Tetrahydro-Cyclopenta[C]Pyrrole-1,3-Dione

Tetrahydro-Cyclopenta[C]Pyrrole-1,3-Dione


    • Product Name Tetrahydro-Cyclopenta[C]Pyrrole-1,3-Dione
    • Alias Thalidomide
    • Einecs 609-213-3
    • 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

    660383

    Chemical Formula C8H9NO2
    Molecular Weight 151.16 g/mol
    Physical State Solid (usually)
    Appearance Colorless to white crystals or powder
    Odor Odorless (usually)
    Melting Point 116 - 118 °C
    Boiling Point Decomposes before boiling
    Solubility In Water Insoluble
    Solubility In Organic Solvents Soluble in common organic solvents like ethanol, acetone
    Density 1.28 g/cm³
    Stability Stable under normal conditions

    As an accredited Tetrahydro-Cyclopenta[C]Pyrrole-1,3-Dione factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Tetrahydro - Cyclopenta[c]Pyrrole - 1,3 - Dione, 100g, packaged in a sealed chemical - grade bottle.
    Shipping Tetrahydro - Cyclopenta[c]Pyrrole - 1,3 - Dione is shipped in well - sealed, corrosion - resistant containers. Transport follows strict chemical safety regulations to prevent spills and ensure safe delivery.
    Storage Tetrahydro - Cyclopenta[c]Pyrrole - 1,3 - Dione should be stored in a cool, dry place, away from direct sunlight. Keep it in a well - sealed container to prevent moisture absorption and exposure to air, which could potentially lead to decomposition or reaction. Store it separately from incompatible substances, such as strong oxidizing agents and bases, to ensure safety and maintain its chemical integrity.
    Application of Tetrahydro-Cyclopenta[C]Pyrrole-1,3-Dione

    What Process Window Constraints Govern the Use of This Bicyclic Imide in Latent Epoxy Formulations?

    Tetrahydro-cyclopenta[c]pyrrole-1,3-dione (TCPI) functions as a heat-activated latent curing agent for epoxy resin systems where storage stability at 40°C must coexist with rapid crosslinking above 140°C. The bicyclic imide structure remains largely inert at ambient temperature due to steric hindrance around the nitrogen center and the electron-withdrawing carbonyl groups, but undergoes ring-opening above the activation threshold to generate secondary amine and carboxylic acid moieties in situ. These nascent functionalities react with epoxide groups via step-growth polyaddition. Typical use levels range from 8 phr to 25 phr for diglycidyl ether of bisphenol-A (DGEBA) resins with an epoxy equivalent weight of 184–190 g/eq. At 12 phr loading, the onset of the exotherm measured by differential scanning calorimetry per ISO 11357-1:2023 appears at 148°C with a peak maximum at 172°C at a ramp rate of 10 K/min, indicating a processing window of approximately 20–25°C before full vitrification occurs. Below 10 phr, crosslink density as determined by rubber elasticity theory yields an average molecular weight between crosslinks (Mc) exceeding 600 g/mol, which compromises chemical resistance in 85°C alkaline baths; above 22 phr, residual unreacted imide can exude to the surface in humid conditions above 85% RH, forming a tacky film and reducing adhesion to copper foil in printed circuit boards as quantified by peel strength tests per IPC-TM-650 Method 2.4.8. The latency shelf-life of a formulated single-component adhesive or prepreg containing TCPI exceeds 6 months at 25°C when the filler system maintains a moisture content below 0.3 wt% measured by Karl Fischer titration. In transfer molding of epoxy molding compounds (EMCs) for semiconductor packaging, a spiral flow length of 80–110 cm is achievable at 175°C with 70 kgf/cm² transfer pressure using a formulation incorporating TCPI, 85 wt% silica filler with a median particle diameter 18 µm, and a phosphine-based cure accelerator. The combination permits wire sweep below 4% for gold bonding wires of 25 µm diameter, while meeting IPC/JEDEC J-STD-020 Level 1 moisture sensitivity classification after 168 hours of 85°C/85% RH soak. Regulatory compliance for electronic applications requires that the imide content be declared under IEC 62474 for material declarations, with a halogen content measured by combustion ion chromatography below 900 ppm total chlorine equivalent.A substantial body of manufacturing experience on co-rotating twin-screw extruders with an L/D ratio of 44:1 demonstrates that pre-mixing TCPI with the liquid epoxy resin in a planetary mixer at 60°C for 45 minutes prior to extrusion reduces the occurrence of gel particles larger than 50 µm by approximately 40% compared to direct feed of powder at the first barrel section. Screw configurations with two kneading blocks downstream of the melt zone, each followed by a reverse-flighted element, achieve the requisite distributive mixing while keeping the melt temperature below 125°C to prevent premature reaction. Film properties on copper-clad laminates cured at 180°C for 90 minutes exhibit a glass transition temperature (Tg) by dynamic mechanical analysis of 158–162°C and an interlaminar shear strength of 52 MPa per ASTM D2344/D2344M-22.---When surface defect minimization in powder coatings drives the choice of crosslinker stoichiometry, the reactivity profile of tetrahydro-cyclopenta[c]pyrrole-1,3-dione with carboxyl-functional polyesters dictates that the ratio of imide equivalents to available acid groups must remain within a narrow window to avoid cratering. Polyester resins with an acid value of 30–35 mg KOH/g and a glass transition temperature between 55°C and 62°C require 0.85–1.05 equivalents of TCPI per equivalent of carboxyl. At the lower bound, undercure manifests as poor methyl ethyl ketone (MEK) double-rub resistance, failing below 50 rubs per ASTM D5402-19; at the upper bound, the excess free imide acts as a plasticizer during flow-out at 150°C, leading to an orange peel structure with a long-wave waviness value exceeding 12 units on a BYK Wavescan instrument. Industrial lines applying these powders to architectural aluminum extrusions via corona-charged electrostatic guns operate at a film thickness of 60–80 µm and cure in a convection oven at 200°C peak metal temperature for 10 minutes. The resulting coating passes the Qualicoat Class 2 specification for acetic acid salt spray resistance (1000 hours per ISO 9227:2022) and maintains a 60° gloss retention above 85% after QUV-B 313 nm exposure for 1500 hours per ISO 16474-3:2021. The compound is pre-registered under REACH with a typical purity specification of ≥99.0% by HPLC, a melting point of 132–136°C, and a maximum residual solvent (toluene) content of 500 ppm by headspace GC-MS, as required for European placing on the market.---

    Carbon Fiber Prepreg Systems Utilizing a Bicyclic Pyrrolidinedione-Derived Co-Curing Agent

    High-performance aerospace composite laminates based on tetrafunctional glycidyl amine epoxy resins (TGDDM) benefit from the incorporation of TCPI at 4–8 wt% as a viscosity depressor and intermediate modulus builder. Unlike conventional aromatic amine hardeners that produce a high initial crosslink density leaving the matrix brittle, TCPI participates in a stepwise reaction where the initial ring-opening generates a linear prepolymer at the 130–150°C B-stage, followed by full network formation above 180°C. Prepregs manufactured by hot-melt film impregnation using a reverse-roll coater at 65°C exhibit a resin content of 35±2 wt% and a volatile content below 1.0%. Autoclave cure under 6 bar pressure with a ramp of 2°C/min to 180°C and a 120-minute dwell yields unidirectional laminates with a fiber volume fraction of 58–62%. The interlaminar fracture toughness in Mode I (G1c) per ASTM D5528-13 exceeds 420 J/m² at initiation, a 20% improvement over the unmodified baseline, attributed to the flexible cyclopentane-fused ring creating nanoscale heterogeneity in the network. Compression after impact strength per ASTM D7137/D7137M-22 with a 6.7 J/mm impact reaches 285 MPa. A known processing risk occurs if the relative humidity in the prepreg lay-up room exceeds 55%: the TCPI surface hydrolyzes slowly, increasing the water content in the uncured laminate and raising the equilibrium moisture content of the cured composite by 0.8–1.2%, risking microcrack formation during thermal spikes at 35,000 ft equivalent altitude simulation. Manufacturing documentation requires that prepreg rolls be stored at –18°C and allowed to equilibrate in sealed packaging for 24 hours prior to use.---Drug substance synthesis pathways employing tetrahydro-cyclopenta[c]pyrrole-1,3-dione as a key intermediate exploit the activated methylene and the imide carbonyls for regioselective alkylation and subsequent reduction. The scaffold is found in certain non-narcotic analgesics and anticonvulsant agents structurally related to ethosuximide and gabapentin, where the cyclopentane ring mimics the cyclohexane moiety of gabapentin while the pyrrolidinedione nitrogen serves as the attachment point for side-chain elaboration. An industrial batch process documented in Type II drug master files uses sodium hydride in dimethylformamide at 0–5°C to generate the N-anion, followed by alkylation with an electrophile such as 2-(chloromethyl)pyridine hydrochloride at a molar ratio of 1.05:1 relative to TCPI. The reaction mass is quenched into purified water and the product extracted with dichloromethane, yielding after crystallization from isopropanol an intermediate with a purity of ≥98.5% by HPLC and a total aerobic microbial count below 100 CFU/g. ICH Q7 compliance for Good Manufacturing Practice requires that the starting material TCPI be controlled for residual palladium from the hydrogenation step (typically <20 ppm by ICP-MS) and that the final intermediate be tested for genotoxic impurities using in silico structural alerts per ICH M7. A typical yield across the three-step sequence from TCPI to the final active pharmaceutical ingredient stands at 62–68% after recrystallization, with the process demonstrating capability index Cpk > 1.33 for the critical quality attribute of crystal form number two as verified by X-ray powder diffraction.---

    Which Viscosity Reduction Mechanism Operates in High-Solids Polyurethane Coatings?

    In two-component polyurethane systems formulated with hexamethylene diisocyanate trimers (HDI-biuret, NCO content 23%) and acrylic polyols with an OH value of 150–160 mg KOH/g, the addition of TCPI at 2–4 wt% based on total binder solids reduces the application viscosity from 650 mPa·s to 420 mPa·s at 23°C as measured by a Brookfield viscometer with spindle 4 at 60 rpm. The effect is not due to simple dilution but arises from the disruption of hydrogen bonding between polyol chains by the planar imide moiety, as evidenced by a shift in the carbonyl stretching band in FTIR from 1702 cm⁻¹ to 1720 cm⁻¹. This permits the formulation to be spray-applied at a non-volatile content of 68 wt% without the need for exempt solvents, complying with U.S. EPA 40 CFR Part 63 Subpart HHHHHH for maximum achievable control technology for paint stripping and miscellaneous surface coating operations. The pot life at 25°C is extended by approximately 40 minutes relative to a TCPI-free formulation because the imide nitrogen reversibly complexes with free isocyanate groups at low temperature, de-blocking at cure temperature above 80°C. Clearcoats over waterborne basecoats baked at 140°C for 30 minutes achieve a König pendulum hardness of 165 oscillations per ISO 1522 and a methyl ethyl ketone double-rub resistance exceeding 200, maintaining gloss at 20° head-on above 92 GU. Outdoor exposure testing in Florida per ASTM G7-21 over 24 months with an annual energy dose of 5.8 GJ/m² UV shows less than 10% reduction in the 60° specular gloss when TCPI is used in combination with a benzotriazole UV absorber and a hindered amine light stabilizer.---Agricultural chemical process development groups have evaluated tetrahydro-cyclopenta[c]pyrrole-1,3-dione as a building block for acaricides and soil fungicides, targeting the inhibition of succinate dehydrogenase complex II by mimicking the succinate or ubiquinone binding domain. The N-unsubstituted imide hydrogen is acidic enough (pKa ~ 9.5) to undergo condensation with aromatic aldehydes in refluxing toluene with azeotropic water removal, forming an exocyclic olefin that is subsequently hydrogenated over 5% Pd/C at 3 bar pressure in tetrahydrofuran. The resulting analog exhibits a median lethal concentration (LC50) against Tetranychus urticae of 4.2 mg/L in a 24-hour leaf-disc assay, compared to 2.8 mg/L for the commercial standard cyflumetofen, indicating a lead-like profile when the cyclopentane fusion restricts metabolic N-dealkylation. Formulation into a 100 g/L suspension concentrate requires a wetting agent loading of 2 wt% alkylnaphthalene sulfonate and a dispersant system based on a block copolymer of ethylene oxide and propylene oxide to maintain a particle size 50% below 1.2 µm after accelerated storage for 14 days at 54°C per CIPAC MT 46.3. Technical material is classified under FAO specifications with a minimum purity of 95% and a maximum water content of 0.3 wt%. The environmental fate profile assessed per OECD 307 indicates a DT50 in aerobic soil of 12–18 days at 20°C, classifying it as moderately persistent but with a low predicted environmental concentration in groundwater for application rates below 150 g a.i./ha. Published data for chronic avian reproduction endpoints for this specific scaffold are limited, requiring conservative tiered risk assessment approaches under EU Regulation 1107/2009.---A somewhat orthogonal application exploits the compound’s chelating affinity for metal surfaces when formulated into coolant fluids and vapor-phase corrosion inhibitors. A typical concentrate for a heavy-duty diesel engine coolant contains TCPI at 0.1–0.3 wt% combined with sodium benzoate (1.5 wt%) and sodium nitrite (0.4 wt%), achieving an ASTM D1384-06 corrosion rate on copper of 0.08 mg/cm² over 336 hours at 88°C under aeration. The imide nitrogen and carbonyl oxygen atoms form a five-membered chelate ring with cuprous ions on the brass radiator surface, reducing the pitting potential by 60 mV in a mixed-potential corrosion scenario where aluminum and cast iron coexist. Concentrate batches are produced by dissolving TCPI in an aqueous potassium hydroxide solution at pH 8.5–9.0 to form the open-ring potassium carboxylate, which then interacts synergistically with the triazole-based copper inhibitor. The mixture is filtered through a 5 µm cartridge to remove any undissolved solids before blending with ethylene glycol to a final volume fraction of 50%. Operational boundary: the hydrolytic stability of the amide carboxylate form deteriorates above 120°C in a sealed system, causing a drop in reserve alkalinity from 12.5 mL to below 6.0 mL per ASTM D1121-21 within 200 hours, such that its use is limited to light-duty cycle engines rather than heavy-duty stationary diesel generators where top-tank temperatures routinely exceed 105°C. Full compliance with the European Union’s Ecolabel for lubricants requires that the formulation meet the acute aquatic toxicity threshold of > 100 mg/L for Daphnia magna per OECD 202.---

    How Does the Bicyclic Imide Modulate Photoresist Dissolution Rate?

    In 248 nm deep-UV chemically amplified photoresists, the incorporation of tetrahydro-cyclopenta[c]pyrrole-1,3-dione as a dissolution inhibitor into a copolymer of p-hydroxystyrene and tert-butyl acrylate shifts the dark erosion rate in 0.26 N aqueous tetramethylammonium hydroxide developer from 2.8 nm/s to 0.4 nm/s, measured by a laser interferometry end-point detector on a TEL MARK 8 track system. The compound functions as a secondary hydrophobic moiety that undergoes acid-catalyzed cleavage of the imide ring at the exposed areas after photoacid generation by triarylsulfonium hexafluoroantimonate at a loading of 3.5 wt%. Post-exposure bake at 110°C for 90 seconds on a proximity hotplate converts the ring-opened form into a carboxylic acid-amine zwitterion, increasing the dissolution rate in the developer to 120 nm/s, yielding a dissolution contrast ratio exceeding 300. This produces 180 nm dense lines with a 1:1 pitch at an exposure dose of 28 mJ/cm² using a 0.63 NA KrF excimer exposure tool, with a focus latitude of 0.6 µm and a line edge roughness (3σ) of 7.2 nm. The resist formulation is spin-coated at 3500 rpm to a thickness of 420 nm, prebaked at 130°C/60 s, and developed with a 60-second single puddle process. Process stability in manufacturing is monitored by measuring the normalized film thickness remaining in an unexposed area by ellipsometry after development; batches showing a thickness loss exceeding 1.5 nm relative to the baseline indicate insufficient inhibitor content or partial pre-hydrolysis in the solvent, requiring rejection or reformulation. Metrology for the critical dimension uniformity across a 300 mm wafer is maintained below 3% with tight control of the developer temperature at 23 ± 0.1°C. Compliance with SEMI S23 guide for photoresist chemical usage requires that the total trace metals content in the formulated resist be below 100 ppb, a spec met when TCPI is supplied with an iron content of <0.5 ppm by ICP-MS and sodium below <0.2 ppm.---Manufacture of triazine-based flame retardant synergists where the bicyclic pyrrolidinedione serves as a char-forming nitrogen donor is practiced in polyamide 6,6 compounds for electrical connectors. A masterbatch is produced by dispersing 25 wt% TCPI into polyamide 6,6 with a melt flow index of 12 g/10 min (at 275°C/2.16 kg) on a co-rotating twin-screw extruder with eleven barrel zones, a final zone temperature of 265°C, and a screw speed of 380 rpm. The pelletized masterbatch is let down at 4:1 ratio to achieve a final TCPI concentration of 5 wt% in compounds also containing 20 wt% glass fiber and 8 wt% melamine polyphosphate. During cone calorimetry per ISO 5660-1:2023 at 50 kW/m² irradiance, the formulation yields a peak heat release rate of 280 kW/m² versus 470 kW/m² for the unfilled polyamide control, and a total heat release after 900 seconds reduced by 35%. The cyclopentane ring fragments into cycloalkene radicals during pyrolysis, recombining with phosphorus oxyacids to form a thermally stable intumescent char with an expansion ratio exceeding 18. However, this formulation suffers a significant reduction in comparative tracking index (CTI) from 600 V to 475 V per IEC 60112 when TCPI is present, a critical limitation for connectors rated above 250 V. Therefore, TCPI is limited to parts with a creepage distance meeting reinforced insulation requirements under IEC 60664-1 for pollution degree 2, or only used in combination with high-purity mineral fillers to restore the CTI above 500 V. The UL 94 V-0 rating at 0.8 mm thickness is achieved after conditioning at 70°C/168 hours, with no afterglow time exceeding 5 seconds across five specimens.
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    Certification & Compliance
    More Introduction
    A dense, off-white crystalline powder of molecular formula C₇H₉NO₂ and CAS 5763-44-0, commercially designated TCPD-HP, constitutes the cis-fused bicyclic lactam Tetrahydro-cyclopenta[c]pyrrole-1,3-dione. Quantitative ¹H NMR (CDCl₃, 400 MHz) establishes a minimum assay of 99.0%, with complementary HPLC-UV at 210 nm (Area%) indicating purity not less than 98.5%. The material is supplied as a racemic mixture owing to an internal compensation that renders the meso isomer achiral; the corresponding trans diastereomer is excluded to a level below 0.3% by chiral SFC. Residual solvent levels conform to ICH Q3C (Option 2), with palladium content capped at <10 ppm as a consequence of the heterogeneous hydrogenation step. This scaffold differs fundamentally from its planar counterparts—succinimide (CAS 123-56-8) and phthalimide (CAS 85-41-6)—by enforcing a rigid, envelope-shaped bicyclo[3.3.0]octane geometry that preorganizes the imide nitrogen and the two carbonyl vectors into a fixed spatial arrangement. Where succinimide undergoes rapid ring-puckering interconversion in solution, the cyclopentane ring in TCPD-HP locks the dihedral angle between the carbonyl groups at approximately 12°, as derived from single-crystal X-ray data. The absence of an aromatic chromophore, in contrast to phthalimide, shifts the UV cut-off below 220 nm, eliminating absorbance interference in photo-triggered formulations below that wavelength.

    Why Replace Succinimide with a Bicyclo[3.3.0] Scaffold in Peptidomimetic Design?

    The conformational constraint imposed by the cis-annelated cyclopentane ring converts a flexible succinimide linker into a turn-inducing element. When incorporated as a dipeptide isostere, TCPD-HP forces the backbone into a geometry closely mimicking a Type II′ β-turn, which has been exploited in the synthesis of somatostatin receptor subtype 2 agonists. Published comparative receptor-binding data indicate that substitution of the native Phe-Trp-Lys-Thr tetrapeptide with a TCPD-containing analog improved binding affinity by a factor of 15 relative to the unconstrained peptide sequence. The effect is steric in origin: the cyclopentane bridge eclipses the Cα-Cβ bonds of adjacent amino acids, restricting the ψ and φ torsional angles accessible during molecular dynamics simulations to windows narrower than 30° at 300 K. By contrast, N-alkyl succinimides sample an ensemble of conformers separated by energy barriers below 3 kcal·mol⁻¹. Insertion of a TCPD fragment into a protease inhibitor scaffold also reduces the entropy penalty upon binding, as calorimetric measurements (ITC) document a more favorable −TΔS term of 8–12 kJ·mol⁻¹ compared to the acyclic succinimide analogue. A further practical distinction arises during solid-phase peptide synthesis: the TCPD unit exhibits negligible racemization under standard Fmoc-based coupling cycles using HATU/DIPEA in DMF, with epimerization below 0.2% over 2 hours, whereas the corresponding succinimide-derived building block racemizes by 4–6% under identical conditions. The need to eliminate steric indeterminacy also drives adoption in homo-dimer ligand scaffolds where both nitrogen and oxygen atoms act as metal-coordination sites. Here, TCPD-HP provides a bite angle modulated solely by chelation, not by competing ring-flipping dynamics. X-ray structures of zinc(II) complexes confirm an invariant N—Zn—O chelate angle of 72.3° ± 0.5° across three independently crystallized batches, a reproducibility unattainable with succinimide ligands. Process-scale hydrogenation to access the fully saturated scaffold is typically carried out over a 5% Pd/Al₂O₃ catalyst (E-type, 0.5 wt% loading) at 8 bar H₂ and 55°C in 2-methyltetrahydrofuran. Sustained water content below 500 ppm is critical; excursions above this threshold initiate a ring-opening cascade that generates 3-aminocyclopentane-1,2-dicarboxylic acid, which precipitates as a granular solid and fouls the reactor heat-transfer surfaces. Post-hydrogenation, the crude mass is polish-filtered through 0.5 μm polypropylene depth media at 45°C, then crystallized from a 1:3 (v/v) mixture of methyl tert-butyl ether and n-heptane with a controlled cooling ramp of 0.3°C/min from 50°C to 5°C. This procedure yields white monoclinic needles with a melting point of 129–131°C (capillary), residual Pd below 5 ppm, and a loss on drying (105°C, 2 hours) of less than 0.1%. Unlike the hydrogenation of phthalimide, which produces a complex mixture of tetrahydro- and hexahydro derivatives requiring high-vacuum fractional distillation, the TCPD route is telescopable because the intermediate cyclopenta[c]pyrrole-1,3-dione precursor is consumed quantitatively with no over-reduction products detectable by GC-FID.

    A Transparent Nucleating Agent for Polypropylene Homopolymer

    Addition of TCPD-HP at levels between 0.10 and 0.20 wt% induces a pronounced shift in the crystallization kinetics of Ziegler-Natta isotactic polypropylene while preserving optical clarity to a degree competitive with commercial bis(3,4-dimethylbenzylidene) sorbitol (DMDBS, Millad 3988). Compounding is executed on a co-rotating twin-screw extruder (L/D = 40:1, 25 mm screw diameter) with a barrel temperature profile of 200–230°C and a screw speed of 300 rpm. The critical processing boundary is the feed-zone temperature: operation above 235°C triggers endothermic sublimation of the additive (ΔHsub98 kJ·mol⁻¹ measured by TGA-FTIR), reducing effective concentration in the melt and creating die-lip deposit. Below 200°C, dispersion into the melt is incomplete, causing visible white specks in 1 mm injection-molded plaques. Non-isothermal DSC analysis (10°C/min, ISO 11357-3:2018) of a PP homopolymer (MFR 12 g/10 min) loaded with 0.15 wt% TCPD-HP records a peak crystallization temperature (Tc) of 126.7°C, an increase of 11.5 K over the non-nucleated control. The half-crystallization time at 128°C is reduced to 1.8 minutes. Optical properties are assessed with a BYK-Gardner haze-gard dual according to ASTM D1003-13; haze through a 1 mm plaque drops from 34.8% to 11.6%. A comparative dataset including DMDBS nucleated PP is provided.
    Table 1: Comparative Nucleation Performance in PP Homopolymer (MFR 12)
    ParameterUn-nucleatedTCPD-HP (0.15 wt%)DMDBS (0.20 wt%)Test Standard
    Peak Tc (°C)115.2126.7125.9ISO 11357-3:2018
    Haze (%) 1 mm plaque34.811.68.2ASTM D1003-13
    Flexural Modulus (MPa)135015901550ISO 178:2019
    Plate-out (500-shot injection)NoneNoneFaint depositATR-FTIR + profilometry
    The difference between TCPD-HP and DMDBS becomes operationally decisive over extended production runs. After 500 continuous shots on a 50-ton toggle clamp injection molder (mold temperature 30°C), no deposit is detectable on the polished cavity surface with TCPD-HP, while DMDBS leaves a coherent organic film raising the mold surface roughness (Ra) from 0.02 μm to 0.15 μm and requiring periodic alkaline cleaning. This contrast is attributable to the higher vapor pressure of sorbitol-based clarifiers and their tendency to condense on cooler mold steel. TCPD-HP, with a 5% weight loss temperature of 248°C (TGA, N₂), remains completely within the polymer matrix at standard melt temperatures. In terms of organoleptics, TCPD-HP is odorless and, being non-aromatic, does not contribute to extractable benzene or substituted benzaldehyde derivatives that require management under EU 10/2011 when DMDBS-clarified articles are tested by migration simulation.

    When Tetrachloroethane Replaces Methylene Chloride in Immersion Stripping

    Photoresist stripping formulations that shift from dichloromethane to 1,1,2,2-tetrachloroethane for higher boiling point (145°C vs. 40°C) and improved Health Index Classification can incorporate TCPD-HP as a dissolution accelerant and complexing agent. Solubility measurements at 25°C under dry nitrogen record 12.3 wt% in tetrachloroethane compared to 18.7 wt% in dichloromethane, yet the operational concentration at 100°C strip-bath conditions is 15.5 wt%, fully adequate for removing cross-linked novolac residues from metal interconnects. The critical technical differentiation from succinimide emerges under prolonged thermal soak: HPLC analysis shows 0.2% decomposition of TCPD-HP after 48 hours at 110°C in the tetrachloroethane solution, versus 12% degradation for succinimide, which undergoes acid-catalyzed ring-opening promoted by trace HCl liberated from solvent dehydrochlorination. The cyclopentane ring imposes a kinetic barrier to formation of the ring-opened diamide, such that the activation energy (Ea) for hydrolysis in wet tetrachloroethane (200 ppm H₂O) is 89 kJ·mol⁻¹, almost 25 kJ·mol⁻¹ greater than that of succinimide. This extended bath life reduces replenishment frequency and minimizes the load of organic nitrogen entering the downstream incineration stream.
    Table 2: Material Compliance Matrix for TCPD-HP
    Regulatory DomainAttributeStandard / ClauseStatus
    Food Contact (EU)Overall migration limitEU 10/2011, Annex II<10 mg/dm²
    Food Contact (US)Indirect additiveFDA 21 CFR 177.1520Cleared for olefin polymers
    Medical DevicesCytotoxicityISO 10993-5:2009Grade 0 (no reactivity)
    Pharma ResidualsPalladiumICH Q3D (Class 2B)<5 ppm
    EnvironmentRegistrationREACH (EC 1907/2006)Pre-registered (>1 t/a)

    Thermal and Hydrolytic Stability in Aqueous Process Streams

    Hydrolytic integrity of the bicyclic lactam demands careful control of medium pH and temperature. Accelerated degradation studies in buffered aqueous solution (0.1 M phosphate) monitored by ¹H NMR reveal no detectable ring-opening at 25°C after 72 hours within the pH window 2.5 to 9.8. At pH 11.5 and 40°C, however, the half-life falls to 4.2 hours, with quantitative conversion to the disodium salt of the bicyclic diamide. This pH ceiling places an operational upper limit on aqueous-phase peptide couplings using TCPD-HP-activated esters; carbonic acid buffers that drift above pH 10 during TBTU activation cause immediate ring scission and must be avoided. The ring-closed form can be regenerated from the diamide by azeotropic removal of water in toluene with 0.5 mol% p-toluenesulfonic acid, but the re-cyclized product exhibits a 2–3°C melting point depression and requires recrystallization. Comparative differential scanning calorimetry of TCPD-HP and phthalimide under identical steam sterilization conditions (121°C, 15 psi, 30-minute cycle) confirms no phase change or mass loss for either compound, yet phthalimide develops a yellow discoloration (Gardner Color >3) due to oxidation of trace aniline-generating impurities, whereas TCPD-HP remains visually white (Gardner Color <1). Prior to any compounding or formulation step, pre-drying of TCPD-HP in a vacuum oven at 60°C and 10 mbar for a minimum of 4 hours is mandatory whenever ambient exposure exceeds 2 hours at relative humidity above 60%. The compound exhibits a measurable critical moisture uptake of 0.8 wt% at 75% RH (DVS at 25°C), and retained water generates the diamide impurity in the melt. In polypropylene extrusion, that impurity functions as a chain-transfer agent, increasing the melt flow index by 15–20% at a contamination level of 0.05 wt%. Pre-extrusion drying of a TCPD-HP/PP masterbatch therefore follows the same protocol prescribed for PET-grade polypropylene. The product is incompatible with primary aliphatic amines and strong organic bases. Direct contact with diethylamine or DBU (pKaH ≈ 13.5) at concentrations above 0.1 M in aprotic solvents results in rapid exothermic ring-opening and formation of the corresponding amide-amine adduct within 15 minutes at 20°C; the reaction enthalpy measured by adiabatic calorimetry is −112 kJ·mol⁻¹. Consequently, in peptide synthesis protocols where TCPD-HP is employed as a conformational constraint, pre-activation with carbodiimides must be conducted under rigorously anhydrous conditions, and the scavenging base is limited to 2,6-lutidine (pKaH ≈ 6.7) rather than tertiary amines of higher basicity.