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Water-White Kristalex 1120 Hydrocarbon Resin for Plastics Modification

    • Product Name: Water-White Kristalex 1120 Hydrocarbon Resin for Plastics Modification
    • 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 185735
    Softening Point Ring Ball C 100
    Color Apha 50 In Toluene 20
    Glass Transition Temperature Tg C 36
    Number Average Molecular Weight Mn 500
    Weight Average Molecular Weight Mw 1200
    Melt Viscosity At 150 C Mpa S 200
    Specific Gravity 25 C 25 C 1.07
    Refractive Index 20 C 1.60
    Flash Point Cleveland Open Cup C 240
    Acid Number Mg Koh G 0.1
    Bromine Number G Br2 100g 1.0
    Density At 25 C Kg L 1.07

    As an accredited Water-White Kristalex 1120 Hydrocarbon Resin for Plastics Modification factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 25 kg sealed bags of Water-White Kristalex 1120 hydrocarbon resin, supplied as pale, water-white pellets for plastics modification.
    Container Loading (20′ FCL) Load Water-White Kristalex 1120 evenly in clean, dry 20′ container; secure palletized bags with straps, preventing damage or contamination.
    Shipping The resin ships as solid pellets or flakes in multi-wall paper bags or meltable polybags on pallets. Keep dry, cool, and away from ignition sources to prevent caking and degradation. Standard non-hazardous cargo transport applies, with proper labeling for industrial use. Ensure secure stacking to avoid bag damage during transit.
    Storage Store Water-White Kristalex 1120 Hydrocarbon Resin in its original, tightly sealed container in a cool, dry, well-ventilated area. Avoid direct sunlight, excessive heat, open flames, and strong oxidizers. Maintain moderate temperatures to prevent softening or clumping. Keep away from moisture and contaminants. Ensure proper labeling and handling to preserve product purity and performance.
    Shelf Life Shelf life is two years from manufacture date when stored in original, unopened container at temperatures below 32°C.
    Application of Water-White Kristalex 1120 Hydrocarbon Resin for Plastics Modification

    Melt flow adjustment in high-gloss GPPS cosmetic packaging compounds is carried out on a corotating twin-screw extruder with L/D 32:1–40:1 using a downstream feed port for Kristalex 1120. The resin is added at 3–8 wt% relative to the polystyrene phase. Feeding the resin above the melting zone reduces screw slip. Barrel zones are set from 180°C in the feed section to 210°C at the die. Melt temperature is recorded by immersion thermocouple. The modified compound is intended for thin-wall multi-cavity moulds with wall sections below 0.8 mm. Injection moulding trials on a 1,200 kN clamp force machine require cavity pressure sensors because published data for this exact mould geometry is limited. The pressure shift at 5 wt% loading must be verified on the production tool. Melt volume-flow rate is measured according to ISO 1133-1:2022 at 200°C/5 kg. Vicat softening temperature is checked under ISO 306:2022 method B50. Tensile properties are obtained from injection-moulded specimens according to ASTM D638-14. Terminal parts include compact cases, lipstick sleeves, transparent caps and display drawers. Non-food cosmetic packaging is controlled under REACH Regulation (EC) No 1907/2006 and RoHS Directive 2011/65/EU. For food-contact cosmetic or confectionery packaging, the compounder verifies compliance with Commission Regulation (EU) No 10/2011 Annex II before production. Higher loadings above 10 wt% can reduce tensile elongation at break, so the upper boundary is confirmed by ASTM D638-14 before tool transfer.

    What Limits End-Block Reinforcement in SEBS-Based Soft-Touch Compounds?

    Kristalex 1120 partitions into the styrene-rich end-blocks of SBS and SEBS triblock matrices. This raises the effective glass transition of the hard phase and increases the storage modulus plateau between service temperature and processing temperature. Dosing is maintained at 5–15 phr relative to the elastomer. The resin is tumble-blended with SEBS crumb before paraffinic oil injection. A corotating twin-screw extruder with L/D 40:1 is operated with oil injection split across 3 barrel zones. Torque instability occurs if oil is injected before the resin melts, so the first oil injection point is positioned after the resin has experienced at least 2 full heating zones. Hardness is measured with ISO 868. Tensile strength and elongation are tested per ISO 37. Compression set is evaluated after 22 h at 70°C according to ISO 815-1. Terminal overmoulded grips for power tools and personal care devices require low odour. Volatile content is checked by VDA 278 for automotive interior relevance. Aromatic hydrocarbon resins can reduce UV stability in light-coloured soft-touch surfaces, so 0.2–0.5 wt% of a HALS-based light stabilizer is added when the part is exposed to artificial weathering under ISO 4892-2 cycles. The final compound is not assigned food-contact status unless migration testing under Commission Regulation (EU) No 10/2011 confirms the overall migration limit. Processors must also monitor Shore A hardness drift because the aromatic resin increases hardness more rapidly in high-styrene SEBS grades than in high-butylene grades. Published data for this specific segment is limited, so the formulation window is validated by pilot compounding on the target twin-screw line before commercial production.

    Extruded styrenic sheet lines running 20–40 wt% in-house thermoforming scrap often record wider die pressure fluctuations than virgin sheet. A scrap-rich edge layer is produced by adding 2–5 wt% Kristalex 1120 to the regrind stream and holding the melt temperature at 205–215°C. The resin acts as a viscosity modifier that reduces the residence time of high-molecular-weight gel particles in the screen pack. Screen packs are configured as 200/400/600 mesh layers and replaced when pre-screen pressure exceeds 120 bar. Gauge uniformity is measured with an online beta scanner. Sheet samples are conditioned at 23°C ± 2°C and 50% ± 5% RH before tensile and Vicat testing. Transparent clamshells and blister packs are tested for Vicat softening under ISO 306:2022 method B50 and for tensile yield under ASTM D638-14. The finished sheet for food-contact thermoforming must meet the overall migration limit specified in Commission Regulation (EU) No 10/2011 Annex II. Production-scale operators should verify that the addition does not raise haze above the printed specification of the sheet. Published data for this specific regrind ratio and sheet configuration is limited, so pilot runs on the target line are required before full-width specification lock.

    Recycled Polypropylene Injection Molding Compounds With Batch-to-Batch Melt Flow Drift

    Injection moulders converting washed post-consumer polypropylene flake encounter melt flow drift because the flake contains ethylene-rich caps, adhesive labels and multilayer film fragments. For rPP streams with initial melt volume-flow rates below 12 cm³/10 min at 230°C/2.16 kg, dosing 2–4 wt% Kristalex 1120 into a vented corotating twin-screw extruder reduces fill pressure and stabilizes short-shot occurrence. The extruder is operated at 190–220°C with a vacuum vent below −0.08 MPa. Flake moisture is pre-dried to below 0.1 wt% by hot-air drying at 80°C for 2 h. A melt filter with 150/250/400 mesh screens is mounted before the die. The compounded pellets are tested for melt volume-flow rate under ISO 1133-1:2022, tensile modulus under ISO 527-2:2012, flexural modulus under ISO 178:2019 and Charpy notched impact under ISO 179-1:2020. Terminal products include dark-coloured storage crates, industrial totes and returnable logistics containers. Regulatory compliance is controlled through REACH Regulation (EC) No 1907/2006 and RoHS Directive 2011/65/EU. The aromatic resin is not a compatibilizer for PE-PP phase boundaries. If the incoming flake contains more than 8 wt% loose polyethylene film, a separate compatibilizer is required because Kristalex 1120 alone cannot prevent interfacial delamination. For rPP streams with melt volume-flow rates above 30 cm³/10 min, further viscosity reduction can produce flash in tight-tolerance moulds, so the dosage is restricted to 1–2 wt% or omitted entirely.

    Application segmentKey test standardCritical regulatory boundary
    GPPS injection moldingISO 1133-1:2022, ISO 306:2022, ASTM D638-14EU No 10/2011 for food contact; RoHS 2011/65/EU
    SEBS soft-touch compoundISO 868, ISO 37, ISO 815-1VDA 278 for automotive volatiles; REACH (EC) No 1907/2006
    Recycled PP injection moldingISO 527-2:2012, ISO 178:2019, ISO 179-1:2020REACH (EC) No 1907/2006; RoHS 2011/65/EU
    Color concentrate carrierEN 13900-5, ISO 11664-4:2008EU No 10/2011 for final food-contact film
    Recycled LDPE filmASTM D1709, ISO 4593, ISO 527-1REACH (EC) No 1907/2006; VDA 277 for enclosed-space odour

    If Low-Molecular-Weight Polystyrene Carriers Cause Die Lip Plate-Out in Blown Film Color Concentrates

    In pigment concentrates for LDPE and LLDPE blown film, low-molecular-weight polystyrene carriers can create die lip plate-out during long runs. A partial replacement of 10–20 wt% of the carrier phase with Kristalex 1120 reduces plate-out frequency when the concentrate is let down at 2–4 wt% into film resin. The masterbatch is produced on a single-screw extruder with L/D 30:1 and a water-ring pelletizer. Barrel temperatures are held between 130°C and 180°C to limit thermal degradation of organic pigments. Dispersion quality is assessed by a pressure rise test according to EN 13900-5. Colour strength is measured by spectrophotometry using ISO 11664-4:2008. Terminal applications include printed retail bags, produce bags and form-fill-seal films. For food-contact films, the masterbatch is evaluated in the final film under Commission Regulation (EU) No 10/2011 Annex II, and the concentration must not exceed the overall migration limit. The resin is not recommended as a carrier additive in polyamide or PET masterbatches because the aromatic structure is incompatible with those matrices and can separate at the die. Processors must also avoid direct contact with acetal homopolymer processing equipment because residual acidic species can interact with the aromatic resin and form surface defects on film.

    Post-industrial recycled LDPE film for non-food industrial liners is processed at a melt temperature of 175–190°C, but recycled lots can drift toward lower dart impact when gel content rises during multiple heat histories. Precompounding 1.5–3 wt% Kristalex 1120 into the recycled LDPE stream reduces melt viscosity and stabilizes the bubble neck during blown film extrusion. The addition is made in a corotating twin-screw extruder with L/D 36:1 at 150–180°C. The resulting pellets are blended with virgin LDPE for the film line. Bubble stability is monitored by contactless bubble diameter measurement, and film thickness is checked according to ISO 4593. Dart impact is tested with ASTM D1709 method A, tensile strength with ISO 527-1 and density with ISO 1183-1. Terminal products include non-food industrial liners, garment bags and temporary construction films. Because Kristalex 1120 is aromatic, haze in thin films rises above 3 wt% addition, so the upper boundary is set by the customer haze limit. Odour and volatile content are assessed by VDA 277 when the film is used in enclosed spaces. Regulatory control is maintained under REACH Regulation (EC) No 1907/2006. Processing should avoid melt temperatures above 200°C because the aromatic resin can generate volatiles and raise die lip deposits on long blown film campaigns.

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    Certification & Compliance
    More Introduction

    Water-White Kristalex 1120 Hydrocarbon Resin for Plastics Modification is a low-molecular-weight aromatic hydrocarbon resin supplied in pastille and flake forms. The nominal ring-and-ball softening point is 100°C measured by ASTM E28, and the material remains in the glassy state at typical warehouse temperatures up to 40°C. The resin is designed for melt-compounded thermoplastics in which viscosity reduction, hardness development, and low color contribution are required. Typical physical data are summarized in Table 1. The product is not a plasticizer; it is a hard, brittle resin that participates in the polymer matrix as a high-Tg aromatic modifier.

    Table 1. Typical specification values for Water-White Kristalex 1120 Hydrocarbon Resin
    PropertyTypical ValueTest Method
    Softening point, ring and ball100°CASTM E28
    Density at 25°C1.07 g/cm³ASTM D792
    Molten Gardner colorbelow 1ASTM D6166
    Ash after ignition0.01 % maxASTM D5630

    What Distinguishes Water-White Aromatic Chemistry from Standard C9 Feedstocks?

    Conventional C9 aromatic hydrocarbon resins are produced from cracked petroleum fractions containing indene, vinyltoluene, and dicyclopentadiene. Those feedstocks typically yield resins with molten Gardner color between 7 and 12, and the dark chromophores carry into unpigmented compounds. Kristalex 1120 is polymerized from a purified aromatic monomer stream in which quinone-type, sulfur-containing, and nitrogen-containing chromophores are reduced. The molten Gardner color is controlled below 1 under ASTM D6166, which is the primary difference in clear polystyrene, styrene-acrylonitrile, and water-white styrenic block copolymer formulations. The aromatic structure still provides compatibility with styrene domains, but the resin does not introduce the characteristic yellow-red tint of standard C9 resin. In ASTM E313 yellowness index measurements on 2 mm plaques, compounds containing Kristalex 1120 are evaluated against the same base polymer without resin; the color shift is smaller than that observed with conventional C9 resins at equal loading. The acid number is typically below 0.1 mg KOH/g by ASTM D974, which limits catalytic interaction with metal stearate stabilizers.

    In general-purpose polystyrene and styrene-acrylonitrile compounds, loadings of 5 wt% to 15 wt% increase melt flow and raise flexural modulus. Flexural modulus is measured according to ISO 178:2019 on 4 mm molded bars; the modulus increases because the aromatic resin has a higher glass transition temperature than the base polymer. Haze and yellowness index are then checked under ASTM D1003 and ASTM E313 at 2 mm thickness. The resin is miscible with polystyrene in the melt and remains in the amorphous phase after cooling. At loadings above 15 wt%, the failure mode shifts toward more brittle behavior; notched Izod impact measured under ISO 180:2019 may decrease, so the loading is balanced against flow requirements.

    On a production-scale co-rotating twin-screw compounding line with 40:1 L/D and electrically heated barrels, Kristalex 1120 is normally dry-blended with the base polymer at the main feed throat. Barrel zones from 120°C onward melt the resin and allow it to wet polymer granules before the kneading blocks. At loadings between 3 wt% and 20 wt%, screw torque and die pressure drop relative to the unfilled polymer, which permits either higher throughput or reduced barrel set temperatures. Vacuum venting should be held at -0.08 MPa to -0.09 MPa gauge; the most common production failure is vacuum-port plugging when melt temperatures exceed 240°C, because the aromatic resin generates low-level volatile oligomers. Operators on strand pelletizing lines observe that a 0.1 wt% processing stabilizer preblended with the resin reduces die-face buildup, but published data for this specific formulation is limited. If the resin is side-fed, the side feeder should be heated to 60°C to 80°C to prevent pastille blocking in the hopper.

    Melt Flow Index Response in Polypropylene and ABS

    In polypropylene homopolymer, Kristalex 1120 functions as a melt-flow modifier at loadings between 5 wt% and 15 wt%. Melt flow index is measured under ISO 1133-1:2022 at 230°C with 2.16 kg piston load; the measured value for a 10 wt% compound is higher than the base resin because the low-viscosity aromatic oligomer reduces melt viscosity and changes the shear-thinning profile. In ABS, the same loading range reduces injection pressure and improves thin-wall fill during molding trials on an 80 t hydraulic clamp machine with a cold runner mold at 220°C to 240°C. The MFR shift is not represented by a single universal factor because it depends on base resin molecular weight distribution, peroxide vis-breaking history, and screw recovery. Reports generated from capillary rheometry under ISO 11443:2021 should state the base polymer MFR and the shear rate range, because the reduction in viscosity is more pronounced at low shear.

    Because Kristalex 1120 is compatible with styrene end-blocks, styrenic block copolymer compounds used in injection-molded footwear, grips, and overmolding are modified with 10 phr to 25 phr of the resin to raise hardness and maintain dimensional stability at service temperatures near the resin softening point. Hardness is evaluated on compression-molded plaques under ASTM D2240; measured Shore A values are typically 2 to 6 points higher than the unmodified SBC at equal oil loading. Tensile modulus increases when tested according to ISO 527-1:2019, while elongation at break may decrease depending on the styrene end-block fraction and paraffinic oil content. The water-white resin maintains lower haze than a conventional C9 resin in 2 mm plaques measured by ASTM D1003. Compatibility is strongest with high-styrene block copolymers; in low-styrene triblock copolymers, loadings above 20 phr can produce surface tack because the resin segregates into the styrene domains and leaves the rubber midblock unsaturated.

    Thermal Stability Limits Are Set by Volatile Generation Rather Than Discoloration

    At temperatures above 200°C, thermal gravimetric analysis under ASTM E2550 in nitrogen indicates that Kristalex 1120 remains mass-stable until the onset of low-molecular-weight aromatic volatile evolution accelerates above 250°C. In high-temperature matrices such as polycarbonate or polyamide, direct addition into the main feed throat is not recommended because the resin can soften and coat the feed zone before dispersing. When pre-compounding is necessary, a concentrate with 30 wt% resin in a compatible carrier is prepared at melt temperatures below 240°C and then let down to the target loading. Residence time in continuous compounding should remain below 120 seconds at melt temperatures above 220°C; otherwise vacuum venting and cold-trap maintenance become necessary to prevent volatile carryover into the pelletizing water bath. Published data for Kristalex 1120 in polyamide and polycarbonate matrices is limited, so thermal stability should be confirmed on the production line before scaling.

    Where optical clarity is not the primary requirement, polyolefin modification with Kristalex 1120 is generally restricted to loadings below 10 wt% because aromatic content increases haze and reduces light transmission in semicrystalline polyethylene and polypropylene. Blown film evaluation on a 40 mm single-screw line with a 1.2 mm die gap and 2.5:1 blow-up ratio shows that films containing 5 wt% resin remain processable, but haze measured under ASTM D1003 increases with loading and film thickness. In polypropylene, Vicat softening temperature measured under ISO 306 method A increases with resin addition, although the stiffening effect is lower than that obtained with 20 wt% talc or 10 wt% short glass fiber. Compatibility with linear low-density polyethylene is limited at loadings above 5 wt%; surface migration and delamination have been observed in production trials, and a maleic anhydride-grafted polyolefin compatibilizer may be required. Published data for this specific configuration is limited.

    Regulatory Documentation and Food-Contact Constraints

    For each end-use jurisdiction, regulatory status must be confirmed before commercialization. Supplier documentation identifies chemical inventory listings for TSCA, DSL, ENCS, and REACH where applicable; the product may be exempt from REACH registration as a polymer under Article 2(9). Food-contact suitability is not automatically conferred by the resin itself. Adhesive applications may be evaluated under FDA 21 CFR 175.105 or European Plastics Regulation EU 10/2011 only when migration testing of the finished article demonstrates compliance. No pharmaceutical or medical-grade claim is made for this product. The safety data sheet identifies molten fumes and dust as primary occupational exposure concerns; local exhaust ventilation is required during bulk transfer, grinding, and extrusion operations. In the European Union, classification and labeling must be reviewed against the latest CLP database entry for hydrocarbon resins with this molecular weight range.

    Table 2. Comparative profile with conventional C9 and C5 hydrocarbon modifiers
    AttributeKristalex 1120Conventional C9 AromaticConventional C5 Aliphatic
    Softening point100°C nominal90–140°C80–110°C
    Molten Gardner colorbelow 17–121–3
    Styrene compatibilityHighModerateLow
    Polyolefin compatibilityModerateModerateHigh
    Color contribution in clear compoundsLowHighLow

    When Kristalex 1120 Replaces a Low-Softening-Point C9 Resin

    When Kristalex 1120 replaces a conventional C9 resin with a softening point of 90°C in a styrenic modifier package, the compound gains higher resistance to warm-climate blocking and better hardness retention at elevated service temperatures. Because the nominal softening point of Kristalex 1120 is 100°C under ASTM E28, barrel temperature may need to be raised by 5°C to 10°C to maintain equivalent melt viscosity. Capillary rheometry under ISO 11443:2021 at 200°C and shear rates from 100 s⁻¹ to 10,000 s⁻¹ provides the comparison. The water-white resin also reduces the yellow tint of unpigmented compounds, but the higher softening point can reduce elongation at break in impact-modified formulations if the loading is not adjusted. In halogen-free flame-retardant systems, the resin should be evaluated against the standard C9 resin because the aromatic content may affect char formation during cone calorimetry under ISO 5660-1:2015.

    Compared with hydrogenated dicyclopentadiene or hydrogenated C9 resins, Kristalex 1120 is not hydrogenated; it retains aromatic carbon rings and therefore has stronger styrenic compatibility but lower oxidative and ultraviolet stability. In accelerated weathering under ISO 4892-2, water-white aromatic resins can yellow earlier than fully hydrogenated counterparts, so UV stabilizers are required for outdoor service. The selection between Kristalex 1120 and a hydrogenated resin is made by measuring the yellowness index under ASTM E313 after 500 h of exposure; published data for this specific resin is limited.

    Storage and handling of Kristalex 1120 require sealed containers at 30°C to 40°C. Bulk silos and pastille transfer lines should maintain product temperature below 50°C to prevent blocking; direct sunlight and high humidity increase surface oxidation potential. The product is combustible, and dust-air mixtures should be controlled below the lower explosive limit. Dust explosion protection should follow NFPA 68 or equivalent national standards. Containers should be kept closed to minimize fines accumulation in warehouse areas.

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