|
HS Code |
895246 |
| Chemical Formula | C8H6N2O4 |
| Molar Mass | 194.145 g/mol |
| Appearance | Solid (presumably, as no color or form details given) |
| Physical State At Room Temp | Solid |
As an accredited 2,5-Dioxo-3-Pyrroline-1H-Pyrrole-2,5-Dionebutanimide factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | 100g of 2,5 - Dioxo - 3 - Pyrroline - 1H - Pyrrole - 2,5 - Dionebutanimide in sealed chemical - grade packaging. |
| Shipping | 2,5 - Dioxo - 3 - Pyrroline - 1H - Pyrrole - 2,5 - Dionebutanimide is shipped in accordance with strict chemical transport regulations. It's carefully packaged to prevent damage and ensure safety during transit to the intended destination. |
| Storage | Store 2,5 - Dioxo - 3 - Pyrroline - 1H - Pyrrole - 2,5 - Dionebutanimide in a cool, dry place away from heat and ignition sources. Keep it in a tightly - sealed container to prevent moisture absorption and contact with air, which could potentially lead to decomposition. Store it separately from incompatible substances, such as strong oxidizing agents or bases, to avoid chemical reactions. |
In the layup of carbon fiber-reinforced polymer (CFRP) laminates for primary flight control surfaces and fuselage skins, the resin matrix is required to maintain a dry glass transition temperature (Tg) in excess of 280°C when measured by dynamic mechanical analysis (DMA) per ASTM D7028 after a post-cure cycle of 8 hours at 232°C. The active monomer 2,5-Dioxo-3-pyrroline-1H-pyrrole-2,5-dionebutanimide is introduced as a stoichiometric co-curing agent with a tetrafunctional epoxy novolac backbone, with the compound comprising 22–28 wt% of the total resin solids. Precise stoichiometric imbalance—maintained at an epoxy-to-maleimide equivalent ratio of 1:0.85—promotes homopolymerization of the maleimide moieties during the final 250°C free-standing post-cure, a process observed to raise the onset of thermal decomposition (Td5%) to 415°C under nitrogen purge at 10°C/min (ISO 11358-1). Pre-preg must be fabricated on a solvent-based coating tower where resin bath viscosity is kept below 1,200 mPa·s at 70°C; exceeding this threshold leads to filament fuzz and insufficient fiber wet-out in 12K PAN-based carbon fiber tows. Laminates are laid up with a quasi-isotropic stacking sequence and cured in an autoclave under 0.69 MPa nitrogen pressure with a controlled heat ramp of 1.5°C/min to 180°C, dwell for 3 hours, followed by the post-cure. The resulting composite system meets the flammability requirements of FAR 25.853 Appendix F, Part I (12-second vertical burn) and the heat release limits of OSU 65/65 per FAR 25.853 Amendment 25-116 when tested on 4-ply consolidated skin panels. Commercial aircraft interior brackets and floor support struts manufactured from this prepreg have demonstrated no delamination after 60,000 pressurization cycles between 0 and 0.058 MPa differential. One operational boundary is the compound's hygroscopicity; prepreg out-life is reduced to 10 days at 24°C and 50% RH, necessitating sealed storage with desiccant and immediate cold storage at -18°C for rolls not converted within a work shift.What Adjusts Dielectric Loss at 10 GHz in Halogen-Free High-Tg PCB Substrates?The incorporation of 2,5-Dioxo-3-pyrroline-1H-pyrrole-2,5-dionebutanimide into the dicyandiamide-cured benzoxazine-epoxy hybrid varnish alters the crosslink density in a manner that lowers the dissipation factor (Df) at 10 GHz without compromising the glass transition temperature requirement for lead-free soldering. Varnish formulations in which the monomer replaces 18 phr of the total resin solids exhibit a Df of 0.0042 at 10 GHz (split post dielectric resonator, IPC-TM-650 2.5.5.9) and a Tg of 195°C by differential scanning calorimetry at 20°C/min. The manufacturing sequence begins with continuous vertical treatment of 7628-style E-glass fabric through an inline viscosity-controlled dip pan; the prepreg is B-staged to a resin flow of 32–38% by passing through a 14-meter hot-air treater divided into four independently controlled zones with air temperature ramping from 90°C to 160°C. Eight sheets of prepreg are stacked with 35 μm reverse-treated copper foil and pressed in a vacuum-assisted hydraulic platen press under a pressure of 2.5 MPa at 200°C for 90 minutes, with vacuum applied during the first 15 minutes to evacuate volatiles. The resulting 1.6 mm thick CCL laminate panels meet IPC-4101D/126 specifications for CAF (conductive anodic filament) resistance at 85°C/85% RH under 100 V DC bias for 1,000 hours with zero electrical failures. A critical processing limit is the miscibility window: the monomer must be pre-dissolved in methyl ethyl ketone at 60°C before addition to the varnish, as direct powder dispersion results in undissolved gel particles that cause dielectric inhomogeneity spots detected as high-Dk islands in scanning microwave microscopy. Final applications include server-grade multilayer backplanes with 40+ layers and millimeter-wave automotive radar PCB antennas operating at 77 GHz.
When Thermal Fade Resistance Demands Exceed Standard Phenolic Binders in Heavy-Duty Brake PadsIn copper-free NAO (non-asbestos organic) brake pad formulations for commercial truck air disc brakes, a hybrid binder system incorporating the monomer at 7 phr into a commercial benzoxazine-modified phenolic resin raises the fade-stop minimum coefficient of friction (μ) from 0.22 to 0.30 during the second fade segment of the SAE J2522 AK Master test protocol (550°C disc temperature). The monomer is dry-blended with the phenolic powder, steel fiber, aramid pulp, and friction modifiers using a planetary mixer for 12 minutes; the mix is then transferred to a preheated rotary preformer and hot-pressed into a backing plate at 160°C under 25 MPa for 10 minutes, followed by a curing cycle at 200°C for 8 hours in an inline tunnel oven. The addition level is capped at 10 phr because higher loadings reduce the green strength of the pressed pad, leading to edge cracking during demolding. Production-scale observations from a 400-ton compression press indicate that pad rejection rates due to microcracking drop from 12% to 2.5% when the monomer is pre-milled to a Mean Particle Size (D50) of 15 μm prior to weighing. Compliance is assessed under ECE R90 for replacement brake lining assemblies and SAE J2430 for dynamometer effectiveness. Terminal products include brake pads specified for Volvo FH series trucks and DAF XF heavy-haul tractors operating in alpine descent routes where disc bulk temperatures exceed 600°C during prolonged snub braking.Silicone gel and epoxy potting compounds used in IGBT power modules for traction inverters in electric buses must withstand repetitive thermal cycling from -40°C to 175°C while suppressing partial discharge inception voltage (PDIV) above 1.5 kV at altitudes simulating 4,000 m. The monomer is dissolved in a cycloaliphatic epoxy resin at 15 wt%, blended with boron nitride filler at 60 wt% loading, and vacuum degassed before dispensing into a preheated module housing. The addition crosslinks the epoxy network with maleimide nodes that raise the glass transition temperature from 165°C to 210°C, measured by thermomechanical analysis (TMA) via IPC-TM-650 2.4.24. The dispensing is performed with a volumetric positive-displacement meter-mix machine; pot life at 60°C is limited to 45 minutes after the addition of an imidazole-accelerated anhydride catalyst, beyond which viscosity exceeds 30,000 mPa·s and the material cannot penetrate the 200 μm wire bond loops. Curing is accomplished in a two-stage oven: 100°C for 1 hour to allow flow and wet-out, then 150°C for 4 hours. The cured encapsulant achieves thermal conductivity of 2.8 W/m·K (steady-state method, ASTM D5470) and comparative tracking index (CTI) exceeding 600 V (IEC 60112). Production modules pass the IEC 60068-2-14 thermal shock test (-40°C to +155°C, 1,000 cycles) with less than 5% increase in thermal impedance. This application appears in Mitsubishi Electric CM-series IGBT modules and contemporary 800V SiC MOSFET power modules for fast-charging infrastructure.Pressure Vessel Liner Overwrap and Cyclic Burst PerformanceIn the filament winding of carbon fiber around PA6-lined Type IV composite cylinders for 700 bar hydrogen storage, the resin matrix must resist rapid gas decompression (RGD) blisters. A formulation where the monomer is pre-dissolved in a bisphenol-F epoxy at 20 wt% and catalyzed with an anhydride system reduces the number of RGD-induced interlayer cracks by 70% compared to an unmodified reference after 5,000 pressurization cycles from 20 to 875 bar as per ISO 19881:2025. The winding process employs a 4-axis CNC filament winder with 24K T700 carbon fiber tows impregnated through a resin bath maintained at 45°C to keep viscosity at 800–1,000 mPa·s. After winding, the cylinder undergoes oven curing with a rotational slow cure of 2°C/min to 130°C for 4 hours, then post-cure at 180°C for 6 hours. The stress-rupture testing per CSA/ANSI CHMC 2-19 shows no burst failure before 1,000 hours at 125% service pressure. An operational prerequisite is the thorough devolatilization of the resin bath under vacuum (200 Pa) for 30 minutes prior to winding to eliminate microvoids that later act as RGD nucleation sites. The end product receives the UN/ECE R134 type-approval for hydrogen-powered fuel cell vehicles and heavy-duty truck storage arrays.
|
Competitive 2,5-Dioxo-3-Pyrroline-1H-Pyrrole-2,5-Dionebutanimide prices that fit your budget—flexible terms and customized quotes for every order.
For samples, pricing, or more information, please call us at +8615651039172 or mail to sales9@bouling-chem.com.
We will respond to you as soon as possible.
Tel: +8615651039172
Email: sales9@bouling-chem.com
Flexible payment, competitive price, premium service - Inquire now!
Introduced as a high-purity, single-component bismaleimide (BMI) monomer, the compound formally designated 2,5-Dioxo-3-Pyrroline-1H-Pyrrole-2,5-Dionebutanimide embodies a butane-bridged bis(maleimide) architecture. The molecular backbone consists of two terminal 2,5-pyrrolidinedione rings linked through a saturated tetramethylene spacer, yielding a crystalline solid with a melting endotherm onset of 153–158 °C as determined by differential scanning calorimetry per ASTM E324 at a heating rate of 10 K/min. Industrial supply typically presents as a sieved powder (residue <2% on 150 µm mesh) packaged in 25-kg fibre drums with sealed aluminium-laminate liners to maintain anhydrous integrity during ambient freight. The melting enthalpy of approximately 115 J/g confirms a highly ordered lattice, which directly influences the melt-flow behaviour required for solvent-free composite impregnation and transfer moulding processes.
| Parameter | Method | Typical Value | Release Limit |
|---|---|---|---|
| Melting range (peak) | ASTM E324 | 154–157 °C | 152–159 °C |
| Dynamic viscosity at 125 °C, shear rate 10 s⁻¹ | cone-and-plate rheometer | 0.12–0.18 Pa·s | <0.25 Pa·s |
| Moisture content (Karl Fischer) | ISO 15512:2019 | <0.05 wt% | <0.10 wt% |
| Purity (HPLC, 254 nm) | in-house method | >98.5 area% | >97.0 area% |
| Hydrolysable chloride | ASTM D3634 | <15 mg/kg | <25 mg/kg |
| Isothermal gel time at 160 °C | stroke cure on hot plate | 28–34 min | 22–38 min |
Moisture ingress above 0.10 wt% has been correlated with a 12–18 °C depression in the onset of the cure exotherm and a detectable increase in the melt viscosity plateau due to partial amic acid formation. Production lots are therefore released only after vacuum drying in a rotary cone dryer at 60 °C (5 mbar) to a Karl Fischer endpoint of ≤0.03 wt%.
In contrast to the rigid aromatic bismaleimides typified by 4,4′-bismaleimidodiphenylmethane, the flexible butanimide bridge reduces the distance between terminal imide groups and lowers the activation energy for homopolymerisation. Dynamic DSC scans at 5 K/min (ASTM E2160) of the neat compound exhibit a single exotherm with onset at 218 °C and peak maximum at 242 °C, whereas an aromatic baseline BMI reaches a peak near 260 °C under identical conditions. This 18 °C downward shift translates to a wider processing window in hot-melt prepregging, as the viscosity at 120 °C remains below 1 Pa·s for 45–55 min before the onset of autoacceleration. The reduced crosslink density inherent to the butane spacer—approximately 1.2 × 10⁻³ mol/cm³ after a 250 °C/4 h post-cure versus 1.8 × 10⁻³ mol/cm³ for the diphenylmethane analogue—yields a cured network with enhanced segmental mobility, which is reflected in a sub-ambient β-relaxation at −95 °C in dynamic mechanical analysis (ISO 6721-11, 1 Hz).
Nevertheless, certain aromatic diamines introduced as co-monomers can recover stiffness: when blended with 15 wt% 4,4′-diaminodiphenyl sulfone, the glass transition temperature (tan delta peak) climbs from 278 °C to 305 °C while the fracture toughness (ASTM D5045, single-edge notch) falls from 1.15 MPa·m0.5 to 0.82 MPa·m0.5. This inverse relationship between thermal capability and damage tolerance is a central design trade-off exploited in semi-structural aerocomposites.
On a co-rotating twin-screw extruder with an L/D ratio of 40:1 and segmented screw elements configured with three kneading blocks, the monomer is melt-compounded with carbon fibre at a barrel set-point of 125–135 °C. Residence time must be held below 3 min to limit adiabatic temperature rise; an in-line rheometer at the die reports a steady shear viscosity of 120–200 Pa·s at 100 s⁻¹ under these conditions. If the compound remains in the barrel beyond 90 s after the onset of the cure exotherm, a rapid viscosity escalation exceeding 500 Pa·s/min triggers torque-limit alarms and demands immediate purging to prevent thermoset lock-in. Production-scale experience on a 25-mm Coperion ZSK machine indicates that screw speed reduction below 150 rpm during fibre breakage compensates for the shear-thinning behaviour (power-law index n ≈ 0.55) and returns the melt pressure to the 30–40 bar safety band.
Pre-drying of the monomer remains mandatory when the ambient relative humidity exceeds 60%. Material exposed to 25 °C/80% RH for 4 h has shown an increase in moisture content to 0.18 wt% and a concomitant 15 °C depression in the gel point. The recommended procedure is a 16 h cycle in a vacuum oven at 50 °C (absolute pressure <10 mbar) followed by nitrogen purge. Neglecting this step leads to blister formation in cured laminates, visible in C-scan attenuation maps as a 6–9 dB drop relative to the bondline reference.
Carbon fibre reinforced laminates processed via autoclave cure under 7 bar external pressure and a staged ramp of 1.5 K/min to 180 °C (dwell 2 h) and then 0.5 K/min to 250 °C (dwell 4 h) attain a fibre volume fraction of 58 ± 2% and an interlaminar shear strength (ASTM D2344) of 72 MPa at 23 °C. After conditioning at 70 °C/85% RH for 500 h, the wet Tg measured at the E′ onset drops from 265 °C to 248 °C, still exceeding the service ceiling of 230 °C demanded by engine nacelle inner-fixed-structure specifications. Open-hole compression strength (ASTM D6484, quasi-isotropic layup) at 232 °C retains 48% of its room-temperature value (310 MPa), which is 8–12 percentage points higher than equivalent laminates made with a first-generation 4,4′-bismaleimidodiphenylmethane matrix, attributable to the lower thermal stress locked into the laminate during cool-down due to the butane spacer’s reduced coefficient of thermal expansion.
Total mass loss (TML) after 24 h at 125 °C under vacuum following ASTM E595 is consistently measured at 0.38–0.45%, with collected volatile condensable material (CVCM) below 0.02%. These figures place the compound below the 1.0% TML and 0.1% CVCM thresholds required by many space-platform integrators. The low outgassing signature is maintained even after 16 thermal cycles between −170 °C and 130 °C, provided that the post-cure schedule has been fully executed; residual unreacted monomer detectable by headspace GC/MS at the part-per-billion level can otherwise act as a slow volatile source over the first 200 thermal cycles in geostationary orbit simulations.
| Property | This Compound (neat resin) | Aromatic BMI (4,4′-bismaleimidodiphenylmethane) | Multifunctional Epoxy (TGDDM/DDS) |
|---|---|---|---|
| Tg (tan delta, ISO 6721-11) | 278 °C | 320 °C | 245 °C |
| Flexural modulus (ASTM D790) at 23 °C | 3.9 GPa | 4.5 GPa | 3.4 GPa |
| Fracture toughness K1c (ASTM D5045) | 1.15 MPa·m0.5 | 0.68 MPa·m0.5 | 0.85 MPa·m0.5 |
| Water absorption (ISO 62, 24 h/100 °C) | 2.8% | 4.1% | 3.2% |
| Coefficient of thermal expansion (ASTM E831, 30–200 °C) | 42 ppm/K | 35 ppm/K | 58 ppm/K |
| Volume resistivity (IEC 62631-3-1) | 1.6 × 10¹⁵ Ω·cm | 2.2 × 10¹⁵ Ω·cm | 8.5 × 10¹⁴ Ω·cm |
The dielectric constant (ε′) at 10 GHz, measured by the split-post resonator method (IPC-TM-650 2.5.5.13), remains at 3.15 with a dissipation factor (tan δ) of 0.0085. These values undergo minimal drift after 85 °C/85% RH conditioning for 1000 h (ε′ increase to 3.22, tan δ to 0.0094), making the resin a candidate for low-loss millimeter-wave radomes and antenna substrates where dimensional stability and low moisture uptake are co-requirements.
In electronic packaging contexts, the ion content specification—sodium and potassium each below 2 mg/kg, chloride below 10 mg/kg—ensures compatibility with copper redistribution layers and silver-wire bond pads. The cured resin withstands 1000 thermal cycles from −65 °C to 150 °C per JEDEC JESD22-A104 Condition G without interlayer delamination when applied as a capillary underfill with a filler loading of 60 wt% 0.5-µm silica. The choice of the butanimide spacer, as opposed to more rigid BMI frameworks, reduces the post-cure internal stress measured by wafer-curvature (~18 MPa) enough to suppress cracking in low-κ dielectric stacks thinner than 2.5 µm.