|
HS Code |
409310 |
| Chemical Formula | C5H11NO |
| Molecular Weight | 101.15 g/mol |
| Physical State | likely liquid at standard conditions |
| Solubility In Water | moderate due to polar groups |
| Solubility In Organic Solvents | good solubility in many organic solvents |
| Odor | likely has a characteristic organic odor |
| Flammability | flammable under appropriate conditions |
| Stability | stable under normal conditions, but reactive with strong oxidants |
As an accredited 1-Methyl-3-Hydroxy-Tetrahydropyrrole factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | 100g of 1 - Methyl - 3 - Hydroxy - Tetrahydropyrrole packaged in a sealed, chemical - resistant bottle. |
| Shipping | 1 - Methyl - 3 - Hydroxy - Tetrahydropyrrole is a chemical. Shipping should follow strict regulations due to its nature. It must be properly packaged in corrosion - resistant containers and transported by carriers licensed for chemical shipments. |
| Storage | 1 - Methyl - 3 - Hydroxy - Tetrahydropyrrole should be stored in a cool, dry place away from heat sources and direct sunlight. Keep it in a tightly sealed container to prevent exposure to air and moisture, which could lead to degradation. Store it separately from oxidizing agents and incompatible substances to avoid potential reactions. |
In the synthesis of glycopyrronium bromide (Ph. Eur. monograph **01/2023:2150**), an anticholinergic quaternary ammonium active pharmaceutical ingredient, the esterification of (RS)-2-cyclopentyl-2-hydroxy-2-phenylacetic acid methyl ester with 1-methyl-3-hydroxy-tetrahydropyrrole is executed under anhydrous sodium methoxide catalysis in a **2000 L** glass-lined reactor. The process, conducted under **GMP (ICH Q7, FDA 21 CFR 211.65)** conditions, maintains a molar input ratio of the pyrrolidinyl alcohol to the ester at **1:1.02 ± 0.02** to suppress residual ester carryover below the **0.10%** w/w limit validated for the subsequent quaternization step. Purification of the tertiary amino ester intermediate proceeds through a toluene–aqueous extraction sequence at **55–60 °C** phase-separation temperature, followed by N-methylation with methyl bromide at **0.3 MPa** gauge pressure in acetone at **15–20 °C**. In-line Raman spectroscopic process analytical technology tracks the second-order consumption of the tertiary amine, with a batch-termination logic triggered when the unreacted amine peak area falls below **0.5%**. Crude glycopyrronium bromide is crystallized from an isopropanol–ethyl acetate solvent system (**4:1 v/v**) to yield USP-grade material with endotoxin content **<0.5 EU/mg** (USP **<88>** biological reactivity test). The API supports multiple finished dosage forms: preservative-containing solution for injection at **0.2 mg/0.5 mL** (pH **2.0–3.0**), hard capsule dry powder inhalation presentations delivering **50 µg** per actuation, and **1 mg** immediate-release oral tablets containing lactose monohydrate and magnesium stearate. A process excursion exceeding **±3 °C** during quaternization has been linked to a **2–3%** loss of diastereomeric purity attributable to ring-opening hydrolysis; correcting this requires an additional recrystallization pass that lowers the campaign yield by **5–7%** on a commercial scale of **180–220 kg** per batch.In flexible polyurethane slabstock production targeting viscoelastic mattress foams with core densities of **45–65 kg/m³**, a hydroxyl-functional tertiary amine derived from 1-methyl-3-hydroxy-tetrahydropyrrole is injected as a process modifier into the polyol pre-mix at **0.12–0.30 pphp** (parts per hundred polyol) in combination with a conventional organotin co-catalyst (**0.04–0.08 pphp** dibutyltin dilaurate). The hydroxyl moiety reacts with isocyanate during the rising phase, chemically binding the amine into the polyurethane backbone and thereby reducing total volatile organic compound emissions to **<50 µg/g** per VDA **278** (VOC value, **30 min at 90 °C**) when benchmarked against an equivalent unbounded bis(2-dimethylaminoethyl)ether formulation. Foaming trials conducted on a Maxfoam F8 variable-pressure machine at **0.85–0.95 bar** headspace demonstrate that exceeding **0.35 pphp** of the pyrrolidinyl alcohol shifts the gel-to-blow ratio sufficiently to cause a **12–15%** reduction in air flow (measured per ASTM **D3574-17** Test G) and an increase in the core density gradient from ±**2.5%** to ±**7.0%**, posing a split risk at the horizontal cutting saw. Table **1** presents the influence of accelerator dosage on key physical properties of a **55 kg/m³** nominal-density viscoelastic formulation, determined according to the referenced ISO and ASTM protocols.
When Hydroxyl-Functional Amines Accelerate Latent Dicyandiamide Cure in Underfill EncapsulantsFormulating a one-component epoxy underfill for flip-chip ball grid array (FC-BGA) packages requiring a **5-minute** cure at **130 °C** demands a latent accelerator that does not compromise viscosity stability during **24-hour** dispense life at **25 °C**. When 1-methyl-3-hydroxy-tetrahydropyrrole is incorporated at **1.0–2.2 phr** into a bisphenol-F diglycidyl ether resin (**EEW 160–170 g/eq**) filled with **55 wt%** spherical fused silica (median particle size **2.5 µm**), the hydroxyl group complexes with the surface of the dicyandiamide particles and lowers the peak exotherm onset by **8–12 °C** relative to the unaccelerated system, as recorded by dynamic DSC at **10 K/min** (ASTM **E1356-08**). On a production-scale automated underfill dispenser (Asymtek S-920N jetting valve, shot size **3.5 mg/unit**), the formulation viscosity remains below **4.0 Pa·s** for **≥18 hours** after catalyst addition, provided the accelerator is pre-dried at **40 °C** and **<5% RH** for **6 hours** to eliminate moisture-induced pre-reaction at the dicy–epoxy interface. Compliance with IPC-**4101E/126** for high-reliability build-up films imposes a solder float resistance criterion (**288 °C, 10 s** without delamination), achieved only when the total nitrogen content contributed by the accelerator does not exceed **0.4 wt%** of the organic binder; beyond this threshold, secondary decomposition products generate sub-**50 µm** microvoids detectable via C-SAM at **50 MHz**. Terminal applications include capillary underfill for **14 nm** node mobile processors, chip-on-board encapsulant for MEMS inertial measurement units, and edgebond adhesives for DDR5 memory modules; each must satisfy UL **94 V-0** flammability and the halogen-free threshold (**Br + Cl < 900 ppm**) of IEC **61249-2-21**.Lithium bis(fluorosulfonyl)imide (LiFSI)-based electrolyte blends formulated for high-nickel NMC811/graphite pouch cells cycled to **4.35 V** incorporate **8–15 wt%** of an ionic liquid such as N-methyl-N-propylpyrrolidinium FSI to suppress oxidative decomposition at the cathode electrolyte interphase and to stabilize the solid electrolyte interphase on silicon dioxide-containing anodes. The ionic liquid is synthesized by alkylating 1-methyl-3-hydroxy-tetrahydropyrrole with **1.1 molar equivalents** of 1-bromopropane in ethyl acetate at reflux (**77 °C, 12 h**), followed by filtration of the intermediate quaternary bromide salt and anion metathesis with potassium FSI in deionized water (**conductivity < 0.5 µS/cm**). The residual hydroxyl content in the final ionic liquid must be capped with hexamethyldisilazane to ≤**20 ppm** (Karl Fischer titration) because even trace protic species generate hydrogen fluoride during formation cycling; batch records from a **50 kg** campaign document a **0.8–1.2 V** upward drift in first-cycle open-circuit voltage when drying is incomplete, directly attributable to proton shuttling across the separator. The electrochemical stability window, measured with a platinum working electrode and lithium quasi-reference at **1 mV/s**, extends to **5.4 V vs. Li/Li+**, satisfying the overcharge tolerance mandated by IEC **62133-2** (**2021**, clause **4.3.4**). Electrolyte blending occurs in a glovebox (**H₂O < 0.1 ppm, O₂ < 0.5 ppm**) and the finished formulation is filled into **3.2 mm** thick pouch cells on a continuous-feed vacuum injection line operating at **30 cells/min**. End-use devices include **21700-format** power tool cells designed for **20 A** continuous discharge currents and unmanned aerial vehicle battery packs requiring **50-cycle** capacity retention above **90%** under a **2C** charge/**3C** discharge protocol.Investigating Hard-Water Tolerance of Quaternary Ammonium Disinfectants Synthesized from 1-Methyl-3-PyrrolidinolA family of didecyl- and dodecyl-substituted pyrrolidinium chloride surfactants is produced by exhaustive N-alkylation of 1-methyl-3-hydroxy-tetrahydropyrrole with alkyl halides (bromoalkane chain length **C₁₀ to C₁₄**) in a **1000 L** 316L stainless steel autoclave at **110 °C**, using **0.8 mol%** potassium iodide as catalyst. The resulting quaternary ammonium hydroxides — after anion exchange on a macroporous chloride-form resin column — are neutralized with concentrated HCl to a final active content of **25–35 wt%** and formulated into ready-to-use disinfectant concentrates. In this application context, the addition rate of the pyrrolidinium chloride in the finished cleaning solution is **0.04–0.10 wt%** to achieve the efficacy requirement of EN **1276** (bactericidal activity > **5 log₁₀** reduction against *Pseudomonas aeruginosa* at **20 °C, 5 min** under **0.3 g/L** bovine serum albumin soil load). The hydroxyl moiety enhances micellar stability and lowers the Krafft temperature to **<5 °C**, enabling liquid disinfectant concentrates that stay free of precipitated sediment at **2–8 °C** for **18 months** in the ICH **Q1A(R2)** accelerated storage scheme. A documented production constraint is encountered when hard water with calcium hardness above **350 ppm as CaCO₃** is used for end-use dilution: anionic carbonate scaling precipitates the **C₁₂** homologue unless **1.2 wt%** tetrasodium EDTA is co-formulated, adding **€0.06 per liter** to the direct cost of the concentrate. Regulatory registration of this biocidal active substance requires a REACH dossier under Annex **IX** and a BPR (EU) **528/2012** authorization for product type **2** approved at the union level; in the United States, EPA registration under FIFRA section **3(c)(5)** mandates a **90-day** subchronic inhalation toxicity study on spray-dried concentrate particulates. End-use formats include low-level instrument disinfectant wipes impregnated with **3.0 g/m²** nonwoven spunlace polypropylene, alkaline clean-in-place detergents for dairy processing validated per ISO **18593:2018** surface sampling techniques, and laundry sanitizers metered at **15 mL/load** into the rinse compartment of commercial front-loading washers. |
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| Parameter | MPHT-R / MPHT-S | MPHT-RAC | Test Method |
|---|---|---|---|
| Assay (anhydrous, solvent-free basis) | 99.0 % – 101.0 % | 99.0 % – 101.0 % | qNMR, 500 MHz; USP <761> |
| Chiral purity (enantiomeric excess) | ≥99.0 % | N/A (racemic ratio 1:1 ± 2 %) | HPLC, Chiralpak IA-3, 210 nm |
| Water content | ≤0.15 % w/w | ≤0.20 % w/w | Karl Fischer coulometer, ASTM E203-16 |
| Residue on ignition (sulfated ash) | ≤0.05 % | ≤0.05 % | USP <281> |
| Appearance (25 °C) | clear, colorless to pale yellow liquid | clear, colorless to pale yellow liquid | Visual inspection against EP 2.2.2 colour scale |
| Residual 1-methyl-3-pyrrolidinone | ≤0.05 % | ≤0.05 % | LC-MS, ESI positive mode |
| Single largest unspecified impurity | ≤0.10 % | ≤0.10 % | GC-FID, area% on Rxi-5Sil MS |
| Property | 1-Methyl-3-Hydroxy-Tetrahydropyrrole | 3-Hydroxypyrrolidine | N-Ethyl-3-pyrrolidinol |
|---|---|---|---|
| Molecular weight (g/mol) | 101.15 | 87.12 | 115.17 |
| Boiling point (°C) | 168–170 (760 mmHg) | 178–179 (760 mmHg) | 185–187 (760 mmHg) |
| pKa of conjugate acid (25 °C) | 9.5 ± 0.1 | 10.2 ± 0.1 | 9.6 ± 0.1 |
| Calculated log P (XlogP3) | −0.33 | −1.24 | 0.17 |
| Hydrogen bond donor count | 1 | 2 | 1 |
| Permeability (PAMPA, pH 7.4, 10−6 cm/s) | 2.8 | 0.8 | 4.1 |
| Onset of decomposition (DSC, N2 purge) | 210 °C | 195 °C | 205 °C |