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Carbon Printers MPU 100 Multi-purpose Polyurethane

    • Название продукта: Carbon Printers MPU 100 Multi-purpose Polyurethane
    • Сайт Factroy: Округ Юду, Ганьчжоу, Цзянси, Китай
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    • Производитель: Ascent Petrochem Holdings Co., Limited
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    Код ТН ВЭД 477411

    Как аккредитованная многоцелевая фабрика по полиуретану для углеродных принтеров MPU 100, мы соблюдаем строгие протоколы качества - каждая партия подвергается строгим испытаниям для обеспечения последовательных стандартов эффективности и безопасности.

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    Применение углеродных принтеров MPU 100 многоцелевой полиуретан

    In retort-pouch laminating ink systems for polyethylene terephthalate, nylon, and aluminium foil webs, Carbon Printers MPU 100 Multi-purpose Polyurethane is incorporated as a 15–22 wt% fraction of total liquid ink weight, typically pre-dissolved to 35–40% solids in a solvent blend of ethyl acetate, isopropyl acetate, and n-propanol. The addition range is not arbitrary: below 15 wt% the post-lamination bond strength on low-slip polyethylene frequently drops below 1.5 N/15 mm, while above 22 wt% the ink viscosity rises beyond 18–22 s Zahn #3 and requires additional retarder solvent, complicating residual solvent compliance under EU Regulation 10/2011, US FDA 21 CFR 175.300, and Swiss Ordinance SR 817.023.21. The production process for this grade in gravure laminating ink begins with pigment dispersion in a horizontal bead mill charged with 0.6–0.8 mm zirconia beads at 8–12 m/s tip speed and a chamber outlet temperature held below 45 °C to prevent shear-induced molecular weight loss in the polyurethane chain. The letdown phase adds MPU 100 solution, nitrocellulose, and wax under a high-speed disperser at 1200–1500 rpm for 20–30 min; final ink is applied through a gravure cylinder with 60–70 l/cm screen ruling and 28–35 µm cell depth at 180–250 m/min line speed, then dried in a three-zone oven at 60–90 °C. The terminal printed webs are laminated to low-density polyethylene or cast polypropylene as retort pouches, stand-up pouches, vacuum pack films, and pharmaceutical lidding laminates. Operational limits include a required ink-room relative humidity below 60% to prevent moisture uptake that accelerates viscosity drift and a prohibition against high-acid pigments that catalyze premature crosslinking of free isocyanate-reactive sites on the polyurethane backbone. ASTM F904 is the standard peel test method for the finished laminate structure.

    Why Does MPU 100 Raise Block Resistance in Two-Component Wood Topcoats Without Sacrificing Flexibility?

    Block resistance in solventborne wood topcoats is governed by the cured film glass transition temperature, surface polarity, and the amount of unreacted hydroxyl left after crosslinking. In formulations using Carbon Printers MPU 100 Multi-purpose Polyurethane, the resin is added at 70–80 wt% of total binder solids, with an aliphatic polyisocyanate hardener at 20–30 parts per 100 parts resin solids and an NCO:OH ratio of 1.1:1. At this ratio the dry film pendulum hardness measured under ASTM D4366 remains in the 90–120 s König range, while DIN 68861-1B chemical resistance against ethanol and coffee is maintained without film cracking. Compliance for the applied topcoat includes the EU Decopaint Directive 2004/42/EC Annex IIA category D limit for solventborne wood coatings and DIN EN 927-1 classification for exterior wood coating systems. Production-scale application uses a gravity-feed HVLP spray gun with a 1.2–1.4 mm nozzle and 2.0–2.5 bar atomizing air pressure; the coating is reduced to 35–45% solids and applied in two wet layers of 80–120 µm each. Between coats, the first film is sanded with P320 paper after 4–6 h at 25 °C. The second coat is force-dried at 40–60 °C for 4–6 h, with full property development after 7 days at 25 °C. Terminal finished products include kitchen cabinet frontals, solid wood desktops, veneer-faced furniture panels, and interior millwork. The operational boundary is the pot life of the mixed product, which is 4–6 h at 25 °C; addition of amine-based accelerators to shorten cure is incompatible because it reacts preferentially with the isocyanate and produces carbon dioxide bubbles.

    Although synthetic leather basecoat manufacturing is often associated with aromatic one-component polyurethane solutions diluted in dimethylformamide, Carbon Printers MPU 100 Multi-purpose Polyurethane can be used as the primary resin in transfer coating and wet coagulation processes at 100 parts resin solids, 40–80 phr of DMF or a DMF/methyl ethyl ketone mixture, 10–20 phr micronized calcium carbonate, 3–8 phr pigment paste, and 0.5–1.0 phr deaerator. The compound is mixed under a planetary mixer at 20–30 rpm for 30–45 min under vacuum of -0.08 MPa to reduce air entrapment, then discharged through a 0.25 mm filter. Coating is performed on a knife-over-roll coater with a knife gap of 0.15–0.25 mm onto coated release paper or nonwoven backing at 8–15 m/min. The wet film enters a coagulation bath containing 15–25% DMF in water at 25–40 °C; phase inversion forms a microporous structure that determines hand feel and peel adhesion. Countercurrent washing then reduces residual DMF below 0.1% before the web is dried at 90–130 °C in a four-zone stenter. Compliance checks include REACH Annex XVII restrictions on restricted solvents and aromatic amines, OEKO-TEX Standard 100 Class II or III limits for skin-contact leather substitutes, ISO 3376 for tensile strength, and ISO 11644 for coating adhesion. Terminal finished product types include automotive seat cover stock, shoe upper material, handbag body stock, and contract furniture upholstery. The process is sensitive to bath DMF concentration: if bath DMF exceeds 25%, surface pores close and produce a glossy, low-breathability skin; if bath DMF drops below 15%, the coagulated layer may delaminate during transfer stripping.

    Adhesive Film Formation and Heat Reactivation on Footwear Sidewalls

    When Carbon Printers MPU 100 Multi-purpose Polyurethane is compounded as a 18–25 wt% solids constituent in a two-component polyurethane footwear adhesive, the product contributes to green strength after solvent flash-off and to peel strength after isocyanate crosslinking. The recommended addition ratio is 100 parts MPU 100 solution, 5–8 phr aliphatic polyisocyanate crosslinker, 50–70 phr solvent blend of methyl ethyl ketone, acetone, and ethyl acetate, and 0.5–1.0 phr of a fumed silica thixotrope. Viscosity at 25 °C is controlled to 3500–5000 mPa·s; pot life after crosslinker addition is 2–4 h. The adhesive is applied by 0.15–0.25 mm roller coater or air-assisted spray to cleaned and primed sidewall surfaces, dried in a forced-air tunnel at 60–80 °C for 8–12 min, and reactivated with infrared surface temperatures of 90–100 °C immediately before assembly. Pressing is performed at 0.5–0.8 MPa for 30–60 s; bond strength after 24 h cure at 25 °C is measured under ISO 11343 impact peel and ASTM D6862 90° peel. Compliance includes REACH restrictions on solvent classification and DIN EN 1392 for footwear adhesive performance. Terminal products include formal leather shoes, safety footwear with rubber outsole bonding, athletic shoe midsole-to-upper assemblies, and board-lasted constructions. The main processing boundary is moisture ingress: if relative humidity exceeds 65% during application, moisture reacts with the isocyanate and generates carbon dioxide at the bond line, reducing peel strength by up to 15% under ASTM D6862 comparisons.

    Where low-gloss, high-flex textile coatings are required on knit automotive seating and technical outerwear, Carbon Printers MPU 100 Multi-purpose Polyurethane is formulated as the base resin in a direct coating compound at 100 parts resin solids, 3–7 phr blocked isocyanate or aliphatic polyisocyanate crosslinker, 2–5 phr fumed silica matting agent, 0.5–1.0 phr leveling agent, and a solvent blend of ethyl acetate and toluene adjusted to a final viscosity of 20–30 Pa·s at 25 °C. The compound is coated on a knife-over-roll or reverse-roll coater at 80–120 µm wet film thickness onto polyester or nylon knit that has been heat-set at 180–190 °C. The web is dried in a stenter at 120–150 °C for 90–180 s, followed by matte finish calendering at 80–100 °C and 0.4 MPa nip pressure when a film-to-textile lamination is specified. Compliance testing for automotive interior specifications includes FMVSS 302 flammability, ISO 105-B02 lightfastness of ≥ 500 h at 80 °C, and ISO 12947-1 Martindale abrasion of ≥ 50,000 cycles depending on the OEM specification. Terminal finished product types include seat bolster cover stock, door panel insert fabric, motorcycle protective apparel, and cold-weather outerwear panels. The principal processing conflict occurs when low-cure blocked isocyanates are replaced by more reactive aliphatic polyisocyanates: cure temperature drops to 100–120 °C, but pot life shortens to 4–8 h and the compound must be used within one shift. Residual isocyanate and solvent content on coated textiles must also be evaluated under ISO 17226 for formaldehyde-free textile testing and REACH Annex XVII for restricted substances.

    When MPU 100 Is Utilized as an Adhesion Modifier in Solvent-Based Laminating Adhesives for Aluminium-Foil Structures

    Solvent-based laminating adhesives for aluminium-foil structures require a narrow balance between metal affinity, film clarity after lamination, and resistance to aggressive filling temperatures. In such systems, Carbon Printers MPU 100 Multi-purpose Polyurethane is added at 10–20 wt% of total adhesive solids as a compatibility bridge between the high-molecular-weight polyester polyol and the aliphatic polyisocyanate hardener; the hardener is dosed at 5–8 parts per 100 parts of total polyol solids, giving a final mix ratio of 100:5 to 100:8 by weight. The adhesive is diluted to 30–40% solids with ethyl acetate, and applied with a 80–120 l/cm gravure cylinder at 2.5–4.0 g/m² dry coat weight. The laminate passes through a three-zone oven at 60–90 °C, followed by a heated nip at 60–80 °C and 0.3–0.5 MPa to bond the foil web to the polypropylene or polyethylene sealant layer. Full bond strength develops after 48–96 h at 40–50 °C, with peel strength measured under ASTM D1876 typically in the 3–6 N/15 mm range on foil-to-polyethylene structures. Compliance for food-contact laminates includes EU Regulation 10/2011 overall migration limits, US FDA 21 CFR 177.1395 for laminated films and adhesives, and Swiss Ordinance SR 817.023.21 for printing inks and coatings in food contact. Terminal finished products include retort pouches, stand-up pouches for ready-to-eat food, pharmaceutical lidding foil, and condiment sachets. The operational incompatibility is with high-amine slip additives in the sealant resin: free amines migrate to the adhesive interface during steam retorting at 121 °C and inhibit the NCO-terminated crosslinking reaction, causing tunneling delamination in the finished pouch.

    Application scenarioStandard or methodControlled or measured parameter
    Laminating ink for retort packagingEU 10/2011, FDA 21 CFR 175.300, SR 817.023.21, ASTM F904Migration limit, residual solvent, bond strength
    Two-component wood topcoat2004/42/EC, DIN EN 927-1, ASTM D4366, DIN 68861-1BVOC content, pendulum hardness, chemical resistance
    Synthetic leather basecoatREACH Annex XVII, OEKO-TEX Standard 100, ISO 3376, ISO 11644Restricted substances, tensile strength, coating adhesion
    Footwear structural adhesiveISO 11343, ASTM D6862, DIN EN 1392, REACHImpact peel, 90° peel, adhesive performance
    Textile coating for automotive interiorFMVSS 302, ISO 105-B02, ISO 12947-1, ISO 17226Flammability, lightfastness, abrasion, textile chemistry
    Solvent-based foil lamination adhesiveEU 10/2011, FDA 21 CFR 177.1395, SR 817.023.21, ASTM D1876Overall migration, adhesive migration, peel strength
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    Более подробное введение

    Carbon Printers MPU 100 Multi-purpose Polyurethane is a light-processable polyurethane resin formulated for digital light synthesis platforms in the Carbon printer family. The product is supplied as a one-part photopolymerizable liquid that requires a forced-convection thermal post-cure to complete the secondary urethane network. Cured parts exhibit a nominal indentation hardness of 100 Shore A when measured to ASTM D2240-15 after the manufacturer’s recommended schedule. The material position in the portfolio is intermediate: it is not a high-elongation elastomer such as EPU 40 or FPU 50, nor a rigid structural polyurethane such as RPU 70 or RPU 130. Its primary usage includes gaskets, seals, cable strain relief, protective covers, vibration isolators, tooling fixtures, and low-pressure wear components in which cut resistance, elastic recovery, and impact absorption are required. Because open-source published data for the MPU 100-specific configuration is limited, numerical values in this document should be treated as product-family references and confirmed against the current supplier certificate of analysis before production release.

    What Distinguishes MPU 100 from EPU 40, FPU 50, and RPU 70 in the Carbon Polyurethane Series?

    MPU 100 occupies a modulus-hardness intersection that separates it from both elastomeric and rigid polyurethane grades. EPU 40 and FPU 50 are specified for high elongation and soft-surface gasketing, but they have lower cut-propagation resistance and lower surface hardness. RPU 70 and RPU 130 are specified for structural rigidity and higher heat deflection, but they have lower elongation at break and less damping. MPU 100 is therefore selected when a component must survive snap-fit insertion, retaining-ring seating, or particulate contact while remaining compliant enough to avoid cracking a mating polymer or lacquered surface. For objective comparison, the following test methods apply: ASTM D638-14 or ISO 527-2:2012 for tensile stress-strain, ASTM D624-20 Die C for tear strength, ASTM D395-18 Method B for compression set, ASTM D2240-15 for durometer hardness, and DIN 53512 for rebound resilience. Direct substitution from cast or millable polyurethane is not recommended without testing digital light synthesis coupons in the same build orientation because the dual-cure network contains acrylate-derived segments that alter elongation and tear relative to a cast polyurethane of the same Shore A hardness.

    Uncured viscosity at 25 °C is shear-thinning. Low-shear viscosity controls puddle stability after the blade pass, while high-shear viscosity controls flux under the recoat blade. A lot-to-lot shift of ±10% in low-shear viscosity can alter green-state thickness by several micrometers if the machine’s closed-loop recoat force is not calibrated. Cartridges and bottles should be equilibrated at 23 ± 2 °C for 8 h before printing. The build chamber should be maintained at 30% to 50% RH. The recoat blade gap is machine-specific; typical digital light synthesis platforms for polyurethane resins operate with a gap between 100 µm and 250 µm. Exposure dose for a 100 µm slice is set by the working curve and should only be adjusted after measuring cure depth on a calibration staircase. At the 405 nm print wavelength, a dose deviation of ±5% changes cure depth sufficiently to affect channel features finer than 1 mm. Excessive dose produces over-cure in negative features, while insufficient dose produces green-state delamination. Printed parts should be rinsed in an approved solvent such as propylene glycol methyl ether acetate or the manufacturer’s specified rinse; solvent dwell above 5 min can soften thin walls. Residual solvent should be removed with low-velocity dry air before thermal post-cure. The oxygen-permeable build window maintains an inhibition layer; the printer’s oxygen setpoint should not be altered from the manufacturer’s resin-specific profile because a lower oxygen concentration increases through-cure and can bond the part to the window.

    When Ambient Relative Humidity Exceeds 60% During Open-Bath Printing or Cartridge Storage

    Moisture ingress is a process risk for MPU 100 because the polyurethane oligomer can react with atmospheric water before photopolymerization. The resulting hydrolysis and chain extension increase the gel point, raise resin viscosity, and can produce surface vesicles or interlayer delamination. In a production enclosure maintained at 20% to 40% RH, the interval between cartridge opening and printing should not exceed 4 h unless the system is purged with dry nitrogen. If the build basin remains idle for more than 8 h, the first build after restart should include an adhesion coupon at the outer corners of the platform. Vacuum drying of the uncured resin is not recommended; removal of low-molecular-weight volatiles changes viscosity and can invalidate the printer’s exposure parameters. For long-term storage, sealed cartridges should be kept at 15 °C to 30 °C, protected from light below 420 nm. Any lot that has been exposed to condensation or visibly increased haze should not be returned to the machine without rheological comparison to a retained reference.

    Verification Matrix for Incoming Resin Lots

    Before a new lot is released to production, the following minimum property envelope is checked against the supplier certificate of analysis. The matrix is not a full validation protocol; it is the incoming inspection gate for typical non-porous components with wall thickness below 3 mm.

    PropertyTest standardConditionAcceptance basis
    Viscosity at 25 °CASTM D2196-20rotational rheometer, 10 s⁻¹supplier certificate of analysis ± 10%
    DensityISO 1183-1:201923 °Csupplier certificate of analysis ± 0.02 g/cm³
    Shore A hardnessASTM D2240-1515 s dwell, cured coupon100 Shore A nominal ± 3 points
    Tensile strengthASTM D638-14 / ISO 527-2:201250 mm/minlower bound from finite-element analysis
    Elongation at breakASTM D638-14 / ISO 37:201750 mm/minlower bound from part flexure requirement
    Tear strengthASTM D624-20 Die C500 mm/minlower bound from cut-growth analysis
    Compression setASTM D395-18 Method B22 h at 70 °Csupplier reference ± 5% absolute

    Dynamic mechanical analysis of MPU 100 after full post-cure typically shows a glass transition temperature below 0 °C. At 23 °C, the material is in the rubbery plateau, and storage modulus should be measured using ISO 6721-1:2019 in tensile mode with a frequency sweep from 1 Hz to 10 Hz. Loss tangent at small strain is not a sufficient predictor of full-scale vibration isolation because polyurethane damping is amplitude-dependent. If the component is used for repeated compression, thickness recovery should be checked after 100,000 cycles at 10 Hz with a displacement limit of 20% of the original thickness. Published data for MPU 100 under these specific dynamic conditions is limited; endurance testing remains application-specific. Continuous service above 80 °C is not recommended because compression set becomes process-significant, and short excursions to 100 °C for 1 h should be validated on the actual part geometry.

    Thermal Post-Cure Is a Two-Stage Isothermal Crosslinking Process

    The green-state modulus of MPU 100 after printing and rinsing is below the final cured modulus because the secondary urethane network is incomplete. The thermal post-cure step in a forced-convection oven should be controlled by air temperature and part internal temperature, not only by the setpoint. A representative qualification profile for dual-cure polyurethane systems consists of ramp to 80 °C, hold for 2 h, ramp to 120 °C, hold for 6 h, and cool to 35 °C before support removal. The exact schedule for MPU 100 should be taken from the current supplier datasheet. For wall thickness above 10 mm, embedded thermocouples are required during process development because the exothermic urethane reaction can create a transient core temperature above the oven setpoint. Under-cured lots show increased compression set after 22 h at 70 °C; over-cure above 130 °C causes yellowing and reduces elongation at break without a corresponding rise in tensile strength. The reaction follows diffusion-limited isothermal kinetics at high conversion, and the final 20% conversion may require a hold at 120 °C because vitrification slows chain mobility. Post-cure ovens should be calibrated to ± 3 °C uniformity according to AMS 2750F or an equivalent internal procedure. Linear shrinkage during thermal post-cure is not uniform; typical dual-cure polyurethane systems can exhibit 0.3% to 1.5% linear shrinkage depending on wall thickness and build orientation. Scale-factor compensation should be derived from a three-dimensional fiducial artifact measured before and after cure.

    Chemical resistance of MPU 100 should not be extrapolated from cast polyurethane specifications. The dual-cure network contains acrylate-derived segments from the photopolymerization step, which modify solvent diffusion relative to a cast polyurethane of the same Shore A hardness. For water and non-ionic detergent solutions, the material is suitable at temperatures below 50 °C. For hydrocarbon oils, esters, and ketones, immersion testing per ISO 1817:2015 is required before production use. Exposure to methyl ethyl ketone at 23 °C for 24 h can produce dimensional change exceeding 10% and surface tack. Alcohol rinses should not be used as the final cleaning stage because retained alcohol plasticizes the surface and lowers abrasion resistance. Amine-based additives, strong bases, and tin-based polyurethane catalysts must not be mixed into the uncured resin; premature crosslinking and measurable exothermic viscosity rise can occur within 30 min. If a lot shows color shift, surface tack, or viscosity spiking during handling, the resin should be quarantined and sampled for Fourier-transform infrared analysis against a retained reference. Migration of unreacted low-molecular-weight species can be detected by gas chromatography-mass spectrometry after solvent extraction; the cure index should be verified by measuring residual isocyanate via titration or FTIR. For food-contact or medical-skin-contact uses, migration testing and biocompatibility testing per ISO 10993-5 are required; no compliance should be inferred from general polyurethane chemistry.

    With 100 Shore A Hardness, Support-Removal Geometry Becomes a Fatigue Initiation Variable

    Support removal from MPU 100 printed parts requires lower peel force than rigid polyurethane grades, but over-cured supports can leave surface scars that become crack initiation sites under cyclic loading. For components subject to bending or compression, the build orientation should place the highest principal tensile stress parallel to the printed layers, not across them. Layer-to-layer adhesion in the green state should be confirmed using a knife-adhesion test on the first article. Support contact points should be located on non-functional surfaces and kept below 3 mm diameter. After support removal, light sanding or tumbling should be validated for dimensional change; abrasive finishing can reduce surface roughness from Ra 6 µm to Ra 1 µm but may alter the effective hardness of thin skins. If a part is exposed to cyclic bending, the orientation should avoid placing support contact marks in the tensile fillet radius. This is particularly relevant for snap-fit arms because the strain concentration at the root can exceed the nominal strain by a factor of 3 when the fillet radius is below 0.5 mm.

    Production-scale digital light synthesis cells using MPU 100 should implement a first-part inspection plan that includes dimensional scan, durometer reading, and tear-coupon testing from each lot. Because dual-cure polyurethane lots can vary in oligomer molecular weight, the build parameter set should be re-qualified when the supplier changes lot manufacturing date or when the printer projection lamp output drifts more than 10% from the baseline radiometer reading. The product is not a food-contact grade; any FDA 21 CFR 177.1680 or EU 10/2011 compliance claim must be supported by migration testing on the cured part. Supplier documentation should include REACH SVHC statements and RoHS 2011/65/EU status for the cured polymer; liquid resin components are not identical to cured part composition.

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