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ExxonMobil PP7945E1

    • Product Name: ExxonMobil PP7945E1
    • 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 183717
    Polymertype Impact Copolymer
    Meltflowrate 45 g/10 min
    Density 0.90 g/cm³
    Tensileyieldstrength 26 MPa
    Elongationatyield 5%
    Flexuralmodulus 1350 MPa
    Notchedizodimpact23c 40 J/m
    Rockwellhardness R90
    Heatdeflectiontemperature0 45mpa 95 °C
    Vicatsofteningpoint 145 °C

    As an accredited ExxonMobil PP7945E1 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing ExxonMobil PP7945E1 polypropylene homopolymer is packaged in 25 kg heat-sealed paper bags, ensuring safe handling and protection.
    Container Loading (20′ FCL) 20′ FCL container loaded with ExxonMobil PP7945E1 polypropylene, securely packed on pallets, sealed, and ready for transport.
    Shipping ExxonMobil PP7945E1 is a polypropylene copolymer supplied as solid pellets. Shipped as non-hazardous plastic resin, it is not regulated under IATA, IMDG, or DOT. Package in clean containers, avoid prolonged high heat and moisture to prevent degradation. No special transport controls are required under normal conditions.
    Storage Store ExxonMobil PP7945E1 in a cool, dry, well-ventilated area away from direct sunlight, heat, and ignition sources. Keep containers tightly sealed to prevent moisture absorption and contamination. Avoid dust accumulation; use proper grounding during handling. No special temperature control is required, but do not store near oxidizers or strong acids.
    Shelf Life Store in a cool, dry place away from direct sunlight. Shelf life is typically 12 months from date of delivery.
    Application of ExxonMobil PP7945E1

    PP7945E1 is a high-flow impact copolymer polypropylene grade; grade-specific melt mass-flow rate is reported on the certificate of analysis under ISO 1133-1:2022 at 230 °C / 2.16 kg. The material is supplied as free-flowing pellets and is processed by injection moulding in the application sectors below. Processing conditions are lot-dependent and should be established from the CoA rather than from historical process sheets.

    Lower instrument panel substrates and glove box assemblies are injection moulded from PP7945E1 on hydraulic or servo-electric machines with clamping force matched to a cavity pressure of 45–60 MPa. Barrel temperature profiles are set with rear zone at 200 °C, centre zones at 220–240 °C, and nozzle at 230–250 °C; the melt is not heated above 250 °C to preserve impact integrity. The screw is a general-purpose single-flight design with L/D of 20:1 to 25:1 and a non-return ring with 2–4 mm clearance; shot stroke is kept between 1.5 D and 3.5 D to avoid excessive residence time. Melt mass-flow rate is verified per ISO 1133-1:2022. Shot-to-shot fill variation is held below ±0.15 s because non-uniform solidification changes post-moulding shrinkage by up to 0.3% as measured by ISO 294-4:2018. The tool is gated through a valve-gated hot-runner manifold with two or three drops located on the rear face of the glove box shell; gate positions are selected after short-shot evaluation so that the flow front does not split around the latch reinforcement. Weld lines are unavoidable where fronts reunite, and their tensile strength is measured on ISO 527-2:2012 type 1A specimens machined across the weld line, with a weld-line factor of not less than 0.75 relative to un-welded material. Automotive interior compliance is established by flammability testing per ISO 3795:1989 with a target burn rate below 100 mm/min at 3.0 mm nominal section, while VOC and fogging are evaluated by VDA 277 and DIN 75201 respectively; the moulder must request grade-specific emission data because published data for this exact configuration is limited. For lower trim panels with scratch-resistant grained surfaces, a formulation of 98–99 wt% PP7945E1 to 1–2 wt% silicone-containing scratch masterbatch is dosed at the hopper; pre-drying at 80 °C for 2 h is applied when storage humidity exceeds 60% RH. End products are map pockets, lower trim panels, and glove box shells with grained or in-mould decorative surfaces.

    Impact Retention in Appliance Housings After Thermal Ageing in 95 °C Detergent Solution

    Because washing machine tubs operate under continuous hot water and alkaline detergent exposure, the processing window is defined by stabilizer retention and insert temperature. PP7945E1 is processed at a melt temperature of 220–240 °C, with screw recovery speed not exceeding 100 rpm on a 25 mm reciprocating screw, because higher shear raises the melt temperature locally and consumes antioxidant. A critical process conflict occurs at the bearing insert over-mould: the insert temperature must be held between 80 °C and 110 °C before injection. If the insert temperature is below 80 °C, the thermal quench at the PP-metal interface creates a micro-gap that promotes detergent wicking and stress cracking; above 110 °C, excessive cooling time and insert oxidation may occur. Qualification includes tensile property retention after immersion in 1.0 wt% sodium carbonate solution at 95 °C for 1,000 h; retention of elongation at yield above 70% of the as-moulded value under ISO 527-2:2012 is a common release criterion. Notched Charpy impact per ISO 179-1:2010/eA is measured before and after ageing, and any crack propagation at the gate or weld line is recorded. The end products are outer tubs, impellers, and pump housings that are annealed at 90 °C for 30 min after demoulding to relax frozen-in orientation. Published data for PP7945E1 in long-term hot detergent exposure is limited, so production validation includes a 72 h moulded-part test at the maximum fill temperature with the specific detergent formulation used by the appliance OEM.

    For returnable transport packaging, injection moulding of foldable crates with integrally moulded hinges forces a trade-off between stiffness and hinge fatigue. The part is filled at wall thickness of 3.0–4.5 mm with a profiled injection velocity of 120–180 mm/s in the main flow and 40–60 mm/s near the hinge to avoid jetting and surface splay. Because the grade flows easily, the end of fill does not normally limit cavity pressure, but over-packing around the hinge can create density gradients that reduce flexural fatigue life. Hinge durability is checked by cycling a 2.0 mm hinge from to 180° for 50,000 cycles at 23 °C; no crack deeper than 0.5 mm under 10× magnification is the internal release criterion, although no ISO standard covers this component-specific test. Stacking load is evaluated according to ISO 2234:2015 with the filled crate loaded to the calculated top-load value for 24 h at 23 °C and 50% RH. If direct food contact is required, EU Regulation 10/2011 migration testing is mandatory; PP7945E1 is not a dedicated food-contact grade unless explicitly certified for the intended food types and temperature conditions. The end products are collapsible crates, bakery trays, and returnable dunnage for automotive parts. Formulation for UV-stabilized outdoor crates includes 1–2 wt% of a hindered-amine light stabilizer masterbatch and 0.5–1.0 wt% of carbon black masterbatch, dosed at the throat and verified by melt filtration pressure rise of less than 20 bar over 4 h.

    Which Processing Strategy Prevents Warpage in Mineral-Filled Compounding Formulations?

    When PP7945E1 is used as the impact copolymer base for mineral-filled compounds, warpage in downstream moulding is controlled by filler aspect ratio, orientation, and the thermal history of the extrudate. A co-rotating twin-screw extruder with L/D 40:1 is configured with an atmospheric vent and side feeding at barrel 6 of 10. Talc or calcium carbonate loadings of 20–30 wt% require distributive mixing after the side feeder; kneading blocks with 45° forwarding angle are used before the side feeder to melt the base resin. Melt temperature at the die is kept below 220 °C to reduce volatile evolution and to preserve impact strength. The compound is strand-pelletized, dried to below 0.05 wt% moisture, and then injection moulded into test plaques. Warpage is measured according to ISO 294-4:2018 after 48 h conditioning at 23 °C and 50% RH; flexural modulus is measured by ISO 178:2019, and notched Charpy impact by ISO 179-1:2010/eA. At filler loadings above 20 wt%, anisotropic shrinkage can be 0.3–0.5% lower in the flow direction than in the transverse direction, requiring a tool compensation factor based on moulding trials at the intended gate location. The end products are mineral-filled appliance brackets and automotive interior substrate layers, where the compound is formulated at 70–80 wt% PP7945E1, 20–30 wt% talc or calcium carbonate, 0.1–0.2 wt% primary antioxidant, 0.1–0.2 wt% secondary antioxidant, and 1–2 wt% colour masterbatch. Published data for this specific formulation configuration is limited; each compound lot is qualified by measuring MFR per ISO 1133-1:2022 and by a 24 h water absorption check per ISO 62:2008 for moisture-sensitive applications.

    The following qualification matrix is applied to PP7945E1 moulded components before production release.

    PropertyStandard / MethodCondition
    Melt mass-flow rateISO 1133-1:2022230 °C, 2.16 kg
    Tensile yield stressISO 527-2:201250 mm/min, type 1A
    Flexural modulusISO 178:20192 mm/min
    Notched Charpy impactISO 179-1:2010/eA23 °C, edgewise
    Notched Izod impactISO 180:2023/A−20 °C
    Heat deflection temperatureISO 75-2:2013 method B0.45 MPa
    Vicat softening temperatureISO 306:2022 A5010 N, 50 °C/h
    ShrinkageISO 294-4:201860 mm × 60 mm × 2 mm plaque

    When the Moulded Part Requires Low-Temperature Drop Performance at −20 °C

    Outdoor furniture shells and institutional seating shells are qualified by drop impact at sub-zero temperature rather than by room-temperature Izod alone. Impact copolymer PP grades can undergo a ductile-to-brittle transition between −10 °C and −30 °C; component-level validation therefore includes instrumented puncture at −20 °C, not solely room-temperature Izod data. Drop tests use a 5.0 kg hemispherical striker at heights of 0.5–1.0 m; the acceptance threshold is no visible crack when examined under 10× magnification. Mould surface temperature is set to 30–40 °C to improve crystallinity uniformity and reduce residual stress; cooling circuits are sized for turbulent flow with Reynolds number above 10,000 in the gate region. The gate is positioned away from the impact site to reduce molecular orientation perpendicular to crack propagation. The grade is checked for notched Izod impact at −20 °C per ISO 180:2023/A; supplier control charts and production lot CoA define the acceptance range, and published data for PP7945E1 in this specific configuration is limited. Formulation includes 1–2 wt% UV stabilizer masterbatch and, for outdoor colour stability, 0.5–1.0 wt% pigment masterbatch. End products are stadium seat shells, waiting-room bench components, and garden furniture structural elements, where accelerated weathering verification is conducted according to ISO 4892-2:2013.

    In lead-acid battery container moulding, acid resistance and post-weld low-temperature impact are the two release criteria that control material substitution. The jar is injection moulded at a melt temperature of 230–250 °C, with holding pressure of 50–70 MPa maintained until gate freeze. Wall thickness is kept between 2.5 mm and 3.5 mm; rib-to-wall ratio is kept below 0.6 to limit sink marks at cell partition bases. Acid resistance is tested by immersion in 1.28 g/cm³ sulfuric acid at 60 °C for 28 days, followed by tensile retention per ISO 527-2:2012. Lid sealing is performed by hot-plate welding with platen temperature 230–250 °C and weld time 10–15 s under controlled displacement; weld burst strength is tested according to the mechanical integrity provisions of EN 50342-1:2018. Because PP7945E1 is not a dedicated battery grade, production qualification includes lot-by-lot melt flow rate verification per ISO 1133-1:2022 and oxidation induction time assessment per ISO 11357-6:2018 for under-hood thermal exposure. The formulation is typically 97–99 wt% PP7945E1 with 1–3 wt% carbon black masterbatch for acid-opaque containers. The end products are battery containers, lids, and vented cell covers used in SLI batteries. For acid resistance testing, specimens are machined from the side wall, not the gate area, to avoid orientation-induced property differences.

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    Certification & Compliance
    More Introduction
    ExxonMobil PP7945E1 is a clarified polypropylene homopolymer formulated for biaxially oriented film (BOPP) conversion on sequential-stretching tenter-frame lines. The resin delivers a nominal melt mass-flow rate of **3.5 g/10 min** when measured under a **2.16 kg** load at **230 °C** in accordance with **ISO 1133-1:2022**. Density registers at **0.900 g/cm³** (**ISO 1183-1:2019**). The additive package includes a sorbitol-based clarifier, an acid scavenger, and a tailored anti-block/slip system that accumulates static COF below **0.25** after 14‑day conditioning at **23 °C** and **50 % RH**. These characteristics target high‑clarity flexible packaging, tobacco overwrap, pressure‑sensitive label stock, and adhesive tape backings.

    What Differentiates This Grade from a Standard PP Homopolymer in Tenter Operation?

    The distinction resides in the interplay between clarifier solubility, melt strength, and controlled oligomer migration. Whereas an unclarified homopolymer of equivalent flow and crystallinity returns a haze value above **15 %** on **50 µm** biaxially stretched film (**ASTM D1003**), PP7945E1 routinely achieves **1.2–1.8 %** haze when processed within a melt‑temperature window of **245–260 °C**. The sorbitol‑derived nucleating agent dissolves completely above **230 °C** but precipitates as a fine, fibrous network during chill‑roll cooling to **30 °C**, raising the crystallization onset temperature by **12–15 °C** versus the un‑nucleated base resin. This elevated Tc narrows spherulite size to sub‑wavelength dimensions, directly impacting light transmission without sacrificing flexural modulus, which remains at **1550 MPa** (**ISO 178:2019**). In comparison, ExxonMobil PP7955E1 — a higher‑flow BOPP grade with an MFR of **5.5 g/10 min** — sacrifices roughly **8–10 %** in room‑temperature flexural modulus and exhibits an equilibrium moisture regain **0.22 %** higher under tropical warehouse conditions, which can promote slip‑agent bloom during extended shelf storage. The lower MFR of PP7945E1 also contributes to a wider processing latitude during transverse‑direction stretching: measured elongation at yield in the melt‑cast sheet increases from **7 %** to **9 %** (**ISO 527‑2**) compared to 5.5‑MFR alternatives, permitting higher draw ratios before catastrophic neck‑in.
    Property PP7945E1 PP7955E1 PP7352E1 (High‑Clarity)
    MFR (230 °C, 2.16 kg) – g/10 min 3.5 5.5 2.8
    Flexural Modulus (ISO 178) – MPa 1550 1410 1350
    Haze, 50 µm BOPP film – % 1.2–1.8 1.5–2.2 0.8–1.2
    Charpy Notched Impact (23 °C, ISO 179) – kJ/m² 3.0 2.7 4.5
    Refractive Index (nD, 25 °C) 1.503 1.503 1.502

    Stenter-Frame Orientation and Output Rates

    In continuous BOPP production on a Brückner or DMT sequential tenter operating at **350–450 m/min** line speed, PP7945E1 is extruded through a flat‑die at **250–265 °C** onto a chill‑roll stack maintained at **28–32 °C**. The cast sheet, typically **180–240 µm** thick, must achieve a crystallinity of ≤ **5 %** in the amorphous‑nucleated state to permit adequate stretching. Quality‑critical sheet gauge uniformity — within **±1.5 %** across a **8.0‑m** die — is maintained by automatic die‑bolt adjustment based on online beta‑gauge feedback; any local thickness deviation exceeding **2 %** manifests as a visible die‑line in the final **18‑25 µm** film. Machine‑direction stretching proceeds through a series of heated rolls ramping from **120 °C** to a peak of **140 °C**, applying a draw ratio of **5.0:1** to **5.5:1**. The stretched sheet then enters the transverse‑direction stretching oven, where clip‑chain rails diverge at a rate generating a **8.0:1** to **10.0:1** stretch ratio over a **45‑meter** zone heated with pressurized air at **165–175 °C**. PP7945E1 exhibits a critical neck‑stabilization temperature of **152 °C** below which transverse‑direction gauge variation exceeds **4 µm** and transverse‑direction tear strength (**ASTM D1922**) drops below **0.15 N**. The upper threshold for the TD‑stretch zone is **185 °C**; dwell above this point initiates solubilization of the sorbitol clarifier, leading to re‑agglomeration and a haze increase of **0.3–0.5 %** per **5 °C** overshoot. Relaxation rollers after the annealing section (set **3–5 °C** below the stretching temperature) allow **2–4 %** shrinkage to reduce internal stress, resulting in a final film thermal shrinkage of **≤ 4 %** after **5 minutes** at **120 °C** (**ASTM D1204**). The film is then corona‑treated to **38–42 dyn/cm** surface energy to ensure adhesion for downstream printing or metallization.
    Parameter Setting / Range Test Method / Equipment
    Melt temperature (die inlet) 245–265 °C2 °C per zone) IR pyrometer / thermocouple mesh
    Chill‑roll temperature 28–32 °C Contact thermocouple, roller surface
    Cast sheet thickness 180–240 µm Beta‑ray gauge (Radiomatic)
    MD draw ratio 5.0–5.5:1 Roll speed differential
    TD draw ratio 8.0–10.0:1 Clip‑chain divergence angle
    Corona treatment intensity 10–12 W/m²/min Dyne test fluids (ISO 8296)

    When Coextrusion with EVOH Barrier Layers Is Required

    PP7945E1 acts as the structural skin layer in three‑layer or five‑layer BOPP/EVOH/BOPP cast films. Maleic‑anhydride‑grafted PP tie‑resins (adhesion layer melt‑flow rate **3.0–4.0 g/10 min**) are coextruded between the PP and EVOH to achieve interlayer adhesion > **2.5 N/15 mm** under **T‑peel** (**ASTM D1876**). The processing window narrows: EVOH grades with **38 mol%** ethylene content demand a combined melt stream temperature at the die not exceeding **240 °C**, to prevent cross‑linking and gel formation. PP7945E1’s lower processing temperature requirement relative to higher‑MFR grades aligns with this ceiling. At the same time, the clarifier in PP7945E1 must not exude into the tie‑layer during annealing; exudation of low‑molecular‑weight sorbitol derivatives increases the oxygen transmission rate (**ASTM D3985**) of the composite structure by **15–20 %** after 30 days at **38 °C**, **90 % RH**, as measured by MOCON OX‑TRAN 2/40. To mitigate this, the cast sheet is quenched to **25 °C** on a polished chill roll before entering the MD‑stretching unit, keeping the out‑of‑plane sorbitol migration depth below **200 nm** as verified by confocal Raman microscopy. Any deviation in the MD‑stretching temperature above **142 °C** coarsens the network and accelerates migration, compromising both haze and oxygen barrier. In water‑quenched blown‑film configurations employed for coextruded shrink‑label BOPP, the asymmetric quench introduces a through‑thickness crystallinity gradient of **8–12 %** between the water‑contact and air‑contact surfaces. PP7945E1 exhibits a tighter gradient tolerance than PP7955E1 due to its lower MFR and higher zero‑shear viscosity, which reduces sag and preserves wall‑thickness uniformity during bubble expansion. The blow‑up ratio is maintained at **2.0:1** to **2.2:1**, and frost‑line height is locked at **0.6–0.8 m** above the die face to avoid premature crystallization that would generate surface haze > **3 %** at the gusseted fold edges. In practice, this configuration demands that the moisture content of pelletized feedstock be controlled below **0.08 wt%**; a desiccant‑bed hopper dryer with dew point **−40 °C** and residence time of **2 hours** at **80 °C** is specified whenever plant ambient humidity exceeds **60 % RH**. Published data for this specific blown‑film configuration is limited, but industrial trials on a Reifenhäuser three‑layer line indicate stable operation at net output rates of **120 kg/h** with defect‑free roll lengths exceeding **24,000 linear meters**.
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