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Dongguan Pule Plastic ABS PL-A09

    • Product Name: Dongguan Pule Plastic ABS PL-A09
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 745663
    Productname Dongguan Pule Plastic ABS PL-A09
    Manufacturer Dongguan Pule Plastic Co., Ltd.
    Grade PL-A09
    Materialtype ABS (Acrylonitrile Butadiene Styrene)
    Polymerfamily Styrenic copolymer
    Appearance Pellets
    Color Natural/Black, custom colors available
    Processingmethod Injection molding
    Density 1.04–1.06 g/cm³
    Meltflowrate 15–25 g/10 min
    Tensilestrength 40–48 MPa
    Elongationatbreak 15–30%
    Flexuralstrength 60–75 MPa
    Flexuralmodulus 2200–2600 MPa
    Heatdeflectiontemperature 80–90 °C
    Vicatsofteningtemperature 90–100 °C
    Rockwellhardness 100–110 R
    Moldingshrinkage 0.4–0.6%
    Dryingtemperature 80–90 °C
    Processingtemperature 200–230 °C
    Flamerating HB

    As an accredited Dongguan Pule Plastic ABS PL-A09 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Packed in 25 kg net-weight moisture-proof bags, palletized and shrink-wrapped for secure storage and transport of Dongguan Pule Plastic ABS PL-A09.
    Container Loading (20′ FCL) Container Loading (20′ FCL): Dongguan Pule Plastic ABS PL-A09 packed in bags, palletized, shrink-wrapped, and secured inside a 20-foot FCL container.
    Shipping Dongguan Pule Plastic ABS PL-A09 is a non-hazardous ABS resin and is not regulated as dangerous goods for transport by road, sea, or air. Ship in sealed, dry packaging, protected from moisture, heat, and direct sunlight. No special shipping labels or placards are required.
    Storage Store Dongguan Pule Plastic ABS PL-A09 in a cool, dry, well-ventilated area away from direct sunlight, heat, ignition sources, and moisture. Keep containers tightly closed and labeled. Prevent dust generation and static buildup. Store separately from incompatible chemicals and oxidizers. Maintain stable temperature and humidity, avoid prolonged storage near strong odors, and follow the manufacturer’s safety data sheet and local regulations.
    Shelf Life Shelf life is approximately 12 months when stored in original unopened packaging under cool, dry conditions, away from sunlight.
    Application of Dongguan Pule Plastic ABS PL-A09

    Selective Etch Morphology and Adhesion Requirements in Electroplating-Grade ABS PL-A09 Automotive Trim

    Selective etch morphology in electroplating-grade ABS PL-A09 automotive brightwork depends on the distribution of polybutadiene particles in the injection-moulded skin rather than on bulk rubber content alone. In formulations for decorative chromium plating, ABS PL-A09 is metered at 100 parts by mass of the polymer fraction, with ethylene bisstearamide as external lubricant at 0.2–0.5 phr and a hindered phenol antioxidant at 0.1–0.3 phr; the compound is kept free of calcium carbonate or other fillers that would alter microcavity geometry during chromic-sulphuric acid etching. The substrate is injection moulded at melt temperature 240–260 °C and mould-surface temperature 60–80 °C using a reciprocating screw with L/D 20:1–22:1, screw back pressure 0.5–1.0 MPa, and clamping pressure sufficient to maintain the cavity parting line below 0.02 mm. After demoulding, parts are annealed at 80 °C for 2 h to relax frozen orientation; unstressed substrates are etched at 65–70 °C for 8–12 min in chromic-sulphuric acid, producing open surface cavities of 1–3 µm diameter. The electroless nickel deposition is followed by semi-bright nickel, bright nickel, and microporous chromium layering; total deposit thickness for exterior brightwork is typically 20–35 µm according to service condition 4 in ASTM B604-19.

    Compliance for exterior automotive trim is evaluated by ASTM B604-19 for coating specification, ASTM B533 for peel adhesion, ISO 1456:2009 for copper-nickel-chromium electrodeposits, RoHS 2011/65/EU and REACH substance restrictions. Automotive OEM standards generally require peel adhesion not less than 9 N/25 mm and thermal shock resistance across -40 °C to 80 °C without blistering; failure modes observed on production lines include local current-density shadowing over gate vestiges and adhesion collapse when moulded-in stress exceeds 6 MPa in the part skin. Terminal parts in this application segment include front grille surround trims, door mirror housings, instrument cluster bezels, steering-wheel control inserts, and wheel centre caps; each part family uses the same etch-and-plate chemistry but requires bespoke runner balancing because the chromium deposit reveals any knit-line or gas-trap defect as a visible delamination or clouded reflection.

    Across miniature circuit breaker and socket-outlet housing lines, flame-retardant ABS PL-A09 compounds are formulated to pass UL 94 V-0 at 1.5 mm without sacrificing the injection-moulding flow length required for multi-cavity tools. A production-validated loading range for this grade places ABS PL-A09 at 78–82 wt% of the compound, brominated epoxy oligomer at 12–16 wt%, antimony trioxide at 3–5 wt%, and phosphate stabilizer at 0.1–0.3 wt%; the brominated epoxy is selected because its aromatic backbone maintains thermal stability during compounding, and the absence of polybrominated diphenyl ethers is required under RoHS 2011/65/EU and REACH. The compound is melt-blended on a co-rotating twin-screw extruder with L/D 40:1, screw speed 300–400 rpm, barrel temperatures 170–210 °C, and head temperature 210 °C. A vacuum port at -0.08 MPa strips volatile degradation products, because antimony trioxide can accelerate styrene-acrylonitrile chain scission above 225 °C; residence time is limited to less than 180 s to avoid pre-crosslinking of the brominated epoxy. The pellet feed is dried at 80 °C for 3–4 h to moisture below 0.05% before injection moulding at melt temperature 200–235 °C and mould temperature 50–70 °C.

    Compliance in switchgear housing service is anchored to UL 94 V-0 at 1.5 mm and 1.0 mm, IEC 60695-11-10 for 50 W horizontal and 500 W vertical flame tests, IEC 60695-2-12 glow-wire flammability index at 850 °C, and IEC 62368-1:2023 for fire enclosure requirements in audio/video and ICT equipment. Injection moulding operators track screw cushion, vent flow, and gas-burn marks; if the melt temperature exceeds 225 °C for more than 120 s, plate-out on the mould surface increases and the UL 94 afterflame time drifts from <2 s per specimen toward the 10 s limit. Terminal finished products supplied from this compound include miniature circuit breaker housings, contactor bases, socket-outlet frames, wiring accessory boxes, and power adapter shells.

    Table 1 — Flame-retardant loading gradient for ABS PL-A09 evaluated at 1.5 mm specimen thickness
    PL-A09 (wt%)Brominated epoxy (wt%)Antimony trioxide (wt%)UL 94 vertical resultMelt temperature limit (°C)
    82123V-1 borderline; afterflame >10 s225
    80144V-0 pass; afterflame <2 s225
    78165V-0 pass but plate-out increase220

    What Limits Low-Temperature Ductility When PL-A09 Is Compounded with Polycarbonate for Instrument Panel Carriers?

    PC/ABS blends for instrument panel carriers use ABS PL-A09 as the flow- and impact-modifying phase at 30–45 wt% of polymer, with bisphenol-A polycarbonate at 55–70 wt%, an MBS core-shell impact modifier at 2–5 wt%, and a phosphite stabilizer at 0.1–0.2 wt%; lowering the ABS fraction below 30 wt% raises notched Charpy impact at 23 °C but increases melt viscosity and reduces knit-line strength, while exceeding 45 wt% lowers heat deflection temperature below what instrument panel retainers require at 100 °C after in-cabin solar load. The two resins are dried separately at 100–110 °C for 4–6 h to residual moisture below 0.02%, then compounded on a co-rotating twin-screw extruder with L/D 36:1–40:1, screw speed 350–450 rpm, and melt temperature 250–270 °C; polycarbonate hydrolysis is the main failure risk, and a moisture level above 0.03% produces surface silver streaks as well as a drop in ISO 179-1/1eA notched impact below 10 kJ/m² at -20 °C. Amine-based heat stabilizers must be excluded from this formulation because amine species catalyse polycarbonate chain scission at processing temperatures.

    Injection moulding of instrument panel carriers uses sequential valve-gated hot runners with melt temperature 250–265 °C and mould temperature 70–90 °C; thick ribs are gas-assisted to avoid sink marks without extending cycle time beyond 60 s. Restricted gating is avoided near airbag deployment seams because frozen molecular orientation at the weld line reduces cold-temperature ductility. Automotive interior compliance is assessed with ISO 1133-1:2022 for melt volume-flow rate, ISO 178 for flexural modulus, ISO 179-1/1eA for Charpy notched impact, ISO 306 for Vicat softening temperature, and VDA 277 or GS 97014-3 for total volatile organic compound emissions; OEM specifications typically require ≤ 50 µg/g total VOC. Terminal finished products include instrument panel retainers, centre console carriers, HVAC ducting, air vent housings, and knee-bolster inserts; each product group is subject to different part thicknesses and gloss levels, so the compounding recipe is adjusted within the stated PL-A09 loading range rather than changed chemically.

    When Solvent-Cemented ABS PL-A09 Fittings Enter Corrosive Chemical Drainage Service

    Chemical drainage systems in laboratories and metal-finishing plants join injection-moulded ABS PL-A09 fittings to extruded pipe with solvent cement containing methyl ethyl ketone and acetone; the cement dissolves the fitting socket surface and forms a fused joint whose hydrostatic burst strength is a function of interference fit and cement viscosity, not just pipe wall thickness. PL-A09 is processed at 100 parts by mass resin with calcium stearate internal lubricant at 0.1–0.3 phr and titanium dioxide at 0–2 phr where colour coding is required; the compound is unfilled because mineral fillers raise the coefficient of linear thermal expansion mismatch between socket and pipe. Injection moulding of fittings uses melt temperature 200–230 °C, mould temperature 40–60 °C, and holding pressure 40–70 MPa; pipe extrusion uses a single-screw extruder with L/D 24:1–30:1, screen pack 40/60/100 mesh, and vacuum calibration at -0.03 to -0.06 MPa to maintain socket roundness within 0.2 mm across diameter. When ambient relative humidity exceeds 60%, the resin is predried at 80 °C for 2 h to suppress splay in the socket base.

    Performance in corrosive chemical drainage service is governed by ASTM D2661-21 for ABS DWV pipe and fittings, ISO 15493:2003 for industrial plastic piping systems, ASTM D3965 for dimensions and workmanship, and ASTM D2855 for solvent-cemented joint practice. Joint failure on production lines is most often traced to socket cement application thickness below 0.5 mm or an assembly temperature below 5 °C; once the joint is fused, the limiting service condition is the solvent cement's chemical resistance to oxidising acids rather than the base resin. Terminal products include DWV pipe and fittings, trap bodies, laboratory waste manifolds, neutralisation tank connections, and industrial drain covers.

    For high-gloss monitor and keyboard housing production, ABS PL-A09 is used without mineral fillers to preserve specular gloss after textured cavity detail; the formulation includes PL-A09 at 100 phr, black carbon masterbatch at 0.3–0.8 phr, hindered phenol antioxidant at 0.2–0.4 phr, and phosphite costabilizer at 0.1–0.2 phr. The compound is injection moulded in high-gloss steel cavities with mould temperature 55–70 °C; melt temperature is held at 230–250 °C, fill time 1.2–2.0 s, holding pressure 60–80 MPa, and cooling time 12–18 s for 2-cavity monitor bezel tools. Parting line flash and sink marks are controlled by gate design at the inner edge of the bezel; optical inspection uses ISO 2813 20° gloss readings above 90 GU and ISO 4287 surface roughness below 0.1 µm Ra.

    Regulatory compliance for consumer electronics housings includes IEC 62368-1:2023 for fire enclosure and electrical insulation, UL 94 HB at 1.5 mm for non-load-bearing external enclosures, RoHS 2011/65/EU and REACH SVHC candidate-list screening. Published data for this exact PL-A09 grade under prolonged UV exposure is limited; production validation typically uses ISO 4892-2 accelerated weathering rather than relying on resin datasheet figures. Terminal finished products include LCD monitor rear housings and bezels, keyboard top frames, mouse shells, calculator covers, and point-of-sale display housings.

    Creep Rupture Boundaries in ABS PL-A09 Appliance Housing Rib Structures

    Rib structures in washing machine consoles and vacuum cleaner bodies moulded from ABS PL-A09 are loaded by screw bosses and snap-fit features at service temperatures that can reach 60–70 °C near motors and drying ducts. The formulation for these structural housings sets ABS PL-A09 at 94–98 wt%, styrene-butadiene block copolymer toughener at 2–6 wt%, internal release agent at 0.2–0.4 phr, and carbon black masterbatch at 0.5–1.0 phr for UV screening in exposed panel surfaces. Injection moulding uses textured cavity surfaces with melt temperature 220–245 °C, mould temperature 45–65 °C, screw back pressure 0.8–1.5 MPa, and screw speed 80–120 rpm; rib thickness is limited to 60% of nominal wall thickness to prevent sink and to maintain cycle time below 45 s. Creep resistance is characterised by ISO 899-2 flexural creep testing, and production quality control uses ISO 527-2 tensile properties and ISO 179-1/1eA impact; a sudden drop in elongation at break below 5% usually indicates inadequate drying or recycled material ratio above 20%.

    Compliance for household appliance structural frames is assessed against IEC 60335-1:2020 for safety of household and similar electrical appliances, EN 60335-1 for the European market, UL 94 HB for unenclosed panels, and RoHS 2011/65/EU for restricted substances. Terminal components produced from this application line include washing machine control consoles, vacuum cleaner body halves, refrigerator door end caps, air conditioner front panels, and portable fan housings; each terminal type requires separate rib and boss validation because creep rupture in an ABS PL-A09 boss is governed by hoop stress concentration, not by average cross-sectional stress.

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    Certification & Compliance
    More Introduction

    Dongguan Pule Plastic ABS PL-A09 is an unfilled acrylonitrile-butadiene-styrene injection-molding grade supplied in pellet form for reciprocating-screw machines and selected extrusion applications. The model designation PL-A09 is printed on certificate-of-analysis documents, lot labels, and color-match records. Published datasheet values for this exact formulation are limited; the following technical characterization therefore presents the typical specification envelope for the medium-flow ABS grade class to which PL-A09 is assigned, and it should be verified against the batch certificate before tool trials or production qualification. The resin is supplied in natural and black color-match variants, normally in 25 kg multi-wall bags or bulk octabins. The polymer morphology consists of a styrene-acrylonitrile continuous phase with dispersed polybutadiene-grafted particles; the manufacturer does not currently publish rubber particle size distribution or graft ratio for PL-A09.

    Storage should be maintained below 30°C in a dry area protected from ultraviolet exposure. If a liner is opened and not fully consumed, the remaining pellets should be resealed and dried before the next molding run. Under correct storage conditions, unopened ABS generally retains processability for 24 months from the certificate date, although pre-colored variants may show minor yellowness index drift after prolonged storage.

    What Is the Processing Window for PL-A09 in Reciprocating-Screw Injection Molding?

    Under ISO 1133-1:2022 at 220°C with a 10 kg load, the melt flow rate of PL-A09 falls within the 18–26 g/10 min range. This places the product in the medium-flow ABS segment, distinct from low-flow extrusion ABS grades that typically test at 8–12 g/10 min and from many heat-resistant ABS grades that test at 10–18 g/10 min under the same conditions. The recommended nozzle melt temperature is 220–240°C. Barrel temperatures should follow a rising profile from rear to front: 190–210°C, 210–230°C, 220–240°C, with the nozzle maintained at 215–235°C. Mold surface temperature should be controlled between 40°C and 70°C; lower settings shorten cooling time but increase the probability of flow-line visibility, jetting, and reduced knit-line strength.

    Hydraulic back pressure should be limited to 0.3–1.0 MPa. Screw speed on a 22:1 L/D general-purpose screw with compression ratio of 2.2:1 to 2.6:1 should be held at 40–80 rpm. Decompression of 2–5 mm reduces nozzle drool without introducing excessive air entrapment. Melt residence time should not exceed 8 min at melt temperatures above 230°C; at barrel temperatures approaching 250°C, degradation of the polybutadiene phase generates volatile by-products that produce splay, yellowing, and impact loss. Machines should be purged with crystal polystyrene or styrene-acrylonitrile copolymer at 200°C before shutdown.

    The apparent shear viscosity of medium-flow ABS is pseudoplastic. Typical capillary rheometry values for the grade class are approximately 400–600 Pa·s at 240°C and 100 s⁻¹, falling to 80–150 Pa·s at 1000 s⁻¹. These values are indicative only and should not replace batch-specific rheology testing. For hot-runner molds, manifold temperature should be maintained at 230–240°C, and valve-gate or open-pipe drops should use tip diameters of 0.8–1.2 mm. Vent depth at the parting line should not exceed 0.03 mm to prevent flash while allowing volatile escape. Polished cavity surfaces with roughness below 0.05 µm Ra improve surface finish but require adequate draft angles to avoid ejection marks.

    Comparative Property Profile Against General-Purpose and High-Heat ABS Grades

    Table 1 compares PL-A09 with two adjacent ABS categories: a standard low-flow general-purpose grade and a heat-resistant copolymer grade. The values are representative of the grade class, not production lot limits. Lot-to-lot shifts in polybutadiene content and molecular mass distribution may alter Charpy notched impact by ±4 kJ/m² and melt flow rate by ±3 g/10 min.

    Property Test standard PL-A09 Standard low-flow ABS High-heat ABS
    Density ISO 1183-1 1.04–1.06 g/cm³ 1.03–1.06 g/cm³ 1.05–1.07 g/cm³
    Melt flow rate, 220°C/10 kg ISO 1133-1:2022 18–26 g/10 min 8–12 g/10 min 10–18 g/10 min
    Tensile yield stress ISO 527-2/1A/50 39–45 MPa 38–46 MPa 42–48 MPa
    Flexural modulus ISO 178 2100–2400 MPa 1900–2300 MPa 2300–2600 MPa
    Charpy notched impact, 23°C ISO 179-1/1eA 18–28 kJ/m² 20–35 kJ/m² 12–20 kJ/m²
    Heat deflection temperature, 1.8 MPa ISO 75-2/A 94–99°C 92–97°C 102–108°C
    Vicat softening temperature, B50 ISO 306 98–104°C 96–102°C 106–112°C
    Mold shrinkage ISO 294-4 0.4–0.7% 0.4–0.7% 0.3–0.6%
    Flame rating, 3.0 mm UL 94 HB HB HB

    The differentiation between PL-A09 and low-flow ABS is primarily rheological. At the same melt temperature, PL-A09 fills a 1.2 mm wall section with lower cavity pressure; however, the higher melt flow rate derives from lower average molecular weight or modified molecular architecture, which reduces the Charpy notched impact plateau by 5–10 kJ/m² relative to high-impact extrusion ABS. Heat-resistant ABS grades typically use α-methylstyrene comonomer, raising heat deflection temperature by 8–12°C but requiring melt temperatures at or above 250°C and producing greater residual stress in thick sections. PL-A09 is therefore unsuitable where continuous service temperature exceeds approximately 65°C under structural load or where UL 94 V-0 flammability classification is required in an unfilled compound.

    In appliance control housings, switch faceplates, power tool shells, and structural brackets, PL-A09 is specified when wall thickness is kept above 1.5 mm and the part is not exposed to continuous load above 65°C. On a 160-tonne hydraulic injection molding machine with a 22:1 L/D barrier screw and 2.5:1 compression ratio, shot size should be maintained between 25% and 75% of barrel capacity. Cavity pressure transducers are recommended, with peak cavity pressure held between 35 MPa and 50 MPa. Clamp force should be derived from projected area and cavity pressure; a 350 cm² housing using 40 MPa cavity pressure requires 140 tonnes of clamp force excluding safety factors. Edge-gate land length should be 0.5–1.0 mm, and gate depth should be 60–80% of the part wall thickness. Weld lines should be positioned away from tensile stress concentrations because weld-line tensile strength in unfilled ABS is typically 60–75% of the parent material tensile strength, depending on melt temperature and hold pressure.

    For snap-fit closures, maximum outer-fiber strain should be held below 1.5% at 23°C and below 0.7% at -10°C to avoid stress whitening. Screw boss outer diameters should be configured at 2.0–2.4 times the thread-forming screw outer diameter. Ultrasonic welding of PL-A09 is feasible with a shear joint interference of 0.2–0.3 mm and amplitude of 20–40 µm at 20 kHz; weld strength is sensitive to residual moisture, so parts should be molded from material dried below 0.02 wt%. Solvent bonding with methyl ethyl ketone or cyclohexanone can cause stress cracking in stressed sections; fixturing and low-molding-stress part design are therefore mandatory when solvent assembly is specified.

    When PL-A09 Is Selected Instead of a Low-Flow Extrusion ABS in Thin-Wall Electronic Housings

    If an existing mold was sampled with a low-flow extrusion ABS having a melt flow rate below 10 g/10 min, substitution with PL-A09 usually lowers fill pressure and permits reduced melt temperature, which can help avoid burning in hot-runner drops. A cavity pressure reduction of 15–25% is common for similar melt-flow differentials in thin-wall electronic enclosures with 1.2 mm nominal wall thickness; published data for this specific configuration is limited, so mold trials with cavity pressure transducers are required. Hold-pressure time may need to be extended by 0.5–1.0 s because the higher-flow grade freezes the gate sooner. Low-temperature impact behavior is lower than that of high-impact extrusion ABS; snap-fits, screw bosses, and hinge anchors should therefore be tested at 0°C and -20°C.

    Mold shrinkage difference between the two grades is usually below 0.1 percentage point, but dimensions should be re-confirmed 24 h after ejection because amorphous ABS shrinkage continues after demolding. If hot-runner balance is marginal, the lower viscosity of PL-A09 may improve filling of the furthest cavity but can also increase overpacking of the first-filled cavity; therefore, multi-cavity tools should be instrumented with pressure sensors and individual gate adjustments.

    Drying and Moisture-Related Defect Thresholds Determine Acceptable Production Rates

    ABS is hygroscopic. At 23°C and 50% relative humidity, equilibrium moisture absorption is approximately 0.2–0.4 wt%. For PL-A09, residual moisture above 0.03–0.05 wt% produces splay, silver streaks, surface haze, and reduced weld-line integrity. The resin should be dried in a desiccant dryer with airflow not less than 3.7 m³/h per kg/h of material consumption and a dew point of -40°C or lower. Drying at 80–90°C for 2–4 h reduces moisture to below 0.02 wt% when measured by ISO 15512. If ambient relative humidity exceeds 60%, virgin pellets and regrind should be conveyed to the machine throat with dry air, and the machine hopper should not remain open for extended periods.

    Prolonged drying above 95°C can oxidize the polybutadiene phase and darken natural resin. If a batch has been exposed to high humidity for more than 8 h, drying time should be extended to 4–6 h. The material should not be mixed with polycarbonate, polyamide, PVC, or acetal regrind because incompatible phases and acidic degradation products can reduce impact and cause delamination. Use of in-plant regrind for visible surfaces is generally limited to 20% of total shot weight; higher levels may increase black specks, gloss variation, and flow-length variability.

    For global material acceptance, PL-A09 must be evaluated under the following regulatory framework. The status column represents the unfilled natural grade classification; final certification requires supplier declaration for the production lot and destination market.

    Regulatory area Requirement or method Status for PL-A09
    RoHS 2011/65/EU with (EU) 2015/863 Pb 0.1 wt% max, Cd 0.01 wt% max, Cr(VI) 0.1 wt% max, PBB/PBDE 0.1 wt% max, each phthalate 0.1 wt% max Supplier declaration required; unfilled natural ABS typically conforms
    REACH SVHC candidate list Concentration below 0.1 wt% in the article No SVHC intentionally added; supplier declaration required
    UL 94 Burning test at 3.0 mm HB for unfilled grade; V-0 not available without flame-retardant additive
    FDA 21 CFR 177.1020 ABS polymer migration testing for food-contact use Not marketed as food-contact grade; no manufacturer-specific migration data for PL-A09
    Chemical resistance Immersion and stress-cracking testing Limited resistance to ketones, esters, aromatic solvents, and chlorinated solvents; susceptible to environmental stress cracking under strain with methanol and certain plasticizers

    The absence of a published datasheet for this exact formulation means any property value used for tooling, process development, or regulatory decisions should be confirmed with Dongguan Pule Plastic technical documentation. Processing boundaries, lot-specific flow values, and colorant effects on mechanical performance may fall outside the ranges shown above.

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