 °C, 2.16 kg |
| Density | ISO 1183-1 | 23 °C, immersion method |
| Tensile stress at yield | ISO 527-2 | Type 1A, 50 mm/min |
| Notched Izod impact | ISO 180/A | 23 °C, edgewise |
| Heat deflection temperature | ISO 75-2/B | 0.45 MPa, flatwise |
| Vicat softening temperature | ISO 306/A50 | 10 N, 50 °C/h |
| US food contact | FDA 21 CFR 177.1520 | Conditions of use A–H as applicable |
| EU food contact | EU 10/2011 as amended | Overall migration 10 mg/dm² |
On fast-cycle high-cavitation molds, batch-to-batch melt-flow variation of ±5 g/10 min can shift filling time by several hundredths of a second, which is relevant when cycle time is 3.5–5.0 s. Multi-cavity runner balance is more difficult with high-flow PP because melt temperature rises along the hot-runner manifold; hot tips with independent thermocouple control are used to maintain temperature differentials below 2 °C. A documented failure mode is uneven core cooling caused by scale buildup in water channels; this produces cavity-to-cavity shrinkage variation and lid ovality. Preventing such drift requires water circuit monitoring and periodic mold maintenance.
The gate-freeze time for a 1.0 mm gate is generally shorter than the packing time required to compensate volumetric shrinkage. With high-flow PP, the machine setup should begin switchover before the gate fully freezes, but hold-pressure decay must be tuned to avoid either sink or flash. Instrumented cavity-pressure sensors are commonly used to set switchover at 25–35 MPa cavity pressure rather than by screw position alone. Because the grade has lower viscosity, the pressure drop from gate to last-filled point is reduced, but this also means the cushion can be smaller; cushion volume below 3 mm of screw travel may lead to inconsistent packing and mass variation.
The material should be protected from prolonged heat aging; continuous exposure above 100 °C in air may cause oxidative embrittlement unless additional stabilization is specified. It is not intended for applications requiring high weld-line strength in large automotive structures, nor for contact with strong oxidizing agents or halogenated solvents. Pre-drying is generally not required below 0.05% surface moisture, but condensation on cold pellets should be prevented when warehouse RH exceeds 60%. Masterbatch and additive packages should be selected for compatibility with peroxide-visbroken polypropylene; high-pH mineral fillers and amine-containing stabilizers may affect color or long-term thermal stability.