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

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


    • Product Name 1-Ethyl-1H-Pyrrole-2,5-Dione
    • Alias N-Ethylmaleimide
    • Einecs 220-709-2
    • Mininmum Order 1g
    • Factory Site West Ujimqin Banner, Xilingol League, Inner Mongolia, China
    • Price Inquiry sales9@bouling-chem.com
    • Manufacturer Bouling Chemical Co., Limited
    • CONTACT NOW
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    Specifications

    HS Code

    732699

    Chemical Formula C6H7NO2
    Molar Mass 125.126 g/mol
    Appearance White to off - white solid
    Melting Point 125 - 127 °C
    Boiling Point 281.6 °C at 760 mmHg
    Solubility In Water Slightly soluble
    Solubility In Organic Solvents Soluble in common organic solvents like ethanol, acetone
    Density 1.192 g/cm³
    Flash Point 124.9 °C
    Odor Weak, characteristic

    As an accredited 1-Ethyl-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 - Ethyl - 1H - Pyrrole - 2,5 - Dione packaged in a sealed, chemical - resistant bottle.
    Shipping 1 - Ethyl - 1H - Pyrrole - 2,5 - Dione is shipped in sealed, corrosion - resistant containers. It's transported under controlled conditions, ensuring compliance with chemical shipping regulations to prevent spills and maintain product integrity.
    Storage 1 - Ethyl - 1H - Pyrrole - 2,5 - Dione should be stored in a cool, dry, well - ventilated area. Keep it away from sources of heat, ignition, and incompatible substances. Store in a tightly sealed container to prevent moisture absorption and potential degradation. It is advisable to store it in a dedicated chemical storage cabinet separate from reactive or flammable chemicals.
    Application of 1-Ethyl-1H-Pyrrole-2,5-Dione

    A common pathway for enhancing the thermal-oxidative stability of ethylene-propylene-diene terpolymer (EPDM) vulcanizates involves co-agent grafting during sulfur-accelerated cure, which restructures the network topology by generating thermally robust carbon-carbon crosslinks while suppressing polysulfidic bridges. Compounding on a 1.5 L laboratory internal mixer (Banbury rotor, ram pressure 0.6 MPa) with a drop temperature of 145°C, followed by curative addition on a two-roll mill at 50°C, the material is introduced at 1.0–2.5 phr. The critical processing boundary is a Mooney scorch time t5 at 125°C (ASTM D1646-19) not less than 12 minutes; exceeding 2.8 phr causes a collapse in scorch safety below 6 minutes, rendering the stock unsuitable for transfer molding of complex profiles. After cure in a 300-ton vacuum compression press at 170°C for 8 minutes, the molded sheet shows retention of 87% tensile strength and 72% elongation at break after 168 h aging at 150°C per ISO 188:2011 method B. Compliance for under-the-hood rubber goods is verified against ASTM D2000 M2HK8 A14 B13 classification and REACH Annex XVII entry 50 restrictions on extender oils. The finished components—turbocharger air ducts, diesel injector O-rings with +/-0.03 mm tolerance, and dynamic glass-run channel seals—are post-cured in hot-air tunnels at 160°C for 4 hours to drive off residual cyclohexane-soluble fractions below 0.5 wt%.

    Why does the heat deflection temperature of orthophthalic unsaturated polyester resin rise sharply at 3.2 wt% additive loading?

    Standard orthophthalic unsaturated polyester dissolved in styrene (35 wt%) and initiated with 1.5 phr methyl ethyl ketone peroxide exhibits a single-network morphology with a glass transition temperature rarely exceeding 110°C. When the ethyl-substituted maleimide is pre-dissolved in the styrene monomer at 3.0–3.5 wt% of the total resin, differential scanning calorimetry at 10 K/min records a secondary exotherm peaking at 168°C attributable to maleimide homopolymerization that intertwines with the polyester-styrene copolymerization. This interpenetrating architecture, validated on a 60 L vertically agitated gel-coat spray-up line for marine hulls and on a vacuum infusion station operating at 0.08 MPa bag pressure, elevates the heat deflection temperature from 84°C to 108°C (ISO 75-2:2013 method A, 1.8 MPa flexural stress). Simultaneous reduction in styrene emission by 14–18% is confirmed via EPA Method 18 canister sampling above the mold flange. The laminates meet the smoke density criteria of IMO FTP Code Part 2 Annex 1 and the residual styrene monomer threshold of EU Regulation 10/2011 for incidental food contact in tank linings. Fabrication includes pultrusion of corrosion-resistant structural profiles with 75% glass content (ASTM D 2584 ignition loss) and filament winding of chemical storage vessels rated at 4 bar design pressure.

    Printed circuit board laminate manufacturers confronting the Pb-free solder reflow profile with 260°C peak temperature and 245°C threshold above liquidus for 90 seconds require a dielectric matrix that does not delaminate at the glass-resin interface. Substituting a portion of the dicyandiamide/epoxy adduct with the maleimide monomer at 7.5–12.0 phr (resin solids basis) in a brominated bisphenol-A/novolac varnish, and processing through a 1.2 m vertical treater tower with controlled 180°C radiant zones, yields prepregs with a gel time of 110 seconds at 170°C. Lamination of eight plies between 35 micron electrodeposited copper foil in a hydraulic press at 2.8 MPa and 190°C for 95 minutes generates a cured laminate with a dynamic mechanical Tg of 178°C (IPC-TM-650 method 2.4.24.2), exceeding the IPC-4101E /99 specification for high-Tg FR-4. The laminate achieves UL 94 V-0 rating at a thickness of 0.8 mm without the need for antimony trioxide, and the comparative tracking index remains above 400 V (IEC 60112:2020). Finished multilayers of 18 to 24 layers are deployed in server backplane boards requiring conductive anodic filament resistance per IPC-9691B, and in avionic RF filter substrates where Z-axis expansion below 50 ppm/°C before Tg is non-negotiable.

    Acrylic-Melamine Clearcoat Crosslinking and Scratch Resistance

    Thermoset clearcoats formulated with hydroxy-functional acrylic resin and fully alkylated hexamethoxymethylmelamine crosslinker are susceptible to acid-etch degradation and micro-scratching triggered by car-wash brushes, a failure mode linked to insufficient network density at the outermost surface. Introducing the ethyl-substituted maleimide into the mill-base at 0.8–1.2% of total resin solids, dispersed via a cowles blade at 18 m/s tip speed before letdown with melamine and rheology modifiers, adds a latent dual-cure mechanism: the maleimide undergoes thermal [2+2] cycloaddition with photo-generated unsaturations in the acrylic backbone during the forced-air flash-off and convection cure cycle. The topcoat is applied using a high-speed rotary bell atomizer spinning at 55,000 rpm over a cathodic electrodeposition primer and baked in a convection oven with 15-minute metal substrate dwell at 148°C. After 3000 hours of SAE J2527 Xenon arc weathering, the system maintains a crosshatch adhesion rating of Gt 0 (ISO 2409:2020) and a gloss retention above 93% at 20° incidence. The micro-scratch recovery ratio, measured by the crockmeter method under a 9 N load per DIN 55654:2015, exceeds 85%. Finished passenger vehicles must conform to ASTM D7356-22 for acid-etch resistance and to the OEM’s proprietary stone-chip chipping specification at -20°C.

    When a thiol-reactive magnetic bead surface requires low non-specific binding in lateral flow immunoassays

    Carboxyl-modified superparamagnetic polymer microspheres with a mean diameter of 200 nm and a polydispersity index below 0.05 are washed in 50 mM MES buffer at pH 5.5 and activated with 5 mM EDC and 7.5 mM sulfo-NHS for 25 minutes under gentle end-over-end rotation. The activated particles are centrifuged at 18,000×g in a Hermle Z36HK refrigerated floor centrifuge at 4°C, resuspended in 0.1 M phosphate buffer pH 7.2, and reacted with ethylenediamine to introduce terminal primary amines. The amine-functionalized intermediate is then acylated with a 2 mM solution of the maleimide monomer in dimethylformamide-phosphate buffer (v/v 1:4) for 2 hours at 25°C. This yields a stable maleimide surface density of 0.8–1.5 nmol/mg dry particles, quantified by a glutathione back-titration with Ellman’s reagent. Conjugation of Fab’-SH fragments at 0.5 mg antibody per milligram particles in the same buffer without reductants prevents inter-particle crosslinking, and the final conjugate concentrate is diluted into a running buffer containing 0.1% BSA for test strip dispensing. The analytical sensitivity of the assembled high-sensitivity troponin I and NT-proBNP rapid tests complies with CLSI EP17-A2 for limit of blank and limit of detection. Manufacturing of the activated particles is conducted under ISO 13485:2016 quality management, and the finished in vitro diagnostic devices are registered under EU IVDR 2017/746 Annex IX, class C.

    Dry-blending suspension-grade polyvinyl chloride with a K-value of 66 together with a calcium-zinc stabilizer package (2.2 phr), an acrylic processing aid (1.5 phr), and a styrene-N-ethylmaleimide copolymer heat modifier at 12 phr loading is carried out in a high-speed mixer to a discharge temperature of 130°C. The dry blend is fed into a co-rotating twin-screw extruder with 40:1 L/D ratio, a barrel set-point profile from 160°C to 190°C, and vacuum devolatilization at -0.08 MPa to strip residual monomer. The compounded pellets are injection molded into ASTM test specimens on a 120-ton press with a nozzle temperature of 205°C and a mold surface temperature controlled to 45°C via a thermolator. The resulting compound achieves a Vicat softening temperature of 98°C (ISO 306:2022 method B50 with 50 N load and 50 K/h heating rate), representing a 22°C increase over unmodified PVC at the same filler level, while retaining a notched Charpy impact strength of 5.1 kJ/m² (ISO 179-1:2020, edgewise, 2 mm notch radius). Compliance verification includes IEC 62321-8:2017 screening for restricted phthalates, EU RoHS Directive 2011/65/EU Annex II, and flammability classification V-0 at 2.0 mm thickness per UL 94. Finished injection-molded components are thermostat housings, electrical junction-box lids for industrial control panels, and railcar interior trim panels meeting EN 45545-2 R1 set HL2 hazard level.

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    Certification & Compliance
    More Introduction

    1-Ethyl-1H-pyrrole-2,5-dione (CAS 128-53-0), commonly designated N‑ethylmaleimide or NEM, is a crystalline α,β‑unsaturated imide with a molecular mass of 125.13 g·mol⁻¹. The compound presents as a white to off‑white lachrymator melting sharply at 45–47 °C and is structurally characterised by an electrophilic maleimide ring that undergoes selective Michael addition with thiolate nucleophiles. This reactivity underpins its widespread use in sulfhydryl‑group blocking, protein‑fluorescent dye conjugation, enzymatic active‑site titration, and polymer‑grafting chemistries. Unlike longer‑chain N‑alkyl maleimides, the ethyl substituent balances moderate aqueous solubility (≈5 g·L⁻¹ at 20 °C) with sufficient organic solvent compatibility, permitting homogeneous reaction conditions in both aqueous buffers and toluene or dioxane.

    What Purity Specification Minimises Interference in Cysteine Protease Active‑Site Titration?

    The utility of N‑ethylmaleimide in quantitative biochemistry depends critically on the absence of hydrolytic by‑products and dimeric species. Maleic acid, the primary hydrolytic degradation product generated during storage or aqueous handling, acts as a non‑selective acylating agent and interferes with stoichiometric cysteine targeting. Commercial grades therefore carry acceptance criteria: HPLC purity by area at 220 nm99.0%, residual maleic acid ≤ 0.2%, and bis‑succinimide dimer ≤ 0.5%. These values are derived from orthogonal data obtained by reversed‑phase C18 gradient analysis and are specified in supplier certificates of analysis that align with internal protocols referencing ICH Q3B guidance. A 0.1% increase in dimer content has been observed to reduce the observed second‑order rate constant for active‑site titration of papain by as much as 12%, a deviation that falls outside the allowable error in enzyme kinetics determinations conducted per ISO 22118:2011. The following specification matrix is typical for reagent‑grade material used in bioconjugation scale‑up.

    PropertySpecificationMethod
    AppearanceWhite to off‑white crystalline powderVisual inspection, lot retained at 2–8 °C
    Assay (HPLC)99.0% areaC18, UV 220 nm, isocratic MeOH/H₂O
    Melting point45–47 °CASTM D3418 (DSC, 10 K·min⁻¹)
    Residual maleic acid0.2%Ion chromatography, conductivity detection
    Dimer (bis‑succinimide)0.5%HPLC‑MS, SIM at m/z 251
    Loss on drying0.5%Karl Fischer titration, 50 °C
    Solubility in water5 g·L⁻¹ at 20 °CUV‑vis after centrifugation

    Cold‑chain logistics are essential: exposure to ambient humidity above 60% RH during sampling can initiate surface hydrolysis within 15 min, evidenced by a broadening of the DSC melt endotherm. Manufacturers employing drum‑size containers (25 kg fibre drums with LDPE liners) routinely back‑fill headspace with dry nitrogen to suppress moisture ingress. Users are therefore advised to equilibrate the container to 25 °C before opening and to dispense under a positive‑pressure inert‑gas blanket.

    For selective blocking of cysteine residues in protein engineering, a 10‑ to 20‑fold molar excess of N‑ethylmaleimide over accessible –SH groups is prepared immediately before use in degassed 50 mM phosphate or Tris buffer, pH 7.0–7.5. The mixture is incubated at 4 °C for 30 min; longer reaction times do not improve blocking efficiency because the reagent undergoes simultaneous hydrolysis. At 25 °C and pH 7.4, the pseudo‑first‑order hydrolysis rate constant is approximately 0.12 h⁻¹, corresponding to a half‑life of 8 h. Consequently, stock solutions held at room temperature for more than 1 h are discarded in regulated GMP environments. Unreacted NEM is quenched with a 5‑fold molar excess of β‑mercaptoethanol and removed by desalting. Using this protocol, residual amidase activity measured in azo‑dye release assays has been reduced to ≤ 0.5% of the native value.

    Thermal and Hydrolytic Behaviour Under Industrial Processing Conditions

    Incorporation of N‑ethylmaleimide into polyolefin backbones via peroxide‑initiated grafting utilises the same Michael‑acceptor character but imposes process‑related stress absent in bioconjugation. Co‑rotating twin‑screw extruders (L/D ratio 40) operating at screw speeds of 200–300 rpm must maintain barrel zone temperatures between 160 °C and 200 °C to achieve complete melting of polypropylene (MFI 2–25 g·10 min⁻¹, ASTM D1238, 230 °C/2.16 kg). At these temperatures the maleimide ring remains kinetically stable, but traces of water present in the feedstock (0.05–0.2%) promote ring‑opening to the corresponding maleamic acid, reducing graft‑to efficiency. The low melting point of NEM (45 °C) is advantageous here: it can be metered as a molten liquid through a heated injection port at 60 °C, avoiding the need for a separate side‑feeder required for higher‑melting maleimides. In a direct comparison with N‑methylmaleimide (mp 94–96 °C), which demands pre‑melting in a jacketed hopper maintained at 105 °C, N‑ethylmaleimide reduces auxiliary heater energy consumption by an estimated 30% and shortens start‑up purge time by 15 min per batch.

    The hydrolytic sensitivity, however, restricts processing of NEM‑grafted extrudates to inline pelletising lines equipped with dry‑air drying hoppers (dew point ≤ ‑40 °C). Pellets exposed to ambient humidity for > 2 h develop an adherent surface layer of maleamic acid that causes feeding instabilities in subsequent injection‑moulding steps and elevates the melt‑swirl gate residue. In a recorded manufacturing campaign, replacing N‑phenylmaleimide (mp 89–91 °C) with N‑ethylmaleimide resulted in a 7% drop in graft yield when the cooling water bath temperature exceeded 15 °C, traced to retro‑Michael depolymerisation catalysed by residual acidity. These boundaries establish that NEM is best suited for continuous compound lines where a closed, moisture‑controlled environment can be maintained from the liquid‑feed stage through to packaging.

    When N‑Ethylmaleimide Replaces N‑Methylmaleimide in Diels–Alder Adduct Formation

    The dienophilic reactivity of N‑substituted maleimides is modulated by both the steric environment of the nitrogen substituent and the inductive properties of the alkyl group. In [4+2] cycloaddition with cyclopentadiene, the ethyl homologue reacts marginally slower than the methyl analogue, an outcome attributable to increased steric demand around the imide dienophile rather than electronic differences. Published rate constants in dioxane at 25 °C indicate a second‑order value of approximately 1.8 × 10⁻³ L·mol⁻¹·s⁻¹ for N‑ethylmaleimide versus 2.3 × 10⁻³ L·mol⁻¹·s⁻¹ for N‑methylmaleimide. This 20% reduction in rate has practical consequences when the adduct is intended as a latent thermal precursor for deprotection: the slightly higher retardance allows processing of resin formulations that require a longer pot life at 100 °C. N‑phenylmaleimide, by contrast, exhibits a dienophilicity suppressed by steric and electronic factors, so much that it is poorly suited for room‑temperature Diels–Alder cross‑linking schemes unless supplemented with Lewis acid catalysts (e.g., Sc(OTf)₃ at 1 mol%). Therefore, N‑ethylmaleimide occupies an intermediate position, providing a balance of reactivity that can be tuned by solvent polarity and temperature without requiring catalytic activation.

    Beyond cycloaddition, the sulphydryl selectivity of N‑ethylmaleimide is routinely exploited to synthesise fluorescent probes. The ethyl capsule does not introduce a rigid aromatic ring that could quench fluorescence, making NEM‑derived conjugates of fluorescein‑5‑maleimide brighter than equivalent N‑phenylmaleimide constructs. In a standard labelling protocol, a 5‑fold molar excess of N‑ethylmaleimide‑activated fluorophore is reacted with a reduced antibody at pH 6.8 in 100 mM MES buffer containing 1 mM EDTA, followed by SEC purification on a Superdex 200 column. Dye‑to‑protein ratios determined spectrophotometrically at 494 nm and 280 nm consistently fall between 3.5 and 4.8, which is within the 4–6 range prescribed by commercial antibody‑drug‑conjugate platforms.

    ParameterN‑EthylmaleimideN‑MethylmaleimideN‑Phenylmaleimide
    Melting point (°C, DSC)45–4794–9689–91
    Hydrolytic half‑life at pH 7.4, 25 °C (h)81224
    Solubility in toluene at 25 °C (g·L⁻¹)20012080
    Reactivity ratio r₁ (styrene, bulk 60 °C)0.10 (styrene)–0.02 (NEM)0.090.030.050.10
    Preferred feeding method in reactive extrusionHeated liquid injection (60 °C)Side‑feeder with hot hopper (105 °C)Pre‑dissolved in monomer or auxiliary melt
    Key limitationMoisture sensitivity; short pot life in aqueous bufferHigher melt viscosity complicates meteringLimited aqueous solubility; fluorescence quenching

    Regulatory inventories for N‑ethylmaleimide include EINECS 204‑892‑0 and TSCA listing, with REACH registration volumes exceeding 10 tonnes·a⁻¹. For cross‑linking applications in food‑contact materials, however, specific migration limits have not been established, and the substance is excluded from positive lists under EU Regulation 10/2011. Users formulating adhesives or coatings that might contact aqueous foods must therefore verify that residual unreacted monomer is below detection limits of 0.01 mg·kg⁻¹ as determined by LC‑MS/MS.

    When experimental workflows demand thiol blocking under acidic conditions (e.g., pH 5.5 for selective labelling of exofacial cysteine residues), N‑ethylmaleimide remains active whereas iodoacetamide-based reagents lose reactivity. The maleimide ring opens only slowly below pH 6.0, extending the working life of the stock solution to 3 h at 4 °C. This pH‑dependent stability is exploited in continuous‑flow microreactors where NEM dissolved in 10 mM acetate buffer is co‑infused with protein at 2 μL·min⁻¹ and the adduct is monitored in‑line at 254 nm. Such configurations have been validated with ovalbumin and β‑lactoglobulin, achieving blocking yields >98% without precipitating the target protein.