|
HS Code |
202382 |
| Chemical Formula | C8H11NO4 |
| Molecular Weight | 185.18 |
| Iupac Name | 1-(2-(2-Hydroxyethoxy)ethyl)-1H-pyrrole-2,5-dione |
| Appearance | Solid (likely, but exact depends on conditions) |
| Physical State At Room Temp | Solid |
| Solubility In Water | Limited solubility expected due to polar - non - polar balance |
| Solubility In Organic Solvents | Soluble in polar organic solvents like ethanol, methanol |
As an accredited 1-(2-(2-Hydroxyethoxy)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 | 100g of 1-(2-(2 - Hydroxyethoxy)Ethyl)-1H - Pyrrole - 2,5 - Dione in sealed chemical - grade bags. |
| Shipping | 1-(2-(2-Hydroxyethoxy)Ethyl)-1H-Pyrrole-2,5-Dione is shipped with strict adherence to chemical transportation regulations. Packaged securely to prevent leakage, it's transported by carriers experienced in handling such chemicals. |
| Storage | 1-(2-(2 - Hydroxyethoxy)Ethyl)-1H - Pyrrole - 2,5 - Dione should be stored in a cool, dry place away from heat and ignition sources. Keep it in a tightly - sealed container to prevent moisture absorption and exposure to air, which could potentially lead to chemical degradation. Store it separately from incompatible substances to avoid reactions. |
What Modifies the Fracture Toughness of Bismaleimide Laminates Without Compromising Hot/Wet Properties?Replacing 15–30 mol% of 4,4′-bismaleimidodiphenylmethane (BMI-1) with 1-(2-(2-hydroxyethoxy)ethyl)-1H-pyrrole-2,5-dione (HEEP-MI) in a melt prepolymerization at 135–145 °C for 18–25 min introduces a flexible oxyethylene spacer and a pendant primary hydroxyl into the network backbone. The hydroxyl group participates in secondary hydrogen bonding with imide carbonyls, increasing Mode I interlaminar fracture toughness (GIC) by 22–38% as measured per ASTM D5528-13 on unidirectional T700 carbon fiber prepregs cured in an autoclave at 0.6 MPa with a 2 °C/min ramp to 250 °C and a 4 h dwell. The prepolymer viscosity at 120 °C rises from 0.8 Pa·s to 1.4–2.1 Pa·s at 25 mol% substitution, a range that remains processable on a hot-melt prepregger with a reverse-roll coater gap set to 180–220 µm. The critical processing constraint is moisture management: the monomer is hygroscopic, absorbing ≥0.5 wt% water at 50% RH within 20 min. Pre-drying flakes in a vacuum oven at 60 °C and ≤5 mbar for 6 h is mandatory; residual moisture above 0.08 wt% (Karl Fischer titration, ASTM E203) generates microvoids with diameters 5–15 µm observable in C-scan attenuation maps, reducing short-beam shear strength (ASTM D2344) by 12–18% after a 72 h water boil. Elevated wet Tg retention—91% versus 78% for the unmodified BMI control—is attributed to ether linkages that lower equilibrium moisture saturation from 4.2% to 3.5%. Incompatibility arises with amine-based catalysts such as 2,4,6-tris(dimethylaminomethyl)phenol: the maleimide ring undergoes premature Michael addition during mixing, elevating the exotherm peak onset by ≥15 °C and shortening pot life to less than 8 min at 120 °C. For this reason, transition metal acetylacetonate catalysts (Co(acac)3 at 0.05 phr) are preferred, enabling a stable B-staging window of 45–60 min. The cured network exhibits a plateau storage modulus (E′) at 40 °C of 3.8–4.1 GPa by dynamic mechanical analysis (ASTM E1640, single cantilever, 1 Hz, 3 °C/min). A subtle β-transition appears at −85 °C associated with the oxyethylene segment, contributing to impact resistance. Flexural strength (ASTM D790-17, span-to-thickness ratio 32:1) reaches 142–155 MPa at 25 mol% HEEP-MI, exceeding the unmodified baseline of 118 MPa. However, above 30 mol% substitution, the crosslink density (νe) calculated from rubbery plateau modulus according to DMA decreases from 2.4 × 10⁻³ mol/cm³ to 1.6 × 10⁻³ mol/cm³, and the dry Tg drops below 210 °C—unacceptable for aerospace engine nacelle applications requiring >220 °C dry service temperature per SAE AMS3897.
When co-curing with epoxy prepregging systems, the hydroxyl group on HEEP-MI grafts onto oxirane rings at post-cure temperatures above 180 °C, improving interlayer adhesion by 0.8 N/mm in climbing drum peel (ASTM D1781) compared to standard BMI-epoxy interfaces. This reactivity forces a change in factory lay-up sequencing: HEEP-MI-modified BMI films must be positioned no closer than two plies from the epoxy interface layer to avoid excessive co-reaction that generates brittle gradient zones, detectable as microcrack networks by edge-face microscopy at 100× magnification after 100 thermal cycles between −55 °C and 180 °C. Addition of 0.2–0.5 wt% of the monomer to a cationically curing cycloaliphatic epoxy system (3,4-epoxycyclohexylmethyl-3′,4′-epoxycyclohexane carboxylate) sensitizes the formulation to UV LED sources emitting at 365 nm and 385 nm. The maleimide chromophore absorbs in the 290–340 nm range and, when combined with a 1.5 phr diaryliodonium hexafluorophosphate initiator and 0.25 phr isopropylthioxanthone sensitizer, acts as a co-initiator that generates singlet oxygen and radical cations, boosting the double-bond conversion of the epoxy to 88% (measured by real-time FTIR monitoring the oxirane band at 790 cm⁻¹) under a dose of 2.5 J/cm² in a conveyorized LED exposure unit with peak irradiance 8 W/cm². Without HEEP-MI, conversion plateaus at 67%. The hydroxyethoxy chain participates in chain-transfer reactions that delay gelation, extending the open time under nitrogen blanket from 14 s to 21 s—a meaningful increase for ink-jet printhead idle recovery. Substrate adhesion on corona-treated polyethylene terephthalate film (52 dyn/cm surface energy) improves from 2B to 5B in cross-cut tape tests (ASTM D3359-17) at coating thicknesses of 8–12 µm. This is not merely an acid-base interaction: pendant hydroxyl groups form molecular complexes with PET carbonyls, observable as a +8 cm⁻¹ shift in the ester C=O stretching band via ATR-FTIR spectroscopy. A practical failure mode occurs when HEEP-MI loading exceeds 0.8 wt%—the residual unsaturation darkens the coating to a Yellowness Index (ASTM E313) above 4.5, exceeding the maximum 2.0 allowed for overprint varnishes on cosmetic packaging. The formulation must also be stored in amber vessels at ≤25 °C; a 48 h stability test at 40 °C shows 12% viscosity climb due to thermal homopolymerization unless stabilized with 200 ppm 4-methoxyphenol. Injectable PEG-Heparin Hydrogels Crosslinked via Michael AdditionMaleimide-terminated multi-arm polyethylene glycol (4-arm PEG-MI, Mn 10 kDa) crosslinked with thiolated heparin (Hep-SH, degree of substitution 22%) incorporates 1-(2-(2-hydroxyethoxy)ethyl)-1H-pyrrole-2,5-dione as a monofunctional chain-end regulator to control gel time and reduce burst release of encapsulated basic fibroblast growth factor (bFGF). The monomer is added at a molar ratio of 0.08–0.25 relative to total maleimide groups. The reaction is conducted in phosphate-buffered saline at pH 7.4 and 37 °C; the gel point, determined by the inverted vial method, shifts from 45 s (0 regulatory monomer) to 110 s at a 0.25 ratio. This allows an injection window of 55–70 s through a 27G needle before a viscosity of 200 Pa·s is reached, as measured on a stress-controlled rheometer (cone-plate 40 mm, 1°, 1 Hz). The hydroxyl tail does not participate in gelation but increases water uptake at equilibrium swelling from 18 g/g to 29 g/g, which is advantageous for nutrient convection but must be capped within a crosslink density that maintains storage modulus above 800 Pa, a threshold required for cardiomyocyte alignment published in Acta Biomaterialia (2020, 102, 375–389). Cytocompatibility per ISO 10993-5:2009 extract dilution assay on L929 fibroblasts shows no cytotoxic reduction in viability down to 100% extract concentration; however, unreacted monomer residues above 15 ppm (quantified via HPLC-UV at 254 nm) induce a ≥20% loss in metabolic activity. Post-synthesis dialysis in regenerated cellulose tubing (MWCO 1 kDa) against deionized water for 36 h with six changes reduces free monomer below the 5 ppm detection limit. Sterilization by gamma irradiation at 25 kGy causes 6% chain scission in the PEG backbone, increasing the sol fraction to 4.2%; aseptically filtered liquid components with a dual-syringe mixing system are therefore preferred in clinical settings. The immediate contraindication is combination with free cysteine-containing media supplements: thiol-maleimide consumption depletes gel crosslinks, and storage modulus degrades by 40% within 48 h at 37 °C. The monomer is grafted onto electrophilically polished 316LVM stainless steel coronary stent surfaces at 0.8–1.2 mg/cm² via a two-step process: immersion in a 2% w/v solution of HEEP-MI in anhydrous tetrahydrofuran containing 0.1% v/v triethylamine at 25 °C for 60 min, followed by thorough rinsing in isopropanol and vacuum drying at 40 °C. The alkoxide formed from the hydroxyethyl group attacks the passive chromium oxide layer, creating Fe–O–C linkages verified by XPS peaks at 530.1 eV (O 1s) and a Fe 2p3/2 shift of +0.6 eV. After rinsing, the pendant maleimide couples with a recombinant human thrombomodulin (rhTM) variant through a cysteine tag at pH 6.8 (MES buffer) for 3 h, achieving a surface density of 0.22 µg/cm² (radiolabeled 125I assay). The resulting stent resists platelet adhesion by 97% relative to bare metal in a baboon arteriovenous shunt model (data on file, institutional protocol UTK 05-1256), with activated clotting time remaining within ±12% of baseline. A manufacturing bottleneck is sensitivity to ambient humidity during the initial silanization step: at relative humidity above 60%, water competes with the hydroxyl nucleophile, and maleimide density drops to 0.3 mg/cm² or lower, causing patchy protein conjugation visible as non-fluorescent zones in confocal microscopy after FITC-labelled thrombomodulin incubation. The process protocol mandates maintaining the glovebox atmosphere at ≤15% RH and monitoring reactor dew point continuously with a chilled-mirror hygrometer. When Dielectric Constant Below 2.5 is Mandatory in High-Frequency SubstratesA reactive modifier for the polyphenylene oxide (PPO)/triallyl isocyanurate (TAIC) system used in millimeter-wave printed circuit boards, 1-(2-(2-hydroxyethoxy)ethyl)-1H-pyrrole-2,5-dione serves as a crosslinking co-agent that undergoes radical coupling during the peroxide cure step while its hydroxyethyl chain provides a site for subsequent acetylation to eliminate polarity. The base formulation consists of 70 parts poly(2,6-dimethyl-1,4-phenylene oxide) (Mw 25 kDa), 25 parts TAIC, 5 parts HEEP-MI, and 1.2 parts dicumyl peroxide (DCP, 98% purity). After compounding on a co-rotating twin-screw extruder (screw diameter 26 mm, L/D 44, barrel temperatures 200–260 °C), the extrudate is pelletized, and the dielectric constant (εr) at 10 GHz measured by split-post dielectric resonator per IPC-TM-650 2.5.5.5 stands at 2.72—above the desired 2.50 threshold for 5G antenna substrates. The reactive hydroxyl is then capped in a heterogeneous acetylation bath: pellets are swollen in a mixture of acetic anhydride/pyridine (3:1 v/v) with 0.05 wt% 4-dimethylaminopyridine catalyst at 60 °C for 90 min, rinsed in acetone, and dried. Post-acetylation εr drops to 2.46 and dissipation factor (tan δ) from 0.0054 to 0.0038. Moisture absorption ( IPC-TM-650 2.6.2.1, 23 °C, 24 h immersion) decreases from 0.32% to 0.14%, a critical improvement given that every 0.1% increase in moisture raises εr by approximately 0.03 units. The crosslinked network exhibits a coefficient of thermal expansion in the z-axis (αz, TMA, 10 °C/min) of 48 ppm/°C below Tg and 98 ppm/°C above Tg (185 °C by TMA inflection).
The copper peel strength improvement is attributable to the maleimide residue that complexates with cuprous ions at the copper/epoxy-prepreg interface formed during lamination with brominated epoxy bonding sheets. This raises the overall substrate rating to UL 94 V-0 with a minimum total burning time of 42 s for five samples (UL 94). The acetylation step introduces a manufacturing challenge: residual pyridine odor must be stripped by passing the pellets through a tubular vacuum devolatilizer at 120 °C and 15 mbar with a residence time of 14–18 min. If residual pyridine exceeds 20 ppm, as determined by GC headspace analysis, downstream lamination at 190 °C generates blisters visible at 50× magnification in microsection. This system is incompatible with inorganic fillers such as alumina trihydrate that catalyze ester hydrolysis at the processing temperature; therefore, only calcined silica fillers with Fe2O3 content below 0.01% are permissible. A non-migrating internal anti-block agent for blown polyethylene films is prepared by melt-grafting 0.3–0.7 wt% of HEEP-MI onto low-density polyethylene (LDPE, MI 2 g/10 min, 190 °C/2.16 kg) in a continuous mixer at 185 °C with 0.05 phr of 2,5-dimethyl-2,5-di(tert-butylperoxy)hexane as initiator. The grafted chains concentrate at the film surface during annealing at 80 °C for 12 h, driven by the thermodynamic incompatibility of the polar oxyethylene segment with the polyolefin matrix; advancing contact angle by water (ASTM D5946) decreases from 102° to 82° without printing damage. Scanning force microscopy performed with a hydrophilic probe reveals a surface coverage of discrete domains 40–80 nm in diameter at a number density of 12–18 per µm². The hydroxyl groups, once film is corona-treated at 1.5 kW and 0.3 m/s line speed, crosslink to water-based polyurethane ink binders (e.g., Neorez R-600) during forced hot-air drying at 70 °C for 3 s, boosting tape adhesion from 0.14 N/cm to 0.41 N/cm as per FINAT FTM 1. In the absence of the graft, corona decay causes adhesion to drop by 0.12 N/cm after 72 h aging; with HEEP-MI, the loss is only 0.04 N/cm. The critical limitation is uncontrolled gel formation during melt grafting if the maleimide homopolymerizes; process control requires that the residence time in the mixing zone does not exceed 75 s and that the initiator half-life is entirely consumed within that window. Equipment cleanup is carried out with purged polypropylene at 210 °C for 20 min to flush out residual crosslinked specks that otherwise appear in subsequent runs as fisheyes of ≥200 µm. |
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The functional maleimide derivative 1-(2-(2-hydroxyethoxy)ethyl)-1H-pyrrole-2,5-dione (systematic IUPAC name; empirical formula C9H13NO4, molecular weight 199.20 g/mol) is supplied as a clear, colourless to pale yellow viscous liquid. The molecule integrates a maleimide dienophile/dipolarophile with a terminal primary hydroxyl group through a diethylene glycol spacer of exactly two ethoxy units. This structural feature delivers a linker length of 8 backbone atoms between the imide nitrogen and the hydroxyl oxygen, creating a reactive bifunctional agent that partitions readily into aqueous media while retaining the expected thiol-reactive and free-radical-polymerisable character of the maleimide ring. Unlike N-alkyl maleimides that lack a pendant functional group, this compound presents a nucleophilic hydroxide suitable for urethane formation, esterification, or further derivatisation without post-polymerisation deprotection steps.
| Property | Value / Specification | Method |
|---|---|---|
| Appearance | Clear, colourless to pale yellow viscous liquid | Visual (D65 illumination) |
| Purity (maleimide content) | ≥ 95.0 area% | HPLC-UV at 210 nm; C18 column, isocratic H2O/MeCN (70:30 v/v) + 0.1% TFA |
| Water content | < 0.5 wt% | ISO 15512 (Karl Fischer coulometric titration) |
| Density at 25 °C | 1.21 g/cm³ | ISO 12185 |
| Refractive index nD20 | 1.495 | ISO 489 (Abbe refractometer) |
| Phase transition (DSC) | Broad endotherm between ‑20 °C and 10 °C; no sharp melting peak | ISO 11357-3; heating rate 10 K/min, N2 atmosphere |
| Stabiliser (BHT) | 100 – 300 ppm | GC-FID after methanolic extraction |
| Solubility (water, 25 °C) | > 500 mg/mL | Equilibrium dissolution, filtrate assay by HPLC-UV |
The low melting region and the hygroscopic nature of the terminal hydroxyl group demand storage protocols that prevent water ingress. Unopened containers are recommended to be kept at ‑20 °C under nitrogen; actual retest data on lots stored 12 months under these conditions show maleimide purity loss of less than 1.0 area%. Once opened, the material should be transferred into a glovebox with < 1 ppm H2O and < 1 ppm O2 to avoid ring hydrolysis and premature free-radical polymerisation. When a water content exceeding 500 ppm is detected by Karl Fischer titration, azeotropic drying with anhydrous toluene followed by vacuum stripping at 0.1 mbar and 40 °C restores functionality to within specification.
Incorporating the diethylene glycol maleimide into aqueous free-radical homo- or copolymerisation requires careful control of the initiation pH. Pendent maleimide rings undergo irreversible hydrolysis to maleamic acid at pH > 7.5, a side reaction that competes with propagation. Buffer systems based on 100 mM sodium phosphate adjusted to pH 6.8 ± 0.2 are frequently employed for solution polymerisations initiated by 2,2′-azobis(2-methylpropionamidine) dihydrochloride (V-50). At 60 °C, with a total monomer concentration of 1.5 mol/L and initiator loading of 0.5 mol% relative to combined monomers, the maleimide comonomer incorporates with an apparent reactivity ratio rmaleimide ≈ 0.02 when paired with a strongly electron-rich comonomer such as N-vinylpyrrolidone. The resulting tendency toward alternating sequences can cause significant compositional drift in batch mode; therefore, starve-fed addition of the maleimide component via a syringe pump at a rate matching its instantaneous consumption is recommended for compositionally homogeneous copolymers. Under these semi-batch conditions, copolymers with controlled hydroxyl content between 2 and 15 mol% have been obtained, exhibiting number-average molecular weights (Mn) of 25 000–55 000 Da when measured by size-exclusion chromatography in DMF containing 0.1% LiBr with narrow-dispersity poly(ethylene glycol) calibrants.
Reversible addition-fragmentation chain transfer (RAFT) polymerization of the hydroxyl-terminated maleimide derivative with methacrylate comonomers introduces sequence-defined hydrophobic–hydrophilic gradients at the chain level. In a typical procedure, 95 mol% methyl methacrylate and 5 mol% maleimide monomer are dissolved in 1,4-dioxane to a total monomer concentration of 30 wt%, combined with 2-cyano-2-propyl dithiobenzoate (chain transfer agent/monomer molar ratio 1:1000) and AIBN (CTA/AIBN = 5:1 mol/mol), then degassed by three freeze-pump-thaw cycles. After 8 h at 65 °C, monomer conversion reaches 75–80% (1H NMR). The isolated copolymer displays a dispersity Đ 1.22 (THF-SEC, PMMA standards) and a hydroxyl content consistent with near-quantitative incorporation of the maleimide unit. Attempts to extend this protocol to styrene as the major monomer require addition of 0.1 wt% 4-tert-butylcatechol to inhibit premature thermal homopolymerisation of the maleimide, which otherwise generates crosslinked gel microparticles during the degassing stage. Published kinetic constants for the diethylene glycol maleimide in RAFT systems are limited; however, the measured propagation rate coefficient of the maleimide terminal radical is estimated to be approximately 1.8 × 103 L·mol‑1·s‑1 at 65 °C, based on the observed molar mass evolution.
Reactive extrusion provides a solvent-free pathway to graft the hydroxyl-bearing maleimide onto polyolefin backbones, enabling subsequent crosslinking or dye-labelling. In pilot trials using a co-rotating twin-screw extruder (ZSK 26, L/D 40, screw speed 200 rpm) with a barrel temperature profile 180–210 °C, a premix of styrene-ethylene/butylene-styrene (SEBS) pellets, the liquid maleimide monomer (0.8–1.2 wt% relative to SEBS), and dicumyl peroxide (0.05 wt%) was fed into the main hopper. Grafting efficiency, determined by back-titration of residual double bonds after Soxhlet extraction with acetone to remove unbound maleimide, reached 55–70% when the liquid was injected directly into the melt zone downstream of the melting section via a heated gear pump, thereby minimising volatile loss. Torque spikes and pressure fluctuations observed with higher maleimide loadings (>1.5 wt%) are attributable to maleimide homodimerisation crosslinking reactions in the extruder barrel; inclusion of 200 ppm of 4-methoxyphenol (MEHQ) as a radical inhibitor mitigated this effect, keeping the melt flow index ( ISO 1133-1, 190 °C/2.16 kg) of the grafted product within 10% of the base resin.Conjugation of the maleimide via thiol-Michael addition is highly sensitive to the ionisation state of the thiol nucleophile and the ring integrity. A standard working buffer of 100 mM sodium phosphate at pH 6.8 ± 0.1 with 1 mM EDTA is appropriate for most cysteine-bearing peptides. Under these conditions, the second-order rate constant for reaction with 2-mercaptoethanol has been measured at approximately 1.2 × 103 M‑1s‑1 at 25 °C, falling within the same order of magnitude as that reported for N-ethylmaleimide. The terminal primary hydroxyl neither accelerates nor retards the addition step significantly, but the extended spacer reduces intramolecular steric clashes when targeting partially buried cysteines in folded protein domains. It has been observed, however, that prolonged exposure of the maleimide conjugate to the buffered medium beyond 4 h leads to progressive ring-opening hydrolysis, yielding a maleamic acid adduct that lacks retro-Diels-Alder lability. For long-term bioconjugate storage, replacement of the aqueous buffer with a non-nucleophilic, anhydrous matrix such as lyophilised powder under argon is necessary; stored at ‑80 °C, the conjugate retains more than 95% of the closed maleimide ring after 6 months, whereas in solution at 4 °C the same degree of retention lasts approximately 48 h. The compound is incompatible with amine-containing buffers (Tris, glycine) because competitive Michael addition of the amine onto the maleimide competes with the target thiol ligation.
When the maleimide monomer is incorporated into a polymer backbone and the resulting hydroxyl groups are subsequently esterified or reacted with isocyanates, the choice of spacer can dictate the glass transition temperature (Tg) suppression. Dynamic mechanical analysis (ISO 6721-11, tensile mode, 1 Hz, heating rate 2 K/min) on copolymers of methyl methacrylate with 5 mol% of the diethylene glycol maleimide showed a single tan δ peak at 102 °C, compared to 118 °C for the PMMA homologue and 97 °C for the same copolymer containing a PEG4-maleimide comonomer. This intermediate plasticisation effect is consistently observed and enables tuning of coating flexibility without resorting to high-molecular-weight side chains that risk phase separation.
The following table contrasts the present product with commonly employed maleimide derivatives that differ in spacer length and terminal functionality, highlighting how the two-unit ethoxy segment sits at a performance crossroad.
| Maleimide Derivative | Hydroxyl Group | Spacer Length (atoms) | Water Solubility at 25 °C (mg/mL) | Relative Thiol Coupling Rate(a) |
|---|---|---|---|---|
| N-Ethylmaleimide | None | 3 | < 10 | 1.0 (reference) |
| N-(2-Hydroxyethyl)maleimide | Yes | 4 | > 200 | 0.95 |
| 1-(2-(2-Hydroxyethoxy)ethyl)-1H-pyrrole-2,5-dione | Yes | 8 | > 500 | 0.92 |
| Maleimide-PEG4-OH | Yes | 16 | > 500 | 0.82 |
(a) Second-order rate constant for reaction with 2-mercaptoethanol in 100 mM phosphate, pH 6.8, normalised to N-ethylmaleimide. Values are derived from in-house Ellman’s reagent monitoring with n = 6 replicates; batch-to-batch variation is within ± 0.04.
In hydrogel formulations, the precise spacer length of this maleimide translates directly into network mesh size. A stoichiometric mixture of 4-arm PEG-thiol (10 kDa) and the diethylene glycol maleimide at a thiol:ene ratio of 1.0 in 100 mM phosphate (pH 7.0) achieved a gel point at 120 s (oscillatory time sweep, 1 Hz, 1% strain). The equilibrium swelling ratio in water at 23 °C, determined gravimetrically per ISO 62, was 15.2 ± 0.5 (mean ± SD, n = 3), compared to 22.4 ± 0.7 for an otherwise identical network crosslinked with a PEG-3.4k-dimaleimide. The tighter mesh, a consequence of the shorter maleimide linker, results in a lower diffusivity of encapsulated solutes, with bovine serum albumin (BSA, 66 kDa) exhibiting a release half-life of 72 h versus 38 h in the PEG-3.4k-dimaleimide system. These differences make the compound particularly suited for sustained-release matrices where an intermediate barrier property is desired without the brittleness introduced by very short crosslinks.
In polyurethane synthesis, the hydroxyl group is titrated with aliphatic diisocyanates such as hexamethylene diisocyanate (HDI) at a NCO:OH ratio of 1.05 using dibutyltin dilaurate (0.01 wt%) as catalyst. The resulting maleimide-terminated prepolymer exhibits residual free maleimide content < 0.5% and can be thermally cured via the maleimide moieties at 180 °C for 30 min. The cure exotherm measured by differential scanning calorimetry (ISO 11357-1, nitrogen purge) centres at 200 °C with a reaction enthalpy of 85 J/g, confirming that the maleimide endogroups remain chemically accessible. This route is not available to N-ethylmaleimide or hydroxyl-free analogues and highlights a distinct application niche for the product.
Operational boundaries must be observed to retain the quoted performance. The maleimide monomer is incompatible with primary and secondary amines at any appreciable concentration because the Michael addition onto the double bond occurs within minutes at pH ≥ 7, consuming the maleimide function. When the hydroxyl group is coupled with isocyanates, residual water must be kept below 200 ppm to avoid urea formation that elevates viscosity and reduces NCO titer. Additionally, formulations containing reducing agents such as dithiothreitol (DTT) should not be processed in the presence of the maleimide without prior thiol capping, as DTT readily adds across the maleimide ring.