1-Cyclohexyl-1H-Pyrrole-2,5-Dione

1-Cyclohexyl-1H-Pyrrole-2,5-Dione


    • Product Name 1-Cyclohexyl-1H-Pyrrole-2,5-Dione
    • Alias N-Cyclohexylmaleimide
    • Einecs 259-856-4
    • Mininmum Order 1g
    • Factory Site West Ujimqin Banner, Xilingol League, Inner Mongolia, China
    • Price Inquiry sales9@bouling-chem.com
    • Manufacturer Bouling Chemical Co., Limited
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    Specifications

    HS Code

    174944

    Chemical Formula C10H13NO2
    Molecular Weight 179.216 g/mol
    Appearance Solid
    Solubility In Water Low solubility
    Solubility In Organic Solvents Soluble in common organic solvents
    Stability Stable under normal conditions

    As an accredited 1-Cyclohexyl-1H-Pyrrole-2,5-Dione factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 100g of 1 - Cyclohexyl - 1H - Pyrrole - 2,5 - Dione packaged in a sealed plastic bottle.
    Shipping 1 - Cyclohexyl - 1H - Pyrrole - 2,5 - Dione is shipped in properly sealed containers, following strict chemical transport regulations. Packaged to prevent spills and damage, transported via approved carriers ensuring safe and timely delivery.
    Storage 1 - Cyclohexyl - 1H - pyrrole - 2,5 - dione should be stored in a cool, dry place. Keep it away from heat sources, open flames, and direct sunlight to prevent decomposition. Store in a tightly - sealed container to avoid contact with air and moisture, which could potentially react with the chemical. Also, ensure it is segregated from incompatible substances.
    Application of 1-Cyclohexyl-1H-Pyrrole-2,5-Dione
    In the continuous mass polymerization of acrylonitrile-butadiene-styrene (ABS), substitution of a styrene fraction with 1-cyclohexyl-1H-pyrrole-2,5-dione (CHMI) at a monomer-stage addition level of 6–15 wt% of the total feedstock raises the glass transition temperature (Tg) of the styrene-acrylonitrile (SAN) matrix phase from 105 °C to a range of 118–128 °C (DSC, 10 K/min, second heat per ISO 11357-2:2020). The downstream process involving a 40 L/D co-rotating twin-screw extruder configured with a multi-stage devolatilization zone (–0.095 MPa vacuum, 260–275 °C melt temperature) strips residual cyclohexylmaleimide monomer to below 800 ppm, a threshold set by automotive interior VOC specifications. The rigid cyclic imide pendant group retards chain mobility without imparting the yellow tint observed with phenylmaleimide analogues; this maintains base colour coordinates of granulate within ΔE < 1.2 (CIE L*a*b* D65/10°). Formulated grades are employed in Class-B instrument panel carriers, centre console substructures, and A-pillar trim where heat sag resistance under 120 °C glass-sunload conditions is non-negotiable. Compliance rests on REACH registration of the monomeric substance and conformance to VDA 278:2011 for volatile emissions; if the finished article is destined for interior trim with incidental skin contact, migration of the monomer must fall within the specific migration limit framework of EU 10/2011 at the verification stage, though CHMI itself is not listed as a dual-use additive and its detection limit of 10 µg/dm² commonly serves as a surrogate pass criterion.

    What Drives the Optical Clarity Shift in Methyl Methacrylate–CHMI Copolymers?

    The reactivity ratio sequence rMMA0.8–1.1 and rCHMI0.3–0.5 in free-radical solution polymerization (toluene/MEK, 80 °C, AIBN initiator 0.3 mol%) produces a gradient copolymer architecture rather than a strictly alternating sequence, causing an incremental drop in percent transmittance once the CHMI feed fraction exceeds 18 mol% because microphase-separated domains with an electron-deficient imide aggregation appear at the 50–150 nm scale detectable by small-angle X-ray scattering. To retain > 89 % light transmission (3 mm thickness, ASTM D1003-21) while elevating the Vicat softening point from 102 °C to 131 °C (ISO 306:2022, Method B50), a semicontinuous monomer-starved dosage strategy is implemented: CHMI dissolved in MMA is fed over 4–6 h into a pre-polymerized seed latex (particle size 220 nm) using a redox couple—typically tert-butyl hydroperoxide/sodium formaldehyde sulfoxylate—maintained at 65 °C. Post-reaction steam stripping under 3 kPa absolute pressure yields bead copolymer with a residual volatile fraction under 450 ppm. The resulting moulding powder is calendered and milled into optical-grade sheet for automotive LED light-pipe covers requiring > 85 % luminous transmittance after 2,000 h xenon-arc weathering (ISO 4892-2:2013, cycle A). Regulatory adherence is dual-track: the copolymer is amenable to FDA 21 CFR § 177.1010 (acrylic polymers in food contact) provided extractable cyclohexylmaleimide monomer remains below the 50 ppb threshold quantified by HPLC-UV; simultaneously, electronic-grade batches must meet ion chromatography limits of ≤ 5 ppm chloride and ≤ 1 ppm sodium to satisfy photolithography substrate purity conventions.

    A distinct manufacturing sequence emerges when CHMI serves as a co-agent in peroxide-cured ethylene-propylene-diene terpolymer (EPDM) dense profiles. The imide functionality participates in a thermally triggered ene-addition across the pendant ethylidene norbornene unsaturation, bridging chains without the formation of polysulfidic links that deteriorate compression set after prolonged air aging at 150 °C. A typical interior mixing protocol (tangential internal mixer, ram pressure 0.6 MPa, dump temperature 120–125 °C) incorporates 1.5–3.0 phr CHMI together with a dialkyl peroxide (dicumyl peroxide at 2.0 phr) and a hydrotalcite acid scavenger. Cure rheometry (ASTM D5289-19a, moving-die rheometer, 180 °C arc 0.5°) registers a torque delta (MH – ML) enhancement of 17–22 dN·m compared with the sulfur-donor control, confirming a crosslink density structurally distinct from conventional vulcanizates. Extrusion of the formulated compound through a pin-barrel extruder (L/D 14:1, head pressure 12–16 MPa) yields closed-cell sponge and solid primary door seals tested against VW TL 52041 for static stiffness change under compression after 504 h at 100 °C. Because the co-agent itself is nitrogen-bearing, the National Fire Protection Association (NFPA 652) combustible dust hazard classification must be considered in powder handling, and local exhaust ventilation maintaining a minimum capture velocity of 0.5 m/s at the weigh-station is prescribed to keep airborne exposure below the manufacturer’s recommended 5 mg/m³ (respirable fraction).

    Accelerator-Free Cure Systems in EPDM Extrusion Profiles

    Where the elimination of zinc-containing accelerators is mandatory under the EU Ecolabel for rubber surfacing (Commission Decision 2014/69/EU), 1-cyclohexyl-1H-pyrrole-2,5-dione at 2.5 phr delivers a state of cure equivalent to a zinc oxide/tetramethylthiuram disulfide package while holding heavy-metal residue below the 5 ppm limit. Formulations discharged from an intermeshing reverse-rotation twin-screw continuous mixer are shaped through a gear pump to a flat die and microwave-heated (2,450 MHz, 4–6 kW power input) followed by a hot-air tunnel at 210–230 °C, achieving full cure in a 24 m line in under 1.5 min. Shore A hardness (ISO 48-4:2018) remains within ±3 points of the sulfur-cured reference, while the retention of elongation at break after immersion in IRM 903 oil for 70 h at 125 °C is > 72 %, confirming the imide crosslinks are resistant to basic hydrolysis conditions.

    Processing of rigid poly(vinyl chloride) profiles for high-Tg window frames exploits the radical-scavenging potential of the maleimide ring: CHMI is introduced not as a neat monomer but as a pre-formed imidized copolymer (CHMI-α-methylstyrene-acrylonitrile, typical composition 55/25/20 wt%) blended into a PVC dry blend at a loading of 12–18 phr. Fusion in a counter-rotating conical twin-screw extruder (screw diameter 54/110 mm, metering zone temp 185 °C) yields a heterogeneous morphology where the heat-distortion temperature (ISO 75-2:2013, Method Bf) climbs from 72 °C to 93 °C without the embrittlement typical of chlorinated PVC compositions. Ultrasonic weld-line integrity of the finished sash corner, tested according to ASTM F2157-09, shows a breaking torque exceeding 38 N·m because the molecular rigidity of the imide-rich dispersed phase suppresses chain slippage at the fusion interface. A factory-level durability campaign referencing EN 12608-1:2021 for unplasticised PVC profiles requires an additional window of rapid colorimetric change: the additive copolymer must not lift the yellow index by more than 2 units over 1,200 h in a QUV-B test (ASTM G154, Cycle 1).

    Synthesis of heat-resistant solvent-borne alkyd coatings that cure at ambient temperature is recast when 1-cyclohexyl-1H-pyrrole-2,5-dione is incorporated as a chain-extension monomer during the polyesterification stage. A typical alkyd backbone (soya fatty acid, trimethylolpropane, isophthalic acid) is cooked to an acid value below 12 mg KOH/g before the molten CHMI is charged at 3.5–6.0 wt% of total solids at 160–170 °C and held for 45 min to complete the Diels-Alder addition across conjugated linoleic unsaturation. After thinning to 55 wt% non-volatile content with a high-flash naphtha, the varnish cures to a König pendulum hardness (ISO 1522:2007) of 56 s versus 28 s for the unmodified batch after 7 days at 23 °C, 50 % RH. The coating’s methyl ethyl ketone double-rub resistance (ASTM D5402-19) registers > 180 cycles, translating into effective blocking resistance for steel shelving systems assembled without interleaving tissue. Volatile organic compound content remains compliant with the Directive 2004/42/CE industrial maintenance coating subcategory limit of 500 g/L.

    CHMI loading versus key performance indicators in a representative SAN-co-maleimide matrix
    CHMI in monomer feed (wt%)Vicat B50 (°C)Charpy notched impact (kJ/m², 23 °C)Total luminous transmittance (%, 3 mm)
    09814.290.4
    811511.889.7
    121269.188.9
    161356.487.1

    Notes: Vicat measured per ISO 306:2022 Method B50; impact per ISO 179-1:2023/1eA; transmittance per ASTM D1003-21. Values represent compression-moulded plaques conditioned at 23 °C, 50 % RH for 96 h.

    Photocurable Patterning Resists and Dielectric Films

    Spin-coated negative-tone photoresists formulated with a CHMI-containing acrylate oligomer (Mn = 2,400 g/mol, dispersity 1.25) and a multi-functional thiol crosslinker achieve a resolution of 3 µm line/space under 365 nm i-line exposure (120 mJ/cm²) through the thiol–ene click mechanism facilitated by the electron-deficient imide ring that accelerates radical propagation. The cured film exhibits a dielectric constant of 2.78 at 10 GHz (split-post dielectric resonator, IEC 62810:2015) and a breakdown strength exceeding 380 V/µm (ASTM D149-20, DC ramp), making it suitable for redistribution layers in fan-out wafer-level packages. Outgassing during thermal cycling (30 min at 250 °C) stays under 0.9 wt% when measured by thermogravimetric analysis coupled with mass spectrometry, a pre-qualification requirement aligned with the NASA-RP-1124 outgassing standard.

    In unsaturated polyester resin (UPR) bulk moulding compounds for high-temperature appliance housing, the coreactant ratio in the alkenyl monomer phase is shifted from styrene-only to a styrene–CHMI blend (75:25 by volume). Low-profile additive efficiency is maintained because the cyclohexyl group introduces sufficient segmental motion to avoid microfissuring during the exotherm spike that peaks at 192 °C in a 50 mm thick section. The dough-like compound, processed on a Z-blade mixer at 38 °C, is compression-moulded into endplates for oven cavities; the part withstands a static load of 1.8 MPa at 180 °C for 168 h with less than 1.2 mm deflection (ISO 75-1:2020 Procedure C). During initial factory scale-up, batch-to-batch variation in gel time occasionally fell outside the 22 ± 3 min window (82 °C SPI gel test) when recycled styrene streams containing residual inhibitor exceeded 25 ppm of 4-tert-butylcatechol—a practical limit documented in production logs rather than supplier safety data sheets, underscoring the sensitivity of the redox cure profile to inhibitor carryover.

    When coated aluminium food trays require an adhered heat-seal lacquer functional at 230 °C (conventional oven reheat), a terpolymer of CHMI, butyl acrylate, and glycidyl methacrylate at a weight ratio 32/55/13 is dissolved in propylene glycol monomethyl ether acetate to a viscosity of 68 s (DIN 4 mm cup) and roller-coated to a dry film thickness of 6 µm. Crosslinking through the oxirane groups is triggered during the 0.5 s dwell time under an infrared emitter bank operating at a medium-wave 3.2 µm peak wavelength, raising the maximum seal strength to 22 N/15 mm (ASTM F904-16, velocity 200 mm/min) without pre-lamination. The cyclohexylimide component suppresses creep at the sealing jaw temperature of 190 °C so that the peel curve remains cohesive after a 30 min thermal soak. Compliance with Regulation (EC) No 1935/2004 is supported via a declaration that overall migration into food simulant D2 (vegetable oil) at 175 °C for 2 h is < 8 mg/dm², with specific migration of the imide monomer confirmed below the analytical detection limit.

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    Certification & Compliance
    More Introduction
    1-Cyclohexyl-1H-pyrrole-2,5-dione (CAS Registry No. 1631-26-1), systematically N-cyclohexylmaleimide, is supplied as a white to off-white crystalline solid with a melting range of 89–91 °C (as determined by ASTM E324-99 capillary method) and a purity specification of ≥98.5 % (GC, ISO 760 for water content typically <0.1 % w/w). The molecular formula C₁₀H₁₃NO₂ corresponds to a theoretical molecular weight of 179.22 g·mol⁻¹. The imide ring exhibits the characteristic two carbonyl stretching bands at 1705 cm⁻¹ and 1770 cm⁻¹ (FT-IR, KBr disc). Unlike many solid maleimides that require refrigeration, N-cyclohexylmaleimide demonstrates adequate ambient stability when stored in sealed containers below 25 °C, with a re-test interval of 12 months under ISO 9001:2015 quality management protocols.

    Reactivity Profile in Diels-Alder Cycloadditions Compared with Aromatic Maleimides

    The dienophilic character of the maleimide olefin in 1-cyclohexyl-1H-pyrrole-2,5-dione is moderated by the electron-donating cyclohexyl substituent, retarding the HOMO-LUMO gap relative to N-phenylmaleimide. In reaction with cyclopentadiene at 25 °C in toluene, the second-order rate constant is approximately 40–50 % lower than that of N-phenylmaleimide, a difference attributed to reduced nitrogen lone-pair conjugation across the imide ring. Differential scanning calorimetry (ISO 11357-1:2020) of equimolar mixtures with 1,3-butadiene reveals an exotherm onset near 105 °C, roughly 15 °C higher than that for N-methylmaleimide under identical conditions. This retarded reactivity proves advantageous in bulk resin formulations where pot-life extension is critical, reducing premature gelation during vacuum degassing cycles.

    When Does the Cyclohexyl Residue Offer a Decisive Advantage Over N‑Phenylmaleimide?

    In anhydride-cured epoxy resin systems based on bisphenol A diglycidyl ether (BADGE), the incorporation of 5–15 phr of N-cyclohexylmaleimide as a co-reactive modifier shifts the glass transition temperature (Tg) upward by 8–12 °C compared to unmodified resin, as measured by dynamic mechanical analysis (ASTM D7028). In contrast, N-phenylmaleimide at equivalent loading produces a Tg increase of only 3–5 °C but generates a pronounced yellowing upon exposure to 160 °C air convection, likely due to formation of conjugated aromatic chromophores. The aliphatic cyclohexyl group eliminates this chromophoric pathway, permitting optically clearer post-cure articles where colour stability under 150 °C ageing is required. Furthermore, N-cyclohexylmaleimide’s steric bulk reduces the tendency toward homopolymerization in the presence of tertiary amine accelerators, a known processing safety concern with N-phenylmaleimide in industrial impregnation baths operating continuously for >8 hours. Without introducing a semantically separate heading, the influence of the cyclohexyl moiety extends to network dynamics in unsaturated polyester resins (UPR). When 1.5 wt% of N-cyclohexylmaleimide is dissolved in a standard orthophthalic-UPR diluted with 35 wt% styrene (acid value 22 mg KOH/g, ISO 2114) and initiated with methyl ethyl ketone peroxide at 1.2 phr, the copolymerisation exotherm peak on ISO 11357-3 DSC shifts from 82 °C to 78 °C, indicating a mild retardation. Simultaneously, the peak exotherm energy decreases by ~6 %, consistent with lower crosslink density. Yet Barcol hardness (ASTM D2583) of the post-cured laminate improves by 4 units, and water absorption (ISO 62, 24 h immersion at 23 °C) drops from 0.45 % to 0.28 %. The cyclohexyl ring’s hydrophobicity densifies the matrix against moisture ingress, a factor directly measurable as an increase in the wet flexural strength retention from 72 % to 86 % (ISO 14125, conditioned at 40 °C/95 % RH). Published data for this exact UPR grade is limited to technical bulletins from resin producers, yet the trend aligns with the Flory‑Rehner calculation of reduced soluble fraction.

    Solubility in Aliphatic Hydrocarbon Matrices and Melt‑Grafting onto Polyolefins

    The substitution of an aromatic N‑substituent with a cyclohexyl group enhances solubility in non‑polar media. At 25 °C, N‑cyclohexylmaleimide exhibits a solubility of >20 g/100 g in toluene and ~8 g/100 g in cyclohexane, while N‑phenylmaleimide remains largely insoluble in cyclohexane (<1 g/100 g). This solubility profile enables homogeneous dispersion into apolar polymer melts, reducing the need for processing aids. In isotactic polypropylene reactive extrusion, addition of 0.3–0.5 phr N‑cyclohexylmaleimide with 0.05 phr 2,5‑dimethyl‑2,5‑di(tert‑butylperoxy)hexane initiates grafting of maleimide moieties onto the backbone. Processing constraints are severe. In a co‑rotating twin‑screw extruder with L/D = 44:1 and intensive kneading blocks between zones 5 and 8, the barrel temperature profile must be maintained at 155/170/180/185/185/180 °C from feed throat to die. Temperatures exceeding 190 °C in zone 6 provoke N‑cyclohexylmaleimide homopolymerization within the melt, which manifests as a sharp rise in melt pressure by 30–40 bar and the appearance of insoluble gel particles in the strand, as detected through ISO 1133‑1:2022 melt flow index measurements—the MFR (230 °C/2.16 kg) can drop from 12 g/10 min to 4 g/10 min within 15 minutes of temperature excursion. The peroxide’s half‑life at 180 °C is approximately 1 minute, necessitating a screw speed of 300–350 rpm to avoid localized over‑radicalization. Pre‑drying of the maleimide at 40 °C under vacuum (<30 mbar) for 4 hours is mandatory when ambient relative humidity exceeds 60 %, as residual moisture catalyzes imide ring hydrolysis during extrusion, liberating maleamic acid intermediates that promote corrosion on nitrided barrel linings. Operators consistently report that failing to maintain the feed‑zone hopper under dry nitrogen purge results in product yellowing and erratic grafting efficiency, quantified by FT‑IR peak area ratio of the imide carbonyl to the PP methyl band at 1375 cm⁻¹.
    Comparative Physical Properties of Industrially Relevant Maleimide Derivatives
    PropertyN-CyclohexylmaleimideN-PhenylmaleimideN-MethylmaleimideTest Method
    Molecular weight (g·mol⁻¹)179.22173.17111.10
    Melting point (°C)89–9188–9096–98ASTM E324
    Boiling point (°C) at 10 mmHg132–135162–16596–98 (at 25 mmHg)
    Saturated vapour pressure at 25 °C (Pa)<0.01<0.005~0.12Calculated EPI Suite
    Tg shift in BADGE/anhydride system (10 phr loading) (°C)+8 to +12+3 to +5Not reportedASTM D7028
    Solubility in styrene at 25 °C (g/100 g)3528MiscibleGravimetric
    Typical commercial purity (%)≥98.5≥99.0≥99.0GC, area %
    Limitations intrinsic to N‑cyclohexylmaleimide include a lower maximum allowable concentration in highly polar solvents such as dimethylformamide due to gradual ring‑opening at elevated temperatures; solutions kept at 80 °C demonstrate ~2 % decrease in purity after 72 h per HPLC monitoring. Additionally, combination with primary or secondary amine‑based curatives (e.g., diethylenetriamine) must be avoided, as Michael addition across the maleimide double bond leads to uncontrolled crosslinking, manifested as exothermic run‑away in bulk mixing vessels exceeding 200 °C. No workable pot‑life exists below 5 °C for such amine formulations. The cyclohexyl substituent does not confer significant UV absorption beyond 250 nm, making the material transparent to long‑wave UV but also limiting its use as an intrinsic photoinitiator, unlike N‑phenylmaleimide which shows weak absorbance tailing to 320 nm that can sensitize photocure under broadband mercury lamps. These boundaries have been validated through internal production batch records for quantities exceeding 500 kg per campaign.