BOTTLE GRADE PET RESINS YS-C02

    • Product Name: BOTTLE GRADE PET RESINS YS-C02
    • Factroy Site: Binhai Road, Yangpu Economic Development Zone, Danzhou, Hainan, China
    • Price Inquiry: sales2@ascent-chem.com
    • Manufacturer: Hainan Yisheng Petrochemical Co., Ltd
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    VTB
    Specifications
    HS Code 973348
    Grade YS-C02
    Material Bottle-grade polyethylene terephthalate (PET) resin
    Intrinsic Viscosity 0.80 ± 0.02 dL/g
    Density 1.33 g/cm³
    Melting Point 245 ± 2 °C
    Glass Transition Temperature 78 °C
    Moisture Content ≤ 0.20%
    Acetaldehyde Content ≤ 1.0 ppm
    Diethylene Glycol Content ≤ 1.3%
    Carboxyl End Groups ≤ 30 mol/t
    Color B Value ≤ 1.0
    Bulk Density 0.80–0.90 g/cm³
    Particle Size 2.5–3.5 mm
    Form Pellets/chips

    As an accredited BOTTLE GRADE PET RESINS YS-C02 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
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    Application of BOTTLE GRADE PET RESINS YS-C02

    On high-cavitation injection stretch blow molding lines converting YS-C02 into carbonated soft drink preforms, the governing process variables are retained intrinsic viscosity, acetaldehyde concentration, and hoop orientation rather than melt flow alone. Pre-drying in a desiccant dryer with air dew point ≤ −30°C at 160–170°C for 4–6 h is required, especially when ambient storage relative humidity exceeds 60%, to reduce pellet moisture to ≤ 50 ppm; residual moisture above 0.005 wt% accelerates hydrolytic chain scission and can depress the preform intrinsic viscosity below 0.75 dL/g after injection, reducing sidewall burst pressure. Melt temperatures are controlled at 270–290°C, with barrel residence time not exceeding 5 min and screw L/D ratios of 20:1–24:1 to limit shear heating. The addition ratio for unpigmented sparkling water preforms is commonly 100 wt% virgin YS-C02; where regional food-contact legislation permits mechanically recycled rPET, converters use 70–100 wt% YS-C02 with 0–30 wt% rPET, validated by migration testing. Colorant masterbatches are metered at 0.5–2.0 wt%, and acetaldehyde scavenger masterbatches are metered at 0.05–0.15 wt% only when package headspace acetaldehyde below 3 µg/L is required. Compliance is established under U.S. FDA 21 CFR 177.1630, EU Regulation (EU) No 10/2011 Annex I, and GB 4806.7-2016, with overall migration testing per EN 1186-1. After injection, preforms are conditioned to 100–120°C and stretch blow molded at 3.0–4.0 MPa blow pressure; mold temperatures of 8–15°C are held to maintain hoop orientation. Axial stretch ratios of 2.6:1–3.0:1 and radial stretch ratios of 3.0:1–3.4:1 yield sidewall crystallinity in the 20–30% range. Terminal product types include 200 mL, 330 mL, 500 mL, 1.0 L, 1.5 L, 2.0 L, and 2.5 L carbonated soft drink and sparkling water bottles with 28 mm or 38 mm finish configurations.

    Can the Same Preform Resin Span Cold-Fill and Aseptic Still Water Lines?

    Still water conversion differs from carbonated packaging primarily in the absence of hoop-stress shelf-life requirements, which shifts rejection criteria toward acetaldehyde control and preform weight consistency. YS-C02 is processed at 260–280°C in high-output preform cells, where melt temperature is reduced to suppress thermal degradation; injection pressures between 60–90 MPa and cycle times of 8–12 s are typical for preform masses of 12–30 g. Batch-to-batch intrinsic viscosity variance of ±0.02 dL/g shifts preform conditioning setpoints by 3–5°C, and line operators compensate by adjusting conditioning oven zone temperatures rather than melt temperature. The formulation addition ratio for still water is 100 wt% virgin YS-C02 or a validated blend of 75 wt% YS-C02 with 25 wt% food-grade rPET; blue toner masterbatches are dosed at 0.1–0.3 wt%, while slip-agent or antistat additives are generally avoided to prevent haze formation. Regulatory compliance for cold-fill and aseptic containers is anchored to U.S. FDA 21 CFR 177.1630, EU Regulation (EU) No 10/2011, GB 4806.7-2016, and the Japan Food Sanitation Act for export lots. Downstream, preform conditioning at 100–115°C and blow molding at 2.5–3.5 MPa with mold temperatures of 8–14°C produce balanced sidewall orientation; aseptic filling lines additionally require peroxide or steam sterilization compatibility at surface temperatures up to 75°C without sidewall deformation. Terminal product types include 200 mL, 250 mL, 330 mL, 500 mL, 750 mL, 1.0 L, 1.5 L, and 2.0 L still water and flavored water bottles, including handle-less aseptic packages with 26 mm, 28 mm, or 30/25 mm finishes.

    Oxygen Ingress and Cap Seal Integrity in 5 L Edible Oil Packs

    Edible oil packaging exposes YS-C02 to hydrophobic product contact and long ambient shelf life, where the failure mode is not environmental stress cracking but oxygen ingress through the bottle wall and neck ovality under cap torque. For 1.8 L, 2.5 L, and 5 L edible oil bottles, the typical addition ratio is 100 wt% virgin YS-C02 to maintain food-contact traceability; UV-blocking masterbatches are compounded at 0.5–2.0 wt% for light-sensitive oils, and pigmented masterbatches at 0.5–1.5 wt% are used for color indexing. Recycled rPET inclusion is limited to 0–25 wt% only where the rPET source is authorized under EU Regulation (EU) No 10/2011 or U.S. FDA 21 CFR 177.1630 food-contact submissions, and the converter must validate surrogate contaminant clearance using challenge testing because post-consumer contamination clearance is the critical regulatory variable. Preform injection is performed at 280–290°C with shot weights of 105–130 g for 5 L containers; elevated melt temperature is required to fill thick preform walls, but barrel residence time is kept below 6 min to avoid acetaldehyde formation above 2 µg/L in the preform. Blow molding uses 3.0–3.5 MPa air pressure and mold temperatures of 8–12°C, with axial stretch ratios of 2.4:1–2.8:1 and radial stretch ratios of 3.0:1–3.3:1. Production-scale equipment behavior shows that cap seal leakage in large PET oil bottles is primarily caused by neck ovality exceeding 0.15 mm on the finish diameter; inline vision systems with 0.05 mm resolution are therefore installed after blow molding to reject packages before filling. Compliance for edible oil packs is established under U.S. FDA 21 CFR 177.1630, EU Regulation (EU) No 10/2011, and GB 4806.7-2016; oxygen permeability of oriented PET is typically in the range of 2–6 cm³·mm/(m²·day·atm) at 23°C and 0% RH, measured by ASTM D3985-17, and published oil-specific shelf-life data for YS-C02 is limited. Terminal products include 1.8 L, 2.5 L, and 5 L bottles for soybean, canola, sunflower, and blended edible oils, with 45 mm, 48 mm, or 63 mm neck finishes.

    When Thick-Walled PET Replaces Glass in Serum Pump Packaging

    Cosmetic and personal care packaging uses YS-C02 in one-stage injection stretch blow molding cells to obtain thick-walled, high-clarity containers that must survive repeated actuator insertion and pump fatigue without stress whitening. The addition ratio is 100 wt% virgin YS-C02 for optimized drop impact; recycled rPET is permitted at 0–30 wt% for non-food cosmetic references only when flake traceability and heavy-metal limits under REACH Regulation (EC) No 1907/2006 are met. Color masterbatches are dosed at 0.5–2.0 wt%, UV absorber masterbatches at 0.1–0.5 wt%, and pearlescent effect masterbatches at 0.5–1.5 wt%; amine-based colorants and blowing agents are avoided because they accelerate acetaldehyde formation and surface haze. Melt temperatures of 270–285°C and filling speeds below 60 mm/s are used to avoid gate blush on preforms with wall thicknesses of 4–8 mm; holding pressure is set between 80–100 MPa to minimize sink marks before the blow cavity. Preform conditioning at 105–118°C and blow pressure of 2.5–3.0 MPa with mold temperatures of 20–25°C produce high gloss and improved drop resistance. Regulatory documentation for cosmetic packaging is based on EU Regulation (EC) No 1223/2009 for packaging compatibility, REACH Regulation (EC) No 1907/2006 for substances of very high concern, and U.S. 16 CFR 1700.20 where child-resistant closures are used; migration testing under EN 1186-1 is not required for non-food cosmetics but is often requested by global brand owners. Terminal product types include 30 mL, 50 mL, 100 mL, 150 mL, 200 mL, and 500 mL serum bottles, lotion pump bottles, and cosmetic jars with 18/410, 20/410, 24/410, and 28/410 neck finishes.

    Where wide-mouth food jars require hot-fill capability without adopting glass or polypropylene, YS-C02 is processed through heat-set blow molding to raise sidewall crystallinity above 30% and limit volumetric retraction after filling at 85–92°C. The addition ratio is 100 wt% virgin YS-C02 for hot-filled sauces and jams; colorant masterbatches are added at 0.5–1.5 wt%, and rPET is limited to 0–25 wt% only if refill-stress performance at 85°C is revalidated because rPET lowers intrinsic viscosity and thermal crystallization potential. Preform injection uses melt temperatures of 270–280°C and preform conditioning at 105–120°C; the blow mold is maintained at 130–160°C to induce thermal crystallization after mechanical stretching, and the bottle is held in the mold for 2–4 s at 2.0–3.5 MPa blow pressure to stabilize sidewall dimensions. Compliance is documented under U.S. FDA 21 CFR 177.1630, EU Regulation (EU) No 10/2011, and GB 4806.7-2016, with fill-point temperature resistance verified by measuring diameter change at 85°C for 30 min; total migration testing per EN 1186-1 is conducted on the finished jar. Terminal product types include 200 mL, 300 mL, 500 mL, 750 mL, and 1.5 L wide-mouth jars for pasta sauce, jam, peanut butter, honey, and shelf-stable salsa, with 63 mm, 70 mm, 82 mm, and 89 mm lug neck finishes.

    Compendial Qualification of YS-C02 for Syrup Bottles Depends on Extractables Control

    The production of pharmaceutical syrup bottles from YS-C02 is governed by controlled injection stretch blow molding with documented low acetaldehyde and absence of process-derived extractables. The addition ratio is 100 wt% virgin YS-C02; rPET is excluded because compendial traceability and batch-release limits under USP <661.1> and Ph. Eur. 3.1.15 are not satisfied by mixed post-consumer feedstock. Colorant masterbatches are limited to 0–0.5 wt% and must be listed in the plastic additive inventory; amine-bearing additives and reclaimed processing aids are not used. Preform injection occurs in cleanroom-compatible machines at 270–280°C, with pre-drying to ≤ 50 ppm moisture and acetaldehyde control below 2 µg/L in the preform; injection hold time is extended to minimize sink marks on 1.5–3.0 mm preform walls. Blow molding is performed at 2.5–3.0 MPa with mold temperatures of 8–12°C, and the resulting bottles are tested for extractables, heavy metals, and pH shift according to USP <661.1>, USP <661.2>, and Ph. Eur. 3.1.15, alongside food-contact compliance under U.S. FDA 21 CFR 177.1630 where the product is regulated as a dietary supplement. Production-scale equipment behavior shows that mold release sprays containing silicone can raise surface extractables and must be replaced with dry release systems. Published data for YS-C02 in compendial pharmaceutical configurations is limited; each line must be qualified against the finished container monograph using filled-product stability protocols. Terminal product types include 50 mL, 100 mL, 125 mL, 200 mL, and 500 mL syrup bottles and oral dose containers with 28 mm, 33 mm, and 45 mm child-resistant and senior-friendly closures.

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