1H-Pyrrole, 2,5-Dihydro-

1H-Pyrrole, 2,5-Dihydro-


    • Product Name 1H-Pyrrole, 2,5-Dihydro-
    • Alias Pyrroline
    • Einecs 202-807-1
    • 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
    VTB
    Specifications

    HS Code

    491301

    Name 1H-Pyrrole, 2,5-Dihydro-
    Molecular Formula C4H7N
    Molar Mass 69.105 g/mol
    Appearance Colorless to light yellow liquid
    Boiling Point 88 - 90 °C
    Density 0.912 g/cm³
    Flash Point -6 °C
    Solubility Soluble in organic solvents like ethanol, ether
    Odor Characteristic, somewhat pungent
    Refractive Index 1.487 (20 °C)

    As an accredited 1H-Pyrrole, 2,5-Dihydro- factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 100g of 2,5 - Dihydro - 1H - Pyrrole in a sealed chemical - grade bottle.
    Shipping 1H - Pyrrole, 2,5 - Dihydro is shipped in accordance with strict chemical safety regulations. It's carefully packaged to prevent spills and damage, transported in containers suitable for its chemical properties, and handled by trained personnel.
    Storage 1H - Pyrrole, 2,5 - Dihydro - should be stored in a cool, dry, well - ventilated area, away from heat sources and ignition sources. It should be kept in a tightly - sealed container to prevent vapor leakage. Due to its potential reactivity, store it separately from oxidizing agents and incompatible substances. Ensure storage conditions comply with safety regulations to minimize risks.
    Application of 1H-Pyrrole, 2,5-Dihydro-

    What makes the N–H moiety in 2,5-dihydropyrrole a privileged handle for pyrrolidine alkaloid synthesis?

    2,5-Dihydropyrrole (DHP) functions as a direct precursor to the fully saturated pyrrolidine ring through catalytic hydrogenation, a transformation that underpins its role in pharmaceutical intermediate manufacture. The olefinic bond residing at the 3,4-position undergoes selective reduction over Raney Nickel or Pt/C catalysts at typical hydrogen pressures of 1.5–3.0 MPa and temperatures held between 60 °C and 110 °C. A production-scale stirred autoclave equipped with a gas entrainment impeller achieves complete conversion within 2–4 h when the DHP charge is diluted to 40–50 wt% in anhydrous tetrahydrofuran or methanol. Residual catalyst fines are removed downstream via 0.2-µm sintered metal filtration, and the pyrrolidine fraction is isolated by fractional distillation under reduced pressure (50–60 mbar, overhead temperature 42–48 °C). Specifications for an active pharmaceutical ingredient (API) starting material require GC-FID purity ≥ 99.0%, water content ≤ 0.1% determined by Karl Fischer coulometry (USP <921> Method Ia), and total volatile organic impurities meeting ICH Q3C limits for Class 2 solvents. The pyrrolidine intermediate is subsequently alkylated or acylated to construct N-substituted piperidine bioisosteres, structural motifs recurrent in selective serotonin reuptake inhibitors and JAK kinase inhibitors. Quality documentation supplied with export batches routinely includes heavy metal screening via ICP-MS to verify compliance with ICH Q3D elemental impurity thresholds, and residual nickel is controlled below 5 ppm to avoid catalytic interference in downstream palladium-catalyzed coupling steps.

    When DHP is employed as a dipolarophile in 1,3-dipolar cycloaddition with nitrones or azomethine ylides, the stereochemical outcome is governed by the choice of electron-deficient alkenes and the Lewis acid cocatalyst. A typical protocol loads 1.0 eq of DHP with 1.2 eq of the nitrone in anhydrous toluene at −10 °C, with 10 mol% magnesium bromide etherate as a Lewis acid promoter; diastereomeric purity exceeds 90% by chiral supercritical fluid chromatography (SFC) monitored at 220 nm. The resulting hexahydropyrroloisoxazole scaffold is a direct precursor to aminocyclitol fragments found in neuraminidase inhibitors. Manufacturers shipping DHP for this purpose supply a certificate of analysis that quantifies the inhibitor p-methoxyphenol (MEHQ) content by HPLC with UV detection at 280 nm, ensuring the stabilizer remains below 50 ppm to avoid interference with radical-sensitive cycloaddition kinetics.

    Epoxy thermoset systems: stoichiometric window and latent cure behaviour

    When formulating with a standard bisphenol-A diglycidyl ether resin (EEW 186–190 g/eq), the theoretical active hydrogen equivalent weight of DHP is 69.1 g/eq, yielding a stoichiometric loading of 36.4 phr. Industrial practice deviates deliberately: a loading of 30 phr is selected to leave residual epoxide groups that enhance adhesion to grit-blasted mild steel, while 40 phr pushes network density toward a full cure plateau at the cost of room-temperature pot life decreasing from 55 minutes to 12 minutes as measured on a Techne GT-6 gel timer at 25 °C. Differential scanning calorimetry performed with a Mettler-Toledo DSC 3+ under nitrogen at a linear ramp of 10 K/min reveals a broad exotherm initiating at 68–72 °C and peaking at 128 °C, which mandates a two-stage industrial cure cycle: 2 h at 80 °C followed by 1 h at 150 °C. Post-cure residual enthalpy is verified to be below 5 J/g to confirm functional conversion above 95%.

    Representative cured properties of DGEBA/DHP systems versus conventional amine hardeners
    SystemLoading / phrTg (DSC midpoint) / °CTensile strength / MPaFlexural modulus / GPaTest standard
    DGEBA/DHP stoichiometric36.4112 ± 363 ± 42.9 ± 0.2ASTM D638-14, ASTM D790-17
    DGEBA/DHP sub-stoichiometric30.098 ± 455 ± 52.4 ± 0.2ASTM D638-14, ASTM D790-17
    DGEBA/piperidine control5.089 ± 548 ± 62.1 ± 0.3ASTM D638-14, ASTM D790-17

    On twin-screw dispersers with L/D 40:1 configured with distributive mixing elements, vacuum-assisted degassing at −0.095 MPa gauge pressure is applied during the final barrel zone to eliminate porosities that otherwise reduce Type IV tensile strength by 18–22%. The resulting cured network withstands ≥ 30 days immersion in 3% NaCl solution at 60 °C with less than 2% mass gain, evaluated per ISO 62:2008 Method 1. A critical processing boundary exists during warm-filling operations: if the resin/DHP blend temperature exceeds 55 °C before moulding, localized auto-acceleration triggers an exotherm that can thermally degrade the aluminium mould release agent, a failure mode mitigated by equipping the static mixer with a PID-controlled cooling jacket maintaining 40 ± 3 °C. REACH SVHC screening confirms that unreacted monomer levels are below 0.1 wt% in the final network, a prerequisite for articles classified under Regulation (EC) No 1907/2006.

    Acrylate-functional binders formulated with 2,5-dihydropyrrole as a co-monomer exhibit markedly improved wet adhesion to aluminium substrates without sacrificing exterior durability as measured by accelerated weathering to ISO 11341:2004. The cyclic allylic amine is incorporated at 5–15 mol% into a solution-polymerized methyl methacrylate–butyl acrylate backbone using 2,2′-azobis(2-methylpropionitrile) initiator at 0.3 mol% on total monomers, with a continuous feed over 4 h in n-butyl acetate at reflux (126 °C). The resulting copolymer exhibits a Mark–Houwink intrinsic viscosity of 0.4–0.6 dL/g in THF at 25 °C. Cross-hatch tape adhesion on AA 2024-T3 panels conditioned under 40 °C/95% RH for 240 h retains > 95% of the dry value, classified as 5B per ASTM D3359-17. The pyrroline ring imparts sufficient hydrophilicity to displace interfacial water while maintaining glass transition temperatures above 45 °C as measured by DMA at 1 Hz, preventing creep in automotive clearcoats applied over basecoat systems cured at 140 °C for 20 minutes.

    The same copolymer architecture is deployed in UV-curable overprint varnishes where the allylic C–H bond participates in thiol–ene click photochemistry. Formulations containing a stoichiometric amount of pentaerythritol tetrakis(3-mercaptopropionate) and 1.5 wt% type-I photoinitiator (diphenyl(2,4,6-trimethylbenzoyl)phosphine oxide) polymerize under a 200 W/cm² mercury arc lamp to produce films with a König pendulum hardness exceeding 140 s and methyl ethyl ketone double-rub resistance above 100 cycles.

    When the N–H moiety replaces conventional diols in polyurethane elastomer synthesis

    Substituting a fraction of the hydroxyl-terminated polyol with DHP in a one-shot polyurethane casting formulation introduces urea linkages that increase the hard-segment melting domain. The prepolymer route is preferred in production: a poly(tetramethylene ether) glycol (PTMEG 1000) is end-capped with 4,4′-methylene diphenyl diisocyanate to an NCO content of 5.0–6.5%, then chain-extended with 0.9–1.0 equivalents of DHP relative to residual isocyanate at 80 °C in a planetary mixer under −0.095 MPa vacuum. Gel time on a heated plate at 130 °C shortens to 90 seconds, placing a hard constraint on the casting window and necessitating direct tool-to-platen transfer within 45 seconds. Post-curing at 110 °C for 20 h stabilizes phase separation; temperature-modulated DSC reveals a soft-segment Tg near −65 °C and a broad hard-segment endotherm spanning 160–210 °C. Elastomeric properties include a Shore A hardness of 88–94 according to ISO 48-4:2018, tensile strength of 25–32 MPa (ISO 37:2017 Type 2 dumbbell), and tear resistance above 85 kN/m measured by the trouser tear method (ISO 34-1:2015).

    Processing adjustments are essential when relative humidity in the casting bay exceeds 60%: the hygroscopic DHP must be vacuum-dried in a rotary evaporator at 40 °C for at least 2 h and protected under dry nitrogen. Failure to do so results in bicarbonate formation that manifests as visible pitting in the cured ribbon and a 30–35% loss in Taber abrasion resistance (ASTM D4060-14; H-18 wheels, 1 kg load). Industrial rollers and high-durometer seal rings manufactured from this elastomer compound demonstrate dynamic fatigue endurance exceeding 500,000 cycles on a Demattia flex tester when correctly processed.

    Catalytic hydrogenation to pyrrolidine—a stepping stone for agrochemical actives

    A continuous-flow fixed-bed reactor charged with a 2% palladium on activated carbon granulate converts DHP to pyrrolidine with space-time yields surpassing 0.8 kg/L-cat·h when operated at 120 °C and 2.5 MPa hydrogen back-pressure. The liquid feed, consisting of 60 wt% DHP in cyclohexane, passes through a static mixer to dissolve hydrogen before entering the catalyst zone; conversion monitored by inline Raman spectroscopy targeting the 1635 cm⁻¹ C=C stretch remains above 99.7%. Pyrrolidine isolated from the solvent by atmospheric distillation serves as the nitrogen-bearing nucleus for diphenyl ether and pyrazole herbicides. The agrochemical supply chain enforces maximum limits of 0.5 ppm palladium in the final intermediate measured by ICP-MS to avoid phytotoxic accumulation in foliar spray formulations. Compliance is documented through certificates aligned with FAO Specification Guidelines 2022 for technical-grade active ingredients, including polychlorinated dioxin/furan screening when the downstream product contains chlorinated phenyl rings.

    Organocatalysis: grafting chiral auxiliaries onto the 2,5-dihydro ring

    Enantioselective synthesis laboratories exploit the secondary amine of DHP to construct chiral pyrrolidine organocatalysts following the MacMillan imidazolidinone motif. A standard sequence begins with Boc protection conducted with di-tert-butyl dicarbonate (1.05 eq) in dichloromethane containing 5 mol% 4-dimethylaminopyridine at room temperature, isolating the N-Boc-DHP as a clear oil after silica plug filtration. Subsequent asymmetric dihydroxylation with AD-mix-β under Sharpless conditions installs two oxygen atoms onto the olefin, followed by mesylation and cyclization to a fused bicyclic framework that retains the pyrrolidine architecture. The catalytic activity of the free amine, recovered by trifluoroacetic acid deprotection, is validated in a test Diels–Alder reaction between cyclopentadiene and cinnamaldehyde; enantiomeric excesses of 88–92% are consistently achieved as determined by chiral SFC with a Chiralpak IA-3 column. Fine-chemical exporters supply supportive documentation for this application that includes quantitative ¹H NMR purity of the Boc-protected intermediate (> 98.0%) and rotational optical purity (specific rotation measured at 589 nm, c = 1.0 in chloroform).

    In the field of conductive polymer precursors, 2,5-dihydropyrrole serves as a vapour-phase transportable pyrrole generator that can be thermally dehydrogenated over transition-metal oxide catalysts in a chemical vapour deposition (CVD) environment. The liquid is heated to 80 °C in a precision bubbler with a MKS mass flow controller set to deliver 50 sccm of nitrogen carrier gas into a 300 mTorr reaction chamber where a FeCl₃-impregnated substrate held at 150 °C simultaneously dehydrogenates and oxidatively polymerizes the monomer. In-situ quartz crystal microbalance monitoring reveals a deposition rate of 8–12 nm/min, and four-point probe measurements under ASTM F43-21 protocols yield a film sheet resistance of 2.5–5.0 kΩ/sq for a 100 nm thickness without additional dopant. The requirement for oxygen-free carrier gas is absolute; oxygen intrusion above 50 ppm induces premature oligomerization inside the delivery lines and a pressure drop deviation exceeding 15% from setpoint. Published data for maximum film uniformity over 300 mm wafer substrates remains limited, though reproducibility across five successive depositions on four-inch silicon wafers shows a coefficient of variance below 8% when a 0.1 µm pore size in-line particle filter is installed directly upstream of the showerhead assembly.

    Free Quote

    Competitive 1H-Pyrrole, 2,5-Dihydro- 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

    Get Free Quote of Bouling Chemical Co., Limited

    Flexible payment, competitive price, premium service - Inquire now!

    Certification & Compliance
    More Introduction

    Commercially supplied as a colorless to pale yellow liquid with a characteristic amine odor, 1H-Pyrrole, 2,5-dihydro- (CAS RN 109-96-6) is a five-membered cyclic secondary amine containing a single endocyclic double bond. The material is routinely manufactured via reduction of pyrrole or by cyclization of 1,4-dihalobut-2-enes with primary amines, followed by fractional distillation under reduced pressure to achieve a typical assay of 97.0–99.5% (GC area%). Industrial batches are standardized to a water content of ≤0.5% (ISO 760:1978, Karl Fischer coulometric titration) and a peroxide value below 0.5 mmol/kg (iodometric titration, internal method adapted from ASTM E298-17a) due to the susceptibility of the allylic amine moiety to autoxidation. Refractive index (nD20) lies between 1.4655–1.4670 (ASTM D1218-21), density at 20°C is 0.909–0.915 g/mL (ASTM D4052-22), and the atmospheric boiling range is 90–92°C. The compound is miscible with common aprotic solvents (THF, DCM, toluene) and exhibits limited aqueous solubility of approximately 12 g/100 mL at 25°C, forming a mildly alkaline solution (pKa of the conjugate acid ≈ 10.0). Producers supply the product in 100 mL, 500 mL, and 2.5 L borosilicate glass bottles under nitrogen blanket, or in 200 L steel drums with internal phenolic lining for bulk users; all containers are fitted with PTFE-faced septa to minimize headspace oxygen ingress.

    Typical Specification Sheet — 1H-Pyrrole, 2,5-dihydro- (Technical Grade)
    ParameterSpecificationTest Method / Standard
    Assay (GC)≥ 97.0% (area%)In-house GC-FID, DB-5 column, 30 m × 0.25 mm × 0.25 µm, He carrier
    Water Content≤ 0.5% w/wISO 760:1978 (K-F coulometric)
    Peroxide Value≤ 0.5 mmol/kgIodometric titration, adapted from ASTM E298-17a
    Refractive Index (nD20)1.4655 – 1.4670ASTM D1218-21
    Density (20°C)0.909 – 0.915 g/mLASTM D4052-22
    Boiling Range90 – 92°C (760 mmHg)ASTM D86-23a (micro-distillation)
    Color (APHA)≤ 100ASTM D1209-05(2019)
    Stabilizer (BHT, optional)100 – 300 ppmHPLC-UV, internal method

    Storage and Stability: The Role of Water and Oxygen

    The allylic C–H bonds adjacent to the nitrogen atom render 1H-pyrrole, 2,5-dihydro- intrinsically sensitive to radical-mediated oxidation. On standing in air, hydroperoxide formation at the α-position proceeds with an induction period of roughly 6–12 hours at ambient temperature in the absence of stabilizer, followed by autocatalytic decomposition that yields ring-opened amino-aldehydes and discolored oligomeric species. To suppress this pathway, the product is routinely inhibited with 100–300 ppm of butylated hydroxytoluene (BHT). Even with BHT, headspace oxygen in partially emptied containers must be replaced with dry nitrogen (dew point ≤ −40°C) immediately after each withdrawal. Storage at 2–8°C extends shelf life to 12 months; storage at room temperature reduces the verified retest interval to 6 months. When the material is stored over molecular sieves (3A) for anhydrous applications, a steep exotherm has been observed during initial contact in adiabatic calorimetry, necessitating slow addition and external cooling if drying more than 500 mL per batch.

    Addition of 2,5-dihydro-1H-pyrrole directly into reaction mixtures containing strong alkylating agents (methyl iodide, dimethyl sulfate) without controlled addition rate has led to thermal runaways on 10 L pilot-plant scale due to the amine’s exothermic quaternization (ΔH ≈ −85 to −110 kJ/mol estimated from analogous secondary amines). Production-scale reactors equipped with jacket cooling (ΔTjacket < 20°C), controlled addition via metering pump, and internal temperature probes with high-limit interlocks are standard when alkylation charges exceed 5 kg.

    What Makes 2,5-Dihydro-1H-Pyrrole Distinct from Its Isomers?

    Three partially hydrogenated pyrrole isomers exist, and confusion in procurement and synthetic planning often arises between 2,5-dihydro-1H-pyrrole (3-pyrroline), 2,3-dihydro-1H-pyrrole (2-pyrroline), and 3,4-dihydro-2H-pyrrole (1-pyrroline). In 2,5-dihydro-1H-pyrrole, the double bond is located at the 3,4-position, and the nitrogen atom exists as a secondary amine capable of N–H addition reactions, salt formation, and carbamate protection. The 2,3-dihydro isomer, by contrast, is a cyclic imine (C=N at the 2-position) that hydrolyzes rapidly in the presence of moisture to γ-aminobutyraldehyde, making it unsuitable for aqueous workups or long-term storage without anhydrous precautions. The 3,4-dihydro-2H-pyrrole (1-pyrroline) is also an imine, with the double bond at the 1,2-position, and is even more prone to oligomerization; its boiling point (87–89°C) overlaps with the title compound, so separation by simple distillation is not reliable. Industrial specifications for 1H-pyrrole, 2,5-dihydro- explicitly limit the 2,3-dihydro isomer content to ≤0.5% (GC) to avoid side reactions in electrophilic additions where the imine tautomer acts as a competitive nucleophile.

    A direct comparison of the fully saturated analog pyrrolidine (CAS 123-75-1) reveals fundamentally different reactivity. Pyrrolidine (b.p. 87–88°C, pKa 11.3) lacks the alkene functionality and is favored when a more nucleophilic, fully sp³-hybridized amine is required. 2,5-Dihydro-1H-pyrrole retains the ring strain (ca. 5.2 kcal/mol above pyrrolidine, estimated from hydrogenation enthalpy) and the electron-rich double bond, allowing post-functionalization via hydroboration, epoxidation, or Diels–Alder cycloaddition with electron-deficient dienophiles. The fully aromatic pyrrole (pKa of protonated form ≈ −3.8) acts as a π-excessive heteroaromatic and undergoes electrophilic substitution; it is not a nucleophilic amine under neutral or basic conditions. Thus, selection among these four compounds pivots on whether the downstream chemistry demands an alicyclic secondary amine with a latent olefin handle (2,5-dihydro), a stable saturated amine (pyrrolidine), an imine susceptible to hydrolysis (2-pyrroline), or an aromatic ring (pyrrole).

    Key Physicochemical Profiles of Pyrrole-Derived C4–C5 Cyclic Amines
    Property1H-Pyrrole, 2,5-dihydro-Pyrrolidine2,3-Dihydro-1H-pyrrole (2-pyrroline)Pyrrole
    CAS RN109-96-6123-75-15664-89-7109-97-7
    B.p. (°C, 760 mmHg)90–9287–8889–91129–131
    pKa (conjugate acid)~10.011.3~7.5 (imine)−3.8
    Ring unsaturation1 C=C, allylic amineNone1 C=N, endocyclic imineFull aromatic
    Stability to H2OStable, slow oxidationStableRapid hydrolysisStable
    Preferred storage condition2–8°C, N2, BHTRT, inert gas−20°C, anhydrousRT, dark

    When 3-Pyrroline Acts as a Dipolarophile in Cycloaddition Cascades

    In medicinal chemistry programs targeting sp³-rich heterocyclic scaffolds, 2,5-dihydro-1H-pyrrole has been employed as a strained dipolarophile in 1,3-dipolar cycloadditions with nitrones and azomethine ylides. The electron-rich double bond, combined with the allylic strain imposed by the ring, accelerates cycloaddition rates relative to acyclic allylamines. In a typical process route documented in pilot-plant campaigns, 2,5-dihydro-1H-pyrrole (1.0 equiv) is combined with a nitrone generated in situ from N-benzylhydroxylamine and paraformaldehyde in toluene at 80°C for 16 hours, producing fused isoxazolidines with diastereomeric ratios exceeding 9:1 (trans:cis) when the nitrogen atom is unprotected. The secondary amine can then be elaborated via reductive cleavage of the N–O bond or retained for further functionalization. Process safety evaluations for these cycloadditions on 50 kg scale required differential scanning calorimetry (DSC) screening of the neat reaction mixture, which showed an onset of decomposition at 180°C with an energy release of −450 J/g. Consequently, the addition of the amine is performed as a controlled semibatch operation with the internal temperature maintained below the onset of the main exotherm by at least 70°C, providing a comfortable margin in the event of cooling failure.

    Batch-to-batch variability in cycloaddition diastereoselectivity on 20 L scale was traced to residual peroxide content in the 2,5-dihydro-1H-pyrrole charge. When the peroxide value exceeded 0.7 mmol/kg, a 5–10% erosion in trans selectivity was observed, attributed to radical side-reactions that epimerize the α-stereocenter of the nitrone intermediate. The specification of ≤0.5 mmol/kg was tightened from an earlier limit of ≤1.0 mmol/kg after this investigation. Vendors now supply material pre-analysed for peroxides using an iodometric method adapted from ASTM E298-17a, and on-site quality-control laboratories re-verify the value upon receipt using a calibrated autotitrator (Metrohm 916 Ti-Touch or equivalent) with potentiometric endpoint detection.

    Within the broad class of primary and secondary allylic amines, 2,5-dihydro-1H-pyrrole exhibits a boiling point sufficiently low to permit removal by distillation from high-boiling solvents, yet sufficiently high that it does not evaporate uncontrollably during ambient-pressure handling—a practical advantage over acyclic allylamine (b.p. 53°C) when conducting reactions at elevated temperatures. This volatility window has been leveraged in the synthesis of N-Boc-3-pyrroline (b.p. 65–67°C at 1.5 mmHg), where unreacted 2,5-dihydro-1H-pyrrole is recovered by atmospheric distillation and recycled. Reported recovery rates in kilo-lab campaigns exceed 92% when the distillation bottoms are not allowed to exceed 100°C, minimizing thermal oligomerization.

    Polymer-Grade Monomer Purity and the Critical Threshold of Amine-Water Azeotrope Behavior

    For applications in precision polymer synthesis—particularly in the preparation of poly(3-pyrroline)-based anion-exchange membranes—monomer purity above 99.5% is mandatory. 2,5-Dihydro-1H-pyrrole forms a minimum-boiling azeotrope with water at approximately 86°C (azeotropic composition ca. 30% water by weight), rendering simple distillation insufficient to achieve the ultralow water content (<50 ppm) demanded by living anionic polymerization. The compound must be dried by fractional distillation from calcium hydride (CaH2) under a static nitrogen atmosphere, discarding a 10% forerun, or by passage through a column of activated neutral alumina (Brockmann I) immediately prior to polymerization. In glovebox-based living polymerization setups with sec-butyllithium initiation at −78°C in THF, water content exceeding 80 ppm in the monomer feed has been correlated with broadened molecular weight distributions (Đ > 1.4) and premature termination, as observed by GPC (RI detection, polystyrene standards). The requirement for exhaustive drying represents a cost driver that has spurred evaluation of alternative purification protocols, including azeotropic drying with toluene using a Dean–Stark trap, but loss of monomer into the distillate remains a limitation, with typical recoveries of 75–80% after two cycles.

    Free-radical polymerization of 2,5-dihydro-1H-pyrrole, though less rigorous with respect to water tolerance, is complicated by the amine’s chain-transfer activity. The N–H bond acts as a chain-transfer agent, reducing the achievable number-average molecular weight in bulk polymerization initiated by AIBN at 60°C to approximately 3,000–5,000 g/mol. This feature has been exploited deliberately in the synthesis of amine-terminated oligomers, where the degree of polymerization is controlled by the initial monomer-to-initiator ratio and the chain-transfer constant (Cs estimated at 0.012 for the N–H bond at 60°C). For production of high-molecular-weight polymers, the amine must be protected as the N-Boc or N-tosyl derivative prior to polymerization, and the deprotection step introduces additional process mass intensity, often necessitating trifluoroacetic acid in dichloromethane or hydrogenation over Pd/C, with associated EHS considerations.

    Single-Phase vs. Biphasic N-Alkylation: Equipment Implications

    An enduring operational challenge in fine chemical manufacture is the N-alkylation of 2,5-dihydro-1H-pyrrole with alkyl halides in the presence of aqueous base. Under the classic biphasic conditions (50 wt% aq. NaOH, tetrabutylammonium bromide as phase-transfer catalyst), the reaction mixture tends to emulsify on 500 L scale due to the surfactant-like properties of the quaternary ammonium salt and the partially water-soluble amine. Phase separations requiring more than 45 minutes have been documented, with rag layers stabilized by trace iron hydroxide introduced from carbon steel equipment. Transition to a homogeneous system using K2CO3 in anhydrous DMF at 60–65°C eliminated the phase-separation bottleneck, but necessitated rigorous removal of residual DMF from the product (final specification < 50 ppm by headspace GC) due to its reprotoxicity classification under REACH. The switch from biphasic to homogeneous conditions is thus contingent on the availability of thin-film evaporators (e.g., wiped-film, 0.1 m² surface area) capable of reducing high-boiling solvent carryover without thermally stressing the N-alkylated product, which undergoes retro-Michael elimination above 120°C.

    Where the production asset does not include thin-film evaporation capability, solid-liquid phase-transfer catalysis using powdered KOH in toluene with Aliquat 336 has been implemented at 100 kg batch size, achieving conversion above 95% within 8 hours and simplifying workup to a straightforward filtration and distillation. However, the hygroscopic nature of powdered KOH under ambient humidity (>60% RH) demands enclosed transfer systems or nitrogen-purged glovebags to prevent deliquescence and subsequent hydroxide-mediated oligomerization of the double bond.

    Published data on the long-term storage stability of N-alkyl-3-pyrrolines in plastic versus glass-lined containers is limited, but accelerated aging studies at 40°C/75% RH for 4 weeks indicate that iron contamination above 5 ppm catalyzes discoloration and viscosity increase, presumably via Fenton-type oxidation of the allylic position. For this reason, all product-contact surfaces in commercial-scale manufacturing and storage are specified as 316L stainless steel, glass-lined steel, or PTFE-lined, while carbon steel and copper alloys are strictly excluded.

    Handling of 1H-Pyrrole, 2,5-dihydro- is governed by UN 2924 (flammable liquid, corrosive, n.o.s.), Packing Group II, with a flash point (closed cup) of approximately −5°C (ASTM D56-22). Ventilation must maintain vapor concentrations below the occupational exposure limit, typically set at an 8-hour TWA of 1 ppm by analogy with similar cyclic secondary amines, though no specific regulatory occupational exposure limit has been assigned. Process vents are routed through packed-bed scrubbers containing dilute sulfuric acid to capture amine vapors before release.