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

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


    • Product Name 1-Methyl-1H-Pyrrole-2,5-Dione
    • Alias N-Methylmaleimide
    • Einecs 212-193-2
    • 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

    933174

    Name 1-Methyl-1H-pyrrole-2,5-dione
    Chemical Formula C5H5NO2
    Molar Mass 111.1 g/mol
    Appearance Colorless to light yellow solid
    Melting Point 82 - 84 °C
    Boiling Point 202 - 204 °C
    Solubility In Water Slightly soluble
    Solubility In Organic Solvents Soluble in common organic solvents like ethanol, acetone
    Density 1.305 g/cm³
    Flash Point 110 °C
    Vapor Pressure Low at room temperature

    As an accredited 1-Methyl-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 1 - Methyl - 1H - Pyrrole - 2,5 - Dione packaged in 100 - gram vials for secure storage.
    Shipping 1 - Methyl - 1H - Pyrrole - 2,5 - Dione is shipped in accordance with chemical transportation regulations. Packed securely in suitable containers, it's transported via approved carriers to ensure safe delivery, minimizing risks during transit.
    Storage 1 - Methyl - 1H - Pyrrole - 2,5 - Dione should be stored in a cool, dry, well - ventilated area. Keep it away from sources of heat, ignition, and strong oxidizing agents. Store in a tightly closed container to prevent moisture absorption and evaporation. It is advisable to store it in a dedicated chemical storage cabinet, separated from incompatible substances to ensure safety and maintain its chemical integrity.
    Application of 1-Methyl-1H-Pyrrole-2,5-Dione

    In the continuous reactive extrusion of heat-resistant acrylonitrile-butadiene-styrene (ABS) grades, N-methylmaleimide (NMMI) is graft-copolymerized onto the styrene-acrylonitrile (SAN) backbone or incorporated as a termonomer during bulk SAN synthesis. The driving requirement is a 10–30 °C elevation in heat deflection temperature under load without sacrificing impact strength retention. A typical charge ratio loads NMMI into the SAN phase at 5–20 wt%, co-fed with a peroxide initiator such as dicumyl peroxide at 0.05–0.2 phr through a liquid injection port at barrel zone three of a co-rotating twin-screw extruder with an L/D ratio of 40–48. Barrel set points are profiled from 180 °C in the feed zone to 230 °C at the reaction and kneading zones, followed by a vacuum vent at ≤50 mbar absolute pressure to strip residual monomer to below 500 ppm. Process records from production lines show that local hot spots exceeding 245 °C trigger retro-Diels-Alder reversion of NMMI adducts, releasing maleimide volatiles and causing surface splay on molded parts. Therefore, screw designs with distributive mixing elements and moderate shear rates below 300 s⁻¹ are selected to manage exotherm. The grafted ABS pellets are subsequently injection molded with mold temperatures of 60–80 °C and melt temperatures of 230–250 °C. Finished components must meet ISO 75-2/A (HDT ≥ 105 °C at 1.8 MPa), UL 94 HB at 1.5 mm, and typical OEM colorfastness standards such as SAE J1885 for interior weatherability. End parts include unpainted automotive rearview mirror housings, center console carriers, and pillar trim, where the elimination of post-molding annealing steps directly improves line throughput.

    What role does N-methylmaleimide play in semiconductor epoxy molding compounds?

    Semiconductor epoxy molding compounds (EMCs) formulated with o-cresol novolac epoxy and phenol aralkyl hardeners are modified with N-methylmaleimide as a co-curing agent to raise the glass transition temperature and improve hot-wet reliability. NMMI participates in the crosslinking network through its electron-deficient double bond, reacting with epoxide groups and phenolic hydroxyls during post-mold cure. Typical loading spans 5–15 phr relative to the epoxy resin base, with the exact value tuned to balance spiral flow length and warpage. Transfer molding is conducted with preheated preforms at 80–100 °C, mold platen temperatures of 175 ± 5 °C, and transfer pressures between 70 and 100 bar. Post-mold cure follows a ramp-and-hold profile of 4 hours at 175 °C under nitrogen. The compound must satisfy the compliance matrix summarized in the table below, drawn from semiconductor packaging qualification protocols. At NMMI addition levels above 15 phr, the storage modulus in the rubbery plateau rises sharply but 90° peel strength on copper leadframes can degrade; filler packages containing spherical silica at 87–92 wt% are adjusted with silane coupling agents to mitigate this interface sensitivity. Finished EMC encapsulates logic devices, memory packages in TSOP and BGA formats, and LED driver ICs where JEDEC MSL 1 reliability is mandatory.

    Test DisciplineReference StandardTest ConditionTypical Acceptance Criterion
    Glass transition temperatureASTM E1640 (DMA)1 Hz, 5 °C/min rampTg ≥ 165 °C
    FlammabilityUL 94Vertical test, 0.8 mm specimenV-0
    Spiral flowSEMI G81-0697175 °C transfer mold90–140 cm
    Volume resistivityIPC-SM-840 3.9.1.2After 85 °C/85% RH≥ 1×10¹⁴ Ω·cm
    Ionic extractablesIPC-TM-650 2.3.25Water extraction 120 °CCl⁻ < 10 ppm

    Photoacid-catalyzed deprotection and the 193 nm resist matrix

    For 193 nm immersion lithography, the photoresist polymer matrix requires a high carbon-to-hydrogen ratio for reactive ion etching resistance without compromising alkaline developer solubility. Terpolymers of 4-hydroxystyrene, tert-butyl acrylate, and N-methylmaleimide have been deployed in commercial resist platforms; NMMI units are incorporated at 15–30 mol% to raise the Ohnishi parameter while preserving acid-labile deprotection kinetics. The resist is spin-coated onto a bottom anti-reflective coating layer with a post-apply bake of 100–130 °C for 60 seconds, then exposed through a 1.35-NA scanner with polarized off-axis illumination. The post-exposure bake (PEB) is executed at 110–130 °C for 90 seconds, during which photo-generated acid cleaves the tert-butyl ester groups, switching the NMMI-containing terpolymer to an aqueous-base-soluble form. Development is carried out with 0.26 N tetramethylammonium hydroxide for 30–60 seconds. A critical processing conflict emerges at NMMI fractions above 25 mol%: the dark erosion rate in unexposed regions increases due to the inherent polarity of the maleimide ring, diminishing contrast. To suppress this, the formulation includes quenchers and lithographic surfactants, and the PEB temperature must be held within a window of ±2 °C. Metallic contamination requirements follow SEMI P3-0418 specifications, with sodium and iron each held below 1 ppb in the neat resin. The end product is used to pattern gate- and metal-layer trenches in foundry logic nodes at 20 nm half-pitch and below.

    When formulating polybenzoxazine resins for halogen-free fire-retardant laminates, a reactive diluent approach replaces inert solvents: N-methylmaleimide is dissolved into benzoxazine monomers and reacts with the phenolic species generated during the ring-opening polymerization, raising the crosslink density of the cured network. The addition level is typically 5–15 wt% based on the total resin mass. Laminates are produced by hot-pressing prepregs at 200–220 °C under 20–40 bar pressure, with isothermal holds of at least 2 hours. Because NMMI is sensitive to premature addition reactions with residual amine-type curing accelerators, the catalyst system is restricted to latent imidazole derivatives or phenolic triazine catalysts that activate above 160 °C. Compliance is evaluated against EN 45545-2 for railway interiors (HL2, R1 hazard levels) and FAR 25.853 for aircraft cabin materials; smoke density (Ds max) measured per ISO 5659-2 remains below 200 at NMMI loadings up to 12 wt%. The finished composite is fabricated into electrical insulation panels, galley partitions, and low-pressure decorative laminate backers, where the absence of halogenated flame retardants simplifies end-of-life incineration.

    A processing window of ±5 °C in melt copolymerization for heat-resistant PMMA sheet

    Copolymerization of methyl methacrylate with N-methylmaleimide introduces cyclic imide units into the acrylic backbone, disrupting the isotactic sequences that otherwise facilitate depolymerization. A typical charge uses 10–25 wt% NMMI in the monomer feed, dissolved at 40–50 °C before being fed into a continuous polymerization reactor. The process relies on a horizontal ribbon-type reactor operating at 220–235 °C with a residence time of 15–45 minutes, followed by twin-screw devolatilization at 250–260 °C under vacuum. The window of operation is narrow: at temperatures above 240 °C, the rate of backbone depolymerization accelerates sharply, generating MMA monomer bubbles that become trapped as optical defects in the sheet. Conversely, at temperatures below 215 °C, the conversion rate drops below 60% and the residual NMMI monomer plasticizes the extruded sheet, pulling the Vicat softening temperature below the target of 125 °C (method B50, ISO 306). Published data for this specific configuration is limited, but plant-scale references indicate that process capability studies cluster the acceptable thermal midpoint at 228 ± 5 °C for NMMI levels of 15 wt%. The extruded sheet must pass ASTM D4802 accelerated outdoor exposure (3000 hours xenon-arc) with yellowness index shift below 2 units, and the final product is thermoformed into aircraft cabin window reveals, high-intensity LED lens rails, and sound barrier panels where the combination of transparency and a service temperature exceeding 110 °C is required.

    In radiation-curable adhesive formulations for electronic assembly, the incorporation of N-methylmaleimide as a dual functional monomer raises crosslink density without increasing initial viscosity to levels incompatible with high-speed jet dispensing. Concentrations span 5–15 wt% in urethane acrylate or polyester acrylate base resins, and curing is initiated by a 365 nm UV-LED array with a radiant intensity of ≥ 2 W/cm². The addition of NMMI increases the modulus above the glass transition by approximately 30% compared to equivalent formulations using isobornyl acrylate. Compliance testing includes lap shear strength per ISO 527-1/-2 adapted for adhesives, with typical values exceeding 12 MPa on polycarbonate substrates, and 85/85 accelerated aging per ISO 6270-2 with weekly cycling. A known limitation is that NMMI exhibits a tendency to crystallize on standing in monomer mixtures stored below 15 °C; pre-warming to 30 °C with gentle recirculation is required before dispensing to avoid clogged micronozzles. End products include lens barrel bonding in smartphone camera modules and voice coil motor magnet assembly, where cycle times under 3 seconds and low outgassing are mandatory.

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    Certification & Compliance
    More Introduction

    1-Methyl-1H-pyrrole-2,5-dione (CAS 941-69-5), systematically referred to as N-methylmaleimide, is a cyclic imide monomer possessing a highly electrophilic 1,2-disubstituted olefinic bond. The compound is supplied as a white to pale yellow crystalline solid with a characteristic melting point of 96–98 °C as determined by differential scanning calorimetry at a heating rate of 10 K/min under nitrogen. Its molecular weight is 111.10 g/mol, and the material typically exhibits a purity of ≥99.0% by GC (area normalization). Residual free maleic anhydride content is controlled to ≤0.10 wt%, and the recommended storage condition — under dry inert gas at 2–8 °C — minimizes dimerization and hydrolytic ring-opening. In radical copolymerization, the reactivity ratios with styrene (rSt0.05, rNMMI0.02 at 60 °C) drive a highly alternating sequence distribution, a characteristic exploited extensively in the production of heat-resistant thermoplastics.

    Processing Stability and Inhibitor Requirements

    Bulk handling of molten N-methylmaleimide demands rigorous temperature control. The monomer undergoes thermal homopolymerization at temperatures exceeding 110 °C, and the rate accelerates autocatalytically in the presence of trace bases. Therefore, commercial grades are stabilized with 10–50 ppm of 4-methoxyphenol (MEHQ) or phenothiazine. When melt-blending into styrenic copolymers via a co-rotating twin-screw extruder with L/D 40:1, barrel temperatures must be profiled to avoid dead zones exceeding 105 °C in the rear zones. Processors operating in production environments where relative humidity exceeds 60% must pre-dry the monomer at 40 °C under vacuum (≤10 mbar) for 4 h; failure to do so results in partial hydrolysis to N-methylmaleamic acid, which retards polymerization kinetics and introduces carboxylic acid defects into the backbone.

    In continuous mass polymerization of acrylonitrile-butadiene-styrene (ABS), incorporation of 5–15 wt% N-methylmaleimide into the styrene-acrylonitrile feed raises the glass transition temperature of the SAN matrix phase by approximately 1.8 °C per 1 wt% of monomer. Heat deflection temperature (HDT) under 1.82 MPa (ISO 75-2:2013, Method A) values exceeding 105 °C are attainable, compared with 82–88 °C for unmodified general-purpose ABS. The resultant copolymer exhibits a melt flow index shift: a reduction of 15–30% in MFR (ISO 1133-1:2022, 220 °C/10 kg) is typical, requiring injection molders to adjust nozzle temperature upward by 10–15 °C and clamp force by 5–8% to maintain complete cavity fill.

    Specification and Purity Control in Polymer-Grade Material

    Typical Release-Limit Specifications for N-Methylmaleimide (Polymerization Grade)
    ParameterSpecificationTest Method
    Assay (GC)≥99.0%In-house GC-FID, DB-5 column, 120–280 °C ramp
    Melting range96.0–98.0 °CPharmacopoeia capillary method, 1 °C/min near melt
    Free maleic anhydride≤0.10%HPLC-UV at 254 nm, C18 column
    Water (Karl Fischer)≤0.20%ISO 760:1978 (coulometric)
    Color (APHA, 50% in acetone)≤30ASTM D1209-05(2019)
    Inhibitor (MEHQ)15–35 ppmHPLC, external standard

    For applications demanding ultra-low ionic contamination — particularly in electronics-grade encapsulants or photosensitive compositions — a high-purity variant is offered with chloride and sulfate each controlled to ≤2 ppm and sodium to ≤1 ppm, determined by ion chromatography following oxygen bomb combustion (ASTM D4327-17). This material is packaged in aluminum-lined fiber drums under a nitrogen blanket to maintain an oxygen headspace concentration below 0.5 vol%.

    Thermal hazard assessment by differential scanning calorimetry (ASTM E537-20) indicates an onset temperature for exothermic decomposition at 290 °C, with a total energy release of 1,250 J/g. This necessitates strict adherence to a maximum local hot-spot temperature of 150 °C during any distillation recovery or vent treatment operation in continuous polymerization plants.

    When N-Methylmaleimide Replaces Maleic Anhydride in High-Heat Copolymers

    A direct substitution of maleic anhydride by N-methylmaleimide in graft-modified polyolefins or styrenic terpolymers introduces three distinct performance shifts. First, the imide ring exhibits superior thermal stability: thermogravimetric analysis (TGA) in air at 10 °C/min reveals a 5% mass loss temperature approximately 40–55 °C higher for NMMI-containing copolymers than for their maleic anhydride counterparts. Second, the lack of anhydride ring-opening eliminates moisture sensitivity — after 24 h immersion in 85 °C water, the retention of tensile strength (ASTM D638-14, Type I specimen) exceeds 92%, whereas anhydride-functionalized analogues retain less than 70%. Third, the N-methyl group imparts a permanent dipole to the imide ring, modifying the dielectric constant. At 1 MHz and 23 °C, the dissipation factor of a 15 wt% NMMI-modified SAN measured per IEC 60250:1969 falls to 0.004–0.007, compared to 0.009–0.014 for the maleic anhydride analogue.

    However, a process incompatibility arises when N-methylmaleimide is combined with primary or secondary amine-functional additives — for example, certain hindered amine light stabilizers (HALS) with reactive >NH groups. The amine can undergo Michael addition across the olefinic bond at processing temperatures, consuming both the stabilizer and the reactive site intended for copolymerization. Formulators must select non-nucleophilic radical scavengers; the use of antioxidant blends based on octadecyl-3-(3,5-di-tert-butyl-4-hydroxyphenyl)propionate (Irganox 1076) and tris(2,4-di-tert-butylphenyl)phosphite (Irgafos 168) has been validated without adverse interaction.

    Comparative Copolymerization Behavior with N-Phenylmaleimide

    Both N-methylmaleimide and N-phenylmaleimide yield alternating copolymers with styrene, but the methyl derivative provides a lower glass transition temperature per unit weight of comonomer. For a copolymer containing 50 mol% imide, the Tg (midpoint, DSC, 20 °C/min) of the N-methylmaleimide-styrene copolymer is 196 °C, whereas the N-phenylmaleimide analogue reaches 229 °C (measured per ISO 11357-2:2020). This 33 °C offset directly impacts extrusion window flexibility: the N-methyl variant can be processed on standard polycarbonate-grade screws with barrel settings of 260–280 °C, while the phenyl variant demands 290–310 °C, a range that accelerates thermal yellowing unless vacuum venting is augmented. Furthermore, the molar volume difference (N-methyl group vs. N-phenyl ring) alters the solubility parameter. The Hansen solubility parameter dispersion component (δd) for poly(N-methylmaleimide-alt-styrene) is calculated at 19.2 MPa1/2, resulting in broader compatibility with aromatic polycarbonate in blends, as evidenced by a single-phase morphology in 70:30 PC/copolymer extrudates at a screw speed of 300 rpm.

    In resist applications, the alkaline dissolution rate in 0.26 N tetramethylammonium hydroxide (TMAH) at 23 °C is 8–12 nm/s for N-methylmaleimide-containing terpolymers, versus 25–40 nm/s for the N-phenyl analogue, enabling finer line-width control in 248 nm photolithography.

    Physical and Processing Properties of Styrene-Imide Alternating Copolymers (50 mol% Imide)
    PropertyN-Methylmaleimide CopolymerN-Phenylmaleimide CopolymerTest Method
    Tg (midpoint)196 °C229 °CISO 11357-2:2020
    Melt viscosity at 280 °C/100 s−11,200 Pa·s3,800 Pa·sISO 11443:2021
    HDT (1.82 MPa, annealed)148 °C172 °CISO 75-2:2013
    Flexural modulus3.9 GPa4.2 GPaASTM D790-17
    Alkaline dissolution rate (TMAH 0.26N)8–12 nm/s25–40 nm/sQuartz crystal microbalance

    Is Thermal Base-Catalyzed Ring-Opening a Limiting Factor in PVC Modification?

    When N-methylmaleimide is graft-copolymerized onto poly(vinyl chloride) (PVC) via reactive extrusion, a critical threshold emerges at a processing temperature of 190 °C. At or above this point, dehydrochlorination of the PVC backbone releases HCl, which can catalyze the hydrolysis of unreacted N-methylmaleimide to N-methylmaleamic acid. This side reaction consumes the monomer without contributing to graft efficiency and introduces carboxylic acid moieties that accelerate further PVC dehydrochlorination autocatalytically. Measurement of grafting yield by Soxhlet extraction with acetone (ASTM D5227-21) shows a drop from 62% at 180 °C barrel set temperature to 31% at 195 °C, all other parameters held constant. Consequently, formulators must employ an acid scavenger — typically a calcium-zinc stabilizer package at 3–5 phr — and limit the residence time distribution in the extruder to a maximum of 90 s. Under these conditions, a VICAT softening temperature (ISO 306:2022, Method B50) increase of 9–12 °C is achieved at a 7 wt% monomer feed.

    A further differentiation from maleimide (unsubstituted) and N-ethylmaleimide lies in the hydrolysis rate constant. The pseudo-first-order rate constant for N-methylmaleimide ring-opening in water at pH 7.0 and 25 °C is 3.2×10−5 s−1, compared to 1.1×10−4 s−1 for maleimide and 2.8×10−5 s−1 for N-ethylmaleimide, as determined by conductometric monitoring. The enhanced hydrolytic stability of the methyl derivative relative to the unsubstituted compound is attributed to the electron-donating inductive effect of the N-methyl group, which reduces the electrophilicity of the carbonyl carbons.

    In coil-coating formulations based on saturated polyesters crosslinked with hexamethoxymethylmelamine (HMMM), a small fraction (2–4 wt% on total resin solids) of an N-methylmaleimide-modified polyester resin introduces a controlled degree of unsaturation. During the cure cycle at 230 °C peak metal temperature, thermoreversible crosslinks via retro-Diels-Alder depolymerization and re-addition are suppressed in favor of irreversible imide group integration, improving the solvent resistance (MEK double rubs per ASTM D5402-19) from 35–45 to 80–100 without a glass transition increase that would compromise flexibility in a 0 T bend test.

    The compound is registered under EU REACH (EC No. 213-395-4) and is classified as a skin irritant and sensitizer, requiring closed-loop transfer systems in compounding facilities. Airborne exposure limits are set at an 8-hour TWA of 0.5 mg/m³ (inhalable fraction) following national occupational hygiene guidelines. Packaging in 25 kg net fiber drums with inner LDPE liner remains standard for industrial distribution; quantities exceeding 500 kg are available in supersacks with conductive polyethylene liners for direct feed into loss-in-weight gravimetric dosing units on extrusion lines.