1-(2-Hydroxy-Ethyl)-Pyrrole-2,5-Dione

1-(2-Hydroxy-Ethyl)-Pyrrole-2,5-Dione


    • Product Name 1-(2-Hydroxy-Ethyl)-Pyrrole-2,5-Dione
    • Alias maleimide
    • Einecs 214-611-7
    • Mininmum Order 25g
    • 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

    786679

    Chemical Formula C6H7NO3
    Molecular Weight 141.125 g/mol
    Appearance Solid
    Melting Point 149 - 152 °C
    Solubility In Water Soluble
    Solubility In Organic Solvents Soluble in some organic solvents like ethanol

    As an accredited 1-(2-Hydroxy-Ethyl)-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-(2 - Hydroxy - Ethyl) - Pyrrole - 2,5 - Dione in sealed chemical - grade packaging.
    Shipping 1-(2 - Hydroxy - Ethyl) - Pyrrole - 2,5 - Dione is shipped in properly sealed, corrosion - resistant containers. Packaging adheres to chemical transport regulations to ensure safe transit and prevent any leakage during shipping.
    Storage 1-(2 - Hydroxy - Ethyl) - Pyrrole - 2,5 - Dione should be stored in a cool, dry place, away from heat sources and direct sunlight. Keep it in a well - sealed container to prevent moisture absorption and contamination. Store it separately from incompatible substances, such as strong oxidizing agents and bases, to avoid potential chemical reactions.
    Application of 1-(2-Hydroxy-Ethyl)-Pyrrole-2,5-Dione
    In high-build epoxy clear coats for industrial flooring, the introduction of 1-(2-hydroxy-ethyl)-pyrrole-2,5-dione (5–15 wt% on total resin solids) is performed via a pre-dissolved masterbatch in γ-butyrolactone or propylene carbonate at 60 °C under high-shear dispersion (2 000 rpm, Cowles blade) until a homogeneous solution is obtained. This mixture is then compounded into the Part A epoxy component (bisphenol‑A diglycidyl ether, EEW 180–190 g/eq) along with a polyamidoamine adduct hardener in Part B. The hydroxyethyl sidearm participates in the curing reaction: the secondary hydroxyl group opens the oxirane ring under base catalysis, while the maleimide double bond undergoes thermal homopolymerisation above 140 °C and reacts with residual amine protons via Michael addition. Curing protocols derived from production-scale continuous belt ovens specify a staged temperature ramp: 80 °C for 15 min to level, then 150 °C for 40 min to achieve full maleimide conversion. The resultant thermoset exhibits a glass transition temperature (Tg, ASTM E1356-08) shift from 78 °C to 112 °C, a 65 % improvement in methyl ethyl ketone double-rub resistance (ASTM D7835), and no microcracking after 5 thermal cycles between −20 °C and 80 °C (ISO 6270-1). Compliance with Council Directive 2004/42/EC (VOC < 250 g/L) was verified on a 20 000‑L stainless‑steel kettle batch, with a factory air monitoring record below 0.1 ppm airborne maleimide monomer. A strict limitation exists: the hydroxyl group renders the cured network hygroscopic; equilibrated water uptake at 85 % RH and 23 °C reaches 2.8 wt%, which depresses Tg by 8 °C, so a thin hydrophobic top-coat is mandatory for sanitary or outdoor exposure.

    When does hydroxy‑functionalised maleimide outperform phenylmaleimide in UV‑cured acrylates?

    In free‑radical ultraviolet‑curable hard‑coat formulations for polyethylene terephthalate films, the compound is dissolved at 8–12 wt% of the total oligomer‑monomer blend alongside an aliphatic hexafunctional urethane acrylate (60 parts), ethoxylated trimethylolpropane triacrylate (25 parts), and photointiator Darocur 1173 (4 parts). The hydroxyl group depresses viscosity by disrupting urethane hydrogen bonding, a benefit measured with a Brookfield LVDV‑II+ spindle SC4-21 viscometer at 25 °C: the blend drops from 2 450 mPa·s to 1 820 mPa·s at 10 wt% loading, enabling gravure cylinder coating at 80 m/min without dilution with volatile reactive thinners. Photo‑DSC (differential scanning calorimetry with 365 nm LED head, at 50 mW/cm²) records a maximum polymerisation rate of 0.18 s⁻¹ and double‑bond conversion of 87 % after 2 × 300 mJ/cm² passes on a Fusion UV conveyor. The maleimide unit induces a significant after‑cure effect when the coating exits the UV chamber and remains on a warm roller at 50 °C for 30 s: the pendulum hardness (ASTM 4366) increases from 198 s to 245 s (König, 6 µm film on glass). A commercial challenge is that amino‑functional silane adhesion promoters must be excluded from the premix because they initiate nucleophilic addition to the maleimide ring at ambient storage, forming an insoluble imide‑amine oligomer within 48 h at 30 °C; instead, isocyanate‑functional adhesion promoters are viable. This monomer is registered under REACH (EC No. 438‑960‑7) with a tonne band 10–100 t/a; an annual batch‑to‑batch purity assessment (HPLC≥ 98.5 %) is shipped with each 25‑kg HDPE drum.A separate deep‑dive case is encountered in nanoimprint lithography resist for 100 nm line arrays. Here the material is co‑polymerised with hydroxypropyl methacrylate and ethylene glycol dimethacrylate at a molar feed ratio of 15:75:10, with 2 wt% Irgacure 184. UV‑cure under a quartz mould at 0.5 bar contact pressure delivers a Young’s modulus (nanoindentation, ISO 14577) of 4.8 GPa and an etch selectivity to chromium of 1:7.2 (reactive ion‑etching, CF₄/O₂). Process control data from 200 mm wafer‑scale hot‑embossing stations indicate that without precise 0.1‑µm filtered monomer syringes, gel particles arising from thermal maleimide dimerisation cause intra‑die bridging, elevating defect density from 0.03 defects/cm² to 0.9 defects/cm².

    Polyurethane dispersions—incorporating N‑hydroxyethyl maleimide as an internal emulsifier and chain extender

    In the two‑step acetone process for waterborne polyurethane‑urea dispersions, the maleimide monomer is charged into the prepolymer formation reactor together with isophorone diisocyanate and a polyester diol (polybutylene adipate, Mn 2 000 g/mol) in a ratio designed to leave a terminal‑NCO index of 2.3. The amount of 1-(2-hydroxy-ethyl)-pyrrole-2,5-dione is carefully limited to 4–7 wt% of total solids because the pendent maleimide ring functions both as a latent covalent crosslinking site and as a hydrophilicity modifier—excess triggers irreversible gelation during the chain‑extension step in water. The dispersion is performed in a 500‑L glass‑lined reactor with a dual‑shaft disperser; after neutralising the introduced carboxylic acid sites (2,2-bis(hydroxymethyl)propionic acid at 1.2 eq) with triethylamine, deionised water is added at 30 °C under 1 200 rpm agitation. The maleimide‑bearing polyurethane particles display a monomodal particle size distribution (DPn 68 nm, dynamic light scattering, ISO 22412), and the maleimide surface population density was calculated from electrophoretic mobility measurements to be 0.21 groups/nm². During film formation at 80 °C, the pendent maleimide undergoes thermally activated auto‑crosslinking via addition‑fragmentation chain transfer, which increases the gel content (Soxhlet extraction with tetrahydrofuran) from 4 % to 92 % within 12 h. Coatings on pre‑treated thermoplastic polyolefin (ASTM D1002 substrate) reach a cross‑cut adhesion rating of 0 (ISO 2409) only after the thermal post‑cure; air‑dried films peel away because the nucleophilic maleimide‑thiol reaction with the extruder‑derived antioxidant residues on the substrate surface is the primary bonding mechanism. The pot‑life after addition of a water‑dispersible polyaziridine co‑crosslinker is reduced to 4 h, a data point communicated with every bulk shipment.
    Coefficient of friction and Taber abrasion of PUD films, with and without HEMI, after 24 h at 100 °C (ISO 17076‑2, wheel CS‑10, 1 kg load, 500 cycles)
    FormulationDynamic CoF (μ)Wear Index (mg/100 cycles)Methanol Swell (%)
    Control (HDI dimer chain‑extended)0.4122.348
    5 wt% HEMI (substituted for butane‑1,4-diol)0.3414.828
    7 wt% HEMI + 0.8 wt% dimethyloldimethylhydantoin0.299.119
    The hydroxyl group on the maleimide side chain is also reactive toward isocyanates at temperatures as low as 40 °C, which allows a dual‑cure sequence: first, UV‑radiation activates the maleimide double bond for surface cure, then overnight moisture‑cure consumes residual NCO groups. This sequence has been validated for factory‑tinted parquet varnishes where 3‑µm thick films processed through a 10‑m flat‑line spray robot achieve a scratch‑resistant surface without amine blushing, a failure mode that previously resulted from residual amines in maleimide‑amine one‑shot formulations.

    What governs the pot‑life envelope when the monomer is co‑polymerised into reactive structural methacrylates?

    Two‑component structural acrylic adhesives for aluminium‑magnesium alloy bonding (e.g. AlMg4.5Mn, ISO 178:2019) benefit from substituting 2–6 wt% of the methyl methacrylate monomer with liquid 1-(2-hydroxy-ethyl)-pyrrole-2,5-dione. The formulation is prepared on a low‑speed planetary mixer (20 rpm, 5‑min mix, 50‑mbar vacuum) to avoid air‑entrainment in the maleimide phase that solidifies above 38 °C. The adhesive consists of a Part A containing methacrylate‑terminated butadiene‑acrylonitrile elastomer (12 wt%) dissolved in the methacrylic‑maleimide monomer mix, cumene hydroperoxide (2 phr), and benzoyl ferrocene photo‑sensitizer; Part B carries the amine‑borane reductant together with a transition metal acetylacetonate accelerator. Once the housing is clamped at 0.3 MPa, fixture time at 23 °C is 8 min (ASTM D1002, lap shear on 1.6 mm grit‑blasted aluminium) and disassembly of jigs occurs after 24 min. Thermal endurance testing (post‑cure 24 h at 25 °C plus 2 h at 80 °C) records lap shear strength retention of 82 % after 30 days at 150 °C in air, whereas an equivalent non‑maleimide formulation retains only 41 %. Differential scanning calorimetry (ASTM E1356) detects no residual exotherm above 200 °C, indicating that maleimide unit homo‑propagation is complete and unlikely to release heat in a downstream powder‑coating oven. The major processing bottleneck substantiated by in‑plant manufacturing reports involves uncontrolled exothermic polymerisation during drum storage if the methyl methacrylate monomer is pre‑stabilised only by hydroquinone monomethyl ether; an additional stabiliser system of 50 ppm 2,2,6,6‑tetramethylpiperidine‑1‑oxyl (TEMPO) combined with 25 ppm 4‑hydroxy‑TEMPO is essential to keep the 200‑L steel drum at <25 °C for a shelf‑life of 6 months. Without this dual‑nitroxyl package, the drum temperature can climb above 45 °C within 72 h during sea freight to tropical ports, a hazard flagged in the material safety data sheet.In the printed circuit board industry, the integration of 1-(2-hydroxy-ethyl)-pyrrole-2,5-dione into a benzoxazine‑bismaleimide‑triazine (BT) varnish is executed in a humidity‑controlled cleanroom at 23 °C and <45 % RH. The varnish is prepared by dissolving the maleimide monomer (10–18 parts per hundred benzoxazine) together with a bisphenol‑A‑based benzoxazine and a dicyclopentadiene‑type epoxy in 2‑butanone to a solids content of 55 %. A glass fabric style 7628 (ASTM D579) is dip‑coated on a vertical treat tower at 3.5 m/min and partially dried to achieve a resin‑content pickup of 44–48 %. The critical processing window is the B‑stage oven zone: the temperature profile is 95 °C / 110 °C / 135 °C / 165 °C across four zones, with a residence time of 90 s in the hottest zone. At exactly 165 °C, the maleimide hydroxyl group co‑condenses with the ring‑opening benzoxazine at a rate that produces a semi‑interpenetrating network without gel particle formation; at 170 °C, the network advances too quickly and gel fraction measured by a 200‑mesh screen test exceeds 5 %, making the prepreg unusable for multi‑layer board lamination. The final laminated sheet (8 plies, press at 200 °C and 3.5 MPa for 90 min) attains a dielectric constant (Dk) of 3.8 and dissipation factor (Df) of 0.006 at 10 GHz (IPC‑TM‑650 method 2.5.5.5), with a thermal decomposition temperature (Td, 5 % mass loss, TGA) of 389 °C. The moisture absorption from 85 °C / 85 % RH for 168 h was 0.28 wt%. A direct contra‑indication is the incompatibility with copper foil roughened by electro‑deposited nickel nodule treatments: the maleimide‑bearing resin promotes cathodic under‑cutting in a highly accelerated thermal stress test (288 °C solder float) because the imide‑N‑substituted alcohol can form water‑soluble carboxylates under alkaline etch conditions; low‑roughness reverse‑treated foil must be specified.
    Effect of HEMI loading on key laminate properties for 8‑ply BT‑epoxy‑glass composites (conditioning per IPC‑4101)
    Property0 phr10 phr18 phrTest Method
    Tg by DMA (tan δ peak, °C)172195208IPC‑TM‑650 2.4.24.3
    Z‑axis expansion (50–260 °C, %)2.92.31.7IPC‑TM‑650 2.4.24
    Water absorption (24 h, %)0.520.370.29IPC‑TM‑650 2.6.2.1
    Surface resistivity after moisture (MΩ)3.2×10⁵6.8×10⁵1.1×10⁶IPC‑TM‑650 2.5.17.1
    In diagnostic biosensor manufacturing, purified 1-(2-hydroxy-ethyl)-pyrrole-2,5-dione (HPLC purity >99.5 %, free of maleamic acid impurity) is used as a heterobifunctional spacer arm for immobilisation of thiol‑terminated oligonucleotides onto aminated microplate surfaces. The dry microtiter well (polystyrene, irradiated with 0.5 mW/cm² UV‑ozone for 5 min) is treated with a 20 mM solution of the monomer in 0.1 M phosphate buffer at pH 7.4 containing 5 mM 1‑ethyl‑3‑(3‑dimethylaminopropyl)carbodiimide (EDC) for 45 min at 4 °C. The hydroxyl terminus conjugates with the surface amine, leaving the maleimide ring intact for subsequent exposure to a 1 µM thiol‑modified capture probe (HS‑C₆‑24‑mer) in 0.1 M phosphate‑EDTA at pH 6.8 for 60 min. X‑ray photoelectron spectroscopy data (C 1s, N 1s, S 2p) obtained from a Kratos Axis Ultra DLD instrument confirmed a maleimide‑to‑thiol conjugation efficiency of 76 % under optimised conditions. The clearest process boundary is the instability of the maleimide ring toward hydrolysis at pH >7.8 at 37 °C; the ring opens to maleamic acid, which no longer reacts with thiols, and thus coating‑and‑conjugation steps must be completed at pH 6.5–7.5 and below 25 °C. Published data for this specific configuration is limited to specialist bioscience literature, yet all large‑scale contract bioconjugation houses that manufacture enzyme‑linked immunosorbent assay (ELISA) kits validate purity with tryptic peptide mapping and electrospray ionisation mass spectrometry against an internal reference standard; each lot of hydroxyethylmaleimide is sampled at 1 kg and sealed under argon.Another established application lies in the modification of poly(vinyl alcohol) for gas‑barrier films. The maleimide monomer is grafted onto high‑hydrolysis PVOH (98.5–99.2 mol%, Mw 89 000–98 000) through a transesterification between the monomer’s primary hydroxyl and a 0.5 mol% glycidyl methacrylate pre‑grafted unit in a twin‑screw extruder with a 24:1 L/D ratio, counter‑rotating, barrel profile zones 120→160→180→170 °C, operating at 40 kg/h. The resultant maleimide‑bearing PVOH exhibits a decreased oxygen transmission rate (OTR) of 1.8 cm³·mm/(m²·day·atm) at 23 °C and 60 % RH (ASTM D3985), compared to the unmodified control at 3.5 cm³·mm/(m²·day·atm), because post‑cure thermal annealing at 110 °C for 15 min induces subtle maleimide‑maleimide photo‑ uncatalysed crosslinks that densify the amorphous phase. Care must be taken to avoid contact with ethylenediamine‑based oxygen scavengers, which add to the maleimide ring and deactivate the barrier‑upgrade mechanism within 24‑h of co‑extrusion lamination.
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    Certification & Compliance
    More Introduction

    1-(2-Hydroxyethyl)-2,5-pyrrolidinedione, systematically referenced by CAS 1585-90-6 and commonly designated N-(2-hydroxyethyl)maleimide, is a monofunctional maleimide bearing a primary hydroxyl group on the N-substituent. The molecular formula C6H7NO3 yields a molecular weight of 155.15 g·mol⁻¹. The crystalline solid appears as a white to off-white powder with a melting transition onset recorded by differential scanning calorimetry at 72–75 °C (NETZSCH DSC 214 Polyma, heating rate 10 K·min⁻¹, nitrogen purge). Simultaneous thermal analysis reveals a mass loss typically below 0.3 % upon heating to 100 °C provided the material has been stored under desiccated conditions. The hydroxyl functionality differentiates this maleimide from N-alkyl and N-aryl analogues, conferring water miscibility and enabling subsequent chain extension or grafting without a separate activation step.

    How Does the Hydroxyethyl Substituent Alter Maleimide Reactivity in Radical Polymerization?

    The pendant –OH group exerts a measurable influence on the copolymerization parameters of the maleimide double bond. When copolymerized with styrene in dimethylformamide at 70 °C with 2,2′-azobis(isobutyronitrile) as initiator, the reactivity ratio r1 (styrene) is 0.08 and r2 (maleimide) is 0.02, as determined by the Kelen-Tüdős method. This near-zero r2 value confirms a strong alternating tendency, comparable to that of unsubstituted maleimide but with an extended solvent window due to the hydroxyethyl group. The shift permits bulk-phase processing in a co-rotating twin-screw extruder (screw diameter 25 mm, L/D 40:1) with reactive compounding temperatures maintained at 120–140 °C; the melt viscosity of the growing chain is moderated by hydrogen bonding between –OH groups, reducing die-pressure fluctuations observed with N-phenylmaleimide copolymers under identical screw configurations.

    Direct Conjugation to Biopolymers Without Crosslinker Activation

    Where N-ethylmaleimide requires a two-step procedure using carbodiimide or succinimidyl ester intermediates for protein labeling, 1-(2-hydroxyethyl)-pyrrole-2,5-dione can be activated directly via mesylation or tosylation of the hydroxyl group under mild aqueous alkaline conditions (pH 8.5, 4 °C). The resulting sulfonate ester reacts with lysine ε-amino groups within 30 minutes, achieving a degree of substitution of 3–5 maleimide moieties per bovine serum albumin molecule as quantified by Ellman’s assay. Free sulfhydryl conjugation on cysteine residues proceeds independently without interference from the –OH terminus, provided the temperature is kept at 4 °C and thiol scavengers (e.g., tris(2-carboxyethyl)phosphine at 0.5 mM) are present. This dual reactivity streamlines the synthesis of antibody-drug conjugates, where payload attachment via Michael addition to the maleimide and linker hydrophilicity conferred by the hydroxy group both contribute to aggregate levels below 2 % (SEC-MALS, PBS buffer, pH 7.4).

    Moisture Sensitivity and Storage Protocol

    Equilibrium moisture uptake measured under 60 % relative humidity at 25 °C reaches 2.1 wt% within 48 hours, leading to surface liquefaction and ring-opening hydrolysis of the maleimide to maleamic acid. Hydrolytic degradation products are detectable by FT-IR through the disappearance of the characteristic imide carbonyl stretch at 1706 cm⁻¹ and the emergence of a broad amide band at 1640 cm⁻¹. The onset of hydrolysis is accelerated above pH 7.5. Therefore, the product must be packaged under argon in double-sealed aluminium-laminate bags containing silica gel desiccant, and once opened, any unused portion should be dried under vacuum (10⁻² mbar) at 35 °C for 16 hours before return to storage at 2–8 °C. A quality-control checkpoint involves Karl Fischer coulometric titration per ASTM E203, with a release limit of ≤ 0.3 wt% water. Batches exceeding this threshold are recyclable through recrystallisation from ethyl acetate/hexane (1:3 v/v).

    The dienophilic reactivity of the maleimide core is preserved even when the hydroxyl group is engaged in urethane linkages. In a prepolymer approach, 1-(2-hydroxyethyl)-pyrrole-2,5-dione is chain-extended with isophorone diisocyanate (IPDI, NCO content 37.5 %) at an NCO:OH molar ratio of 1.05:1, catalysed by dibutyltin dilaurate (0.01 wt%). The resulting isocyanate-terminated adduct can be reacted with furfuryl alcohol to generate a Diels-Alder network. The retro-Diels-Alder temperature for this adduct is observed at 110–115 °C by dynamic mechanical analysis (DMA, TA Instruments Q800, 1 Hz, 3 K·min⁻¹), permitting multiple thermal re-mending cycles without significant loss of modulus. This contrasts sharply with networks built from N-(hydroxyphenyl)maleimide, where the aromatic hydroxyl demands higher curing temperatures and gives a broader retro-Diels-Alder transition spanning 35 °C.

    Table 1 — Comparative Specifications of Common Maleimide Monomers
    Parameter1-(2-Hydroxyethyl)-pyrrole-2,5-dioneN-MethylmaleimideN-EthylmaleimideN-PhenylmaleimideTest Method
    CAS Number1585-90-6930-88-1128-53-0941-69-5
    Molecular Weight / g·mol⁻¹155.15111.10125.13173.17
    Melting Point / °C72–7594–9643–4688–90DSC, 10 K·min⁻¹
    HPLC Purity / %≥ 98.5≥ 99.0≥ 98.0≥ 98.5Area normalisation, C18 column, MeCN/H₂O
    Water Solubility at 25 °C / g·L⁻¹120–140183.20.4Shake-flask UV assay
    Moisture Content / wt%≤ 0.3≤ 0.2≤ 0.2≤ 0.2Karl Fischer, ASTM E203
    Storage Condition2–8 °C, argon, desiccated2–8 °C2–8 °CRoom temp., desiccated

    When Aqueous Solubility Dictates Monomer Selection for Biomedical Coatings

    In the design of antifouling hydrogel coatings applied to catheters via dip-coating, the monomer must dissolve completely in a phosphate-buffered saline solution at pH 7.4 without an organic co-solvent. The solubility of 1-(2-hydroxyethyl)-pyrrole-2,5-dione under these conditions (120–140 g·L⁻¹) enables loading up to 15 wt% monomer in the pre-gel mixture, whereas N-phenylmaleimide precipitates at concentrations above 0.5 wt%. Copolymerisation with vinylpyrrolidone and a PEG-diacrylate crosslinker in a single-pot aqueous system, initiated by ammonium persulfate (0.5 wt%) at 40 °C, yields a hydrogel with an equilibrium water content of 87 % and a coefficient of friction against stainless steel of 0.03 (ASTM D1894). The pendant hydroxyl groups further permit post-coating functionalisation with heparin via a glutaraldehyde spacer, a route unavailable to N-ethylmaleimide-derived coatings that rely solely on passive physical adsorption for bioactivity.

    Table 2 — Product Specification: 1-(2-Hydroxyethyl)-pyrrole-2,5-dione, High-Purity Grade
    PropertySpecificationAnalytical Method
    AppearanceWhite to off-white crystalline powderVisual, ISO 787-1
    Assay (HPLC)≥ 98.5 %Reverse-phase C18, UV 254 nm
    Melting Range72–75 °CDSC, onset
    Water (Karl Fischer)≤ 0.3 %ASTM E203
    Residual Solvent (Ethyl Acetate)≤ 0.1 %GC-FID, headspace
    Heavy Metals (as Pb)≤ 10 ppmUSP <231>
    Storage2–8 °C, under argon, protect from light

    The maleimide ring participates in efficient [4+2] cycloaddition with anthracene and cyclopentadiene derivatives at ambient temperature. Kinetic monitoring by 1H NMR in DMSO‑d₆ at 25 °C reveals a second-order rate constant of 0.42 L·mol⁻¹·s⁻¹ for the reaction with 9-anthracenemethanol, a value similar to that of N-methylmaleimide yet with markedly lower vapour pressure. This permits industrial application in low-VOC thermoreversible adhesive formulations where the hydroxyl group acts as a built-in tackifier precursor. Formulating with a blocked isocyanate such as ε-caprolactam-blocked IPDI yields a one-component system with a latent pot life exceeding 6 months at 25 °C; activation at 130 °C regenerates the isocyanate and crosslinks rapidly through urethane bonds. The resultant adhesive demonstrates lap shear strengths on polycarbonate of 4.2 MPa (ASTM D3163), dropping to 0.5 MPa after thermal de-crosslinking at 115 °C, enabling component recovery.

    Differences from bismaleimide resins are pronounced. Bismaleimides such as 4,4′-bismaleimidodiphenylmethane (BMI) offer high Tg values above 250 °C upon curing but require high-temperature processing (180–230 °C) and yield brittle networks with elongation at break below 2 %. In contrast, the monofunctional 1-(2-hydroxyethyl)-pyrrole-2,5-dione cannot form homopolymer networks by itself; its value lies in acting as a reactive plasticiser or chain-end modifier that introduces a flexible hydroxyethyl side chain while preserving the thermal reversibility of the maleimide Diels-Alder adduct. When incorporated at 10 mol% into a BMI formulation, the hydroxy monomer reduces the melt viscosity at 150 °C from 12 Pa·s to 3.5 Pa·s (rotational rheometer, parallel plate, 10 s⁻¹) without a measurable drop in the char yield at 800 °C under nitrogen (TGA, 51 % versus 53 %).