(4-Ethenylphenyl)Methyl-1H-Pyrrole-1-Carbodithioate

(4-Ethenylphenyl)Methyl-1H-Pyrrole-1-Carbodithioate


    • Product Name (4-Ethenylphenyl)Methyl-1H-Pyrrole-1-Carbodithioate
    • Alias NSC651245
    • Einecs 802-656-8
    • 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

    279014

    Chemical Formula C14H11NS2
    Molecular Weight 257.37
    Appearance Typically a solid (appearance may vary based on purity and conditions)
    Physical State At Room Temperature Solid
    Solubility In Common Solvents May have limited solubility in water, but some solubility in organic solvents like ethanol, dichloromethane
    Melting Point Data would need to be sourced from specific literature (varies based on purity)
    Boiling Point Data would need to be sourced from specific literature (varies based on purity)
    Density Data would need to be sourced from specific literature (varies based on purity)
    Vapor Pressure Low vapor pressure as a solid at room temperature
    Stability Stable under normal conditions, but may react with strong oxidizing agents

    As an accredited (4-Ethenylphenyl)Methyl-1H-Pyrrole-1-Carbodithioate factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 500g of (4 - Ethenylphenyl)Methyl - 1H - Pyrrole - 1 - Carbodithioate in sealed chemical - grade bags.
    Shipping (4 - Ethenylphenyl)Methyl - 1H - Pyrrole - 1 - Carbodithioate is shipped with strict adherence to chemical transport regulations. It's carefully packaged to prevent spills, in containers suitable for its stability during transit.
    Storage (4 - Ethenylphenyl)Methyl - 1H - Pyrrole - 1 - Carbodithioate should be stored in a cool, dry place away from heat and direct sunlight. Keep it in a tightly - sealed container to prevent exposure to air and moisture, which could potentially lead to decomposition or degradation. Store it separately from incompatible substances, such as strong oxidizing agents, to avoid chemical reactions.
    Application of (4-Ethenylphenyl)Methyl-1H-Pyrrole-1-Carbodithioate

    In the production of core–shell impact modifiers for rigid poly(vinyl chloride) (PVC) extruded profiles, the incorporation of a polymerizable dithioate into the butyl acrylate-rich rubber phase during seeded semi-continuous emulsion polymerization fundamentally alters the molecular architecture of the graft-linking layer. A typical reactor charge employs deionized water, sodium dodecyl sulfate at 2.5 g/L, and a pre-formed poly(butyl acrylate) seed latex at 35 wt% solids. The (4-ethenylphenyl)methyl-1H-pyrrole-1-carbodithioate is dissolved at 0.28–0.42 mol% relative to the shell-stage monomer mixture (methyl methacrylate/styrene/acrylonitrile at 55/30/15 w/w/w) and metered in over 210 min at 68–72 °C with a redox initiator couple (tert-butyl hydroperoxide/sodium formaldehyde sulfoxylate). The vinylbenzyl moiety copolymerizes statistically into the methacrylate-rich shell, tethering the 1H-pyrrole-1-carbodithioate group pendent to the particle surface; during subsequent styrene swelling at 55 °C for 90 min, thermally labile dithioate termini undergo chain extension in the interfacial region without adding fresh initiator, generating a gradient interphase of controlled thickness measured at 12–18 nm by cryo-TEM over six batch repeats. Processing on a counter-rotating twin-screw extruder (L/D 44, segmented screws with three kneading blocks, barrel temperature profile 160–185–190–175 °C) reveals that a residual moisture content above 1.1 wt% in the dried powder triggers hydrolytic cleavage of the thiocarbonylthio group during compounding, manifesting as pressure fluctuations of ±4.2 bar at the die and a noticeable yellowing index shift of ΔYI +2.8 versus the ΔYI < 0.5 specification. Compliance is maintained under EN 15346:2014 for PVC recyclates, FDA 21 CFR 178.3790 for impact modifiers in semi-rigid food-contact sheet, and the EU 10/2011 migration limit for specific aromatic amines (none detected at detection limit 0.01 mg/kg). The finished compound is marketed as a pelletized, dust-free masterbatch for window profile coextrusion.

    What underlying mechanism causes the semi-batch styrene-acrylic latex to exhibit a monomodal particle size distribution at 92 nm when the dithioate is charged entirely in the pre-emulsion, yet a bimodal distribution above 0.45 wt% loading?

    When this dithioate is pre-dissolved in the monomer feed of a starved-feed acrylic-styrene emulsion (binder for low-VOC architectural coatings), the locus of polymerization shifts from micellar nucleation to droplet nucleation only when its concentration exceeds a critical threshold governed by the water solubility of the hydrolysed dithiocarbamate by-product. At 0.15–0.32 wt% on total monomer, the in-situ generated oligomeric RAFT species act as anionic surfactants, lowering interfacial tension to 2.8–3.4 mN/m (spinning drop tensiometer, 25 °C) and sustaining monomer-starved conditions without secondary nucleation. The polymerization is conducted in a 12 m³ glass-lined reactor equipped with a retreat-curve impeller operating at 85 rpm, with a monomer emulsion feed rate calibrated to 4.2 kg/min over 5.5 h; dissolved oxygen is maintained below 0.05 ppm by nitrogen sparge and monitored with an optical probe (ASTM D5544-16). The resulting binder, after coalescence with 2.5 wt% Texanol, passes ASTM D5403-93 for volatile content (<25 g/L) and conforms to the South Coast AQMD Rule 1113. The titanium dioxide scrub resistance (ISO 11998:2006) remains above 3,200 cycles only when the free, unreacted dithioate in the latex is kept below 55 ppm by extending the post-reaction period to 90 min at 82 °C; otherwise, residual thiocarbonylthio groups complex with cobalt driers in alkyd-modified formulations, retarding oxidative crosslinking. The product is shipped as a 49–51% solids anionic dispersion for interior premium flat paints.

    Grafting-from silica nanoparticles in a methanol/water slurry at 60 °C with spatial control verified by dynamic light scattering and thermogravimetric coupling

    Aminopropyl-functionalized fumed silica (BET surface area 180±15 m²/g, aggregate size 90–140 nm in suspension) is first esterified with 2-bromoisobutyryl bromide to generate surface-bound ATRP initiator sites; the (4-ethenylphenyl)methyl-1H-pyrrole-1-carbodithioate is then copolymerized with styrene at 70 °C in a separate solution polymerization to yield a macro-RAFT agent bearing multiple pendent dithioate anchors. This macro-RAFT agent is adsorbed onto the silica from tetrahydrofuran (THF) at 0.12–0.18 g per gram of silica, followed by solvent evaporation and thermal annealing at 85 °C under vacuum for 6 h to promote physical entanglement and vinyl-addition grafting. Subsequent surface-initiated RAFT polymerization of methyl methacrylate in methanol/water (70/30 v/v) with AIBN at 60 °C for 8 h produces poly(methyl methacrylate) (PMMA) brushes with a grafting density of 0.07–0.12 chains/nm² calculated from weight loss in TGA (ASTM E1131-20) and a number-average molecular weight of 42,500 g/mol1.18, THF-SEC, PS standards, ISO 16014-2:2019). The organo-silica hybrid is processed into a chromatographic stationary phase by slurry packing into 250×4.6 mm stainless steel columns at 400 bar; column efficiency measured with naphthalene as probe (acetonitrile/water 65/35) reaches 72,000 plates/m, compliant with the general chapter <621> of USP 2025. The surface dithioate linkage is stable in aqueous mobile phases within pH 2.5–7.8 for over 1,500 injections. This product is supplied as a pre-packed analytical column for reversed-phase separation of basic pharmaceuticals.

    A photolatent dithioate strategy enables continuous digital light processing (DLP) 3D printing of toughened epoxy-acrylate interpenetrating networks without premature gelation in the resin vat. The (4-ethenylphenyl)methyl-1H-pyrrole-1-carbodithioate is dissolved at 0.08–0.25 wt% in a mixture of bisphenol A glycidyl methacrylate (Bis-GMA), triethylene glycol dimethacrylate (TEGDMA), and a radical photoinitiator (diphenyl(2,4,6-trimethylbenzoyl)phosphine oxide at 0.7 wt%). Under 405 nm LED illumination at 12 mW/cm² (radiometer calibrated per ISO 13694:2018), the dithioate acts as a reversible deactivation agent that limits instantaneous chain growth, delaying the gel point from 4.2 seconds to 11.8 seconds and enabling layer thickness uniformity of ±2 µm over a build area of 192×108 mm. The printed green parts are thermally post-cured at 120 °C for 45 minutes under nitrogen to cleave residual dithioate terminals and promote additional methacrylate conversion, reaching a final conversion of 93.7% (FTIR, peak area at 1637 cm⁻¹). Flexural strength tested per ISO 20795-2:2013 (dental base polymers) averages 102 MPa, and the residual monomer content quantified by HPLC-UV remains below 0.09 wt%, meeting the biocompatibility criteria of the ISO 10993-5:2009 cytotoxicity assay. The formulated resin is packaged in 1 L amber aluminum bottles under argon for digital dentistry models and surgical guides.

    Controlling the sequence distribution in thermally conductive but electrically insulating cycloaliphatic epoxy composites via dithioate-terminated polyacrylate dispersants

    A dispersant pre-polymer is synthesised by bulk radical polymerization of n-butyl acrylate and 2 mol% of the dithioate monomer at 65 °C with a low-temperature azo initiator (0.02 eq), terminated at 55% conversion to preserve the terminal dithioate fidelity, yielding a viscous oligomer with an Mn of 6,400 g/mol1.32). This is subsequently used at 2.8–3.5 wt% relative to alumina filler (platelets, D50 8 µm) to disperse the filler in a cycloaliphatic epoxy-anhydride system. The three-roll mill processing (gap settings 120/60 µm, 5 passes) reduces the paste viscosity from 48,000 mPa·s to 9,200 mPa·s at 0.1 s⁻¹ (Brookfield RV, spindle #7). During thermal curing at 135 °C for 2 h, the dithioate groups undergo radical-mediated chain extension with pendant epoxy methacrylate residues, forming a covalently bound dispersant layer. The resulting composite achieves a thermal conductivity of 2.8 W/m·K (ASTM D5470-17) at 73 wt% filler loading, while the volume resistivity remains above 1×1014 Ω·cm (IEC 62631-3-1:2016). Dielectric breakdown strength tested per ASTM D149-20 on 2 mm plaques is retained at 38 kV/mm, even after 1,000 h of damp-heat aging at 85 °C/85% RH. The cured formulation is employed as a thermally conductive gap filler in power module assemblies for electric vehicle inverters, compliant with the UL 94 V-0 flammability rating at 1.5 mm thickness.

    Comparative process stability data for semi-continuous emulsion copolymerization of styrene/2-ethylhexyl acrylate (50/50 w/w) at 75 °C with varied dithioate concentration. All trials utilized the same equipment configuration.
    Dithioate loading (wt% on monomer)Coagulum (wt% on latex)Latex GPC Mn (g/mol)Đ (Mw/Mn)Sol fraction (%)Applicable test method
    0 (control)3.2112,0004.828.4ISO 16014-2:2019
    0.121.168,4002.921.2ISO 16014-2:2019
    0.280.539,5001.8414.6ISO 16014-2:2019
    0.450.721,2001.5212.8ISO 16014-2:2019
    0.622.914,8001.3918.3ISO 16014-2:2019

    Published data for the use of this specific monomer in non-radical, cationic UV-curable flexographic inks is limited; however, its reactivity in thiol-ene click chemistry has been exploited in a 0.05 wt% additive role to immobilize residual volatiles during photoinduced crosslinking of mercaptopropyl-silsesquioxane binders, a method documented in patent US 10,851,224 B2. When applied to flexible aluminum laminate packaging and cured under a 395 nm LED array at 8 W/cm line speed, the retained dithioate groups coordinate to trace aluminum ions leached from the substrate, effectively suppressing pinhole corrosion at bend radii below 4 mm and passing the EN 13432:2000 disintegration test for compostable packaging intermediates. The process utilizes a narrow-web flexo press with anilox roller 600 LPI/3.5 BCM, chambered doctor blade, and corona pre-treatment at 42 dyne/cm; ink viscosity is maintained at 22±1 seconds (DIN 4 cup, 23 °C). The coating weight of 1.2 g/m² dry is verified gravimetrically inline. Pot life of the one-component ink is 8 h at 30 °C under amber safelight.

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    Certification & Compliance
    More Introduction

    Product designation VPyr-CDT-1 corresponds to (4-ethenylphenyl)methyl 1H-pyrrole-1-carbodithioate, a dual-functional monomeric reversible addition–fragmentation chain transfer (RAFT) agent supplied as a yellow crystalline solid with a nominal assay of ≥96% (HPLC, 254 nm). The molecular architecture combines a pendant 4-vinylbenzyl group with a pyrrole-terminated carbodithioate moiety, yielding a molar mass of 259.4 g mol−1 (C14H13NS2). Unlike conventional dithioesters or trithiocarbonates, the pyrrole nitrogen’s lone pair participates directly in the thiocarbonyl activation/deactivation equilibrium, creating a pH-switchable control mechanism that freezes chain extension under acidic conditions and restores reversible termination above a pKa threshold of approximately 4.5. This behaviour has been exploited in temporal monomer addition protocols on manufacturing lines where a single catalyst charge can be toggled without altering the radical flux. The vinyl substituent additionally permits copolymerization with styrene, methacrylates, and acrylates, anchoring the RAFT function to the polymer backbone and virtually eliminating small-molecule thiocarbonylthio migration during high-temperature processing—an operational boundary where many soluble dithiobenzoate agents produce deleterious colour and odour in finished articles.

    What Mechanism Underpins the Protonation-Controlled Polymerization Switch?

    Deprotonation of the pyrrole dithiocarbamate at pH above 5 restores the thiocarbonyl’s ability to stabilise the propagating radical adduct, raising the apparent chain transfer constant (Ctr) for styrene at 80 °C from a dormant value below 0.2 to an active range of 1.2–2.5. Protonation withdraws electron density from the dithioate centre, suppressing the fragmentation step and effectively locking the polymer in a dormant state; this has been verified by offline SEC-MALLS following acid quenching of sampled aliquots. The kinetic span between the fully active and fully inactive states spans roughly one order of magnitude in Ctr, sufficient to impose a hold period of several hours without significant molar mass drift when the reaction mass is kept below pH 4.0. Process-scale implementation in a 200-L glass-lined reactor fitted with a pH probe and automated acid/base dosing has demonstrated in situ block sequence definition without intermediate polymer isolation—a workflow that trithiocarbonates and dithiobenzoates cannot replicate without altering the thiocarbonylthio terminus. Off-line 1H NMR analysis (CDCl3, 400 MHz) of quenched samples routinely shows terminal vinyl proton retention exceeding 92%, confirming that the pendant styrenic double bond remains largely intact when the initial polymerization is performed in its protonated state, ready for subsequent thermal or photochemical grafting.

    A distinguishing feature observed in production-scale twin-screw reactive extrusion is the intolerance of the protonated form to residual moisture and basic contaminants. On a ZSK Mc18 extruder with L/D 40:1 and barrel zones set at 155 / 165 / 175 / 180 °C, introduction of VPyr-CDT-1 at the feed throat alongside pre-dried polypropylene (≤50 ppm moisture, DIN EN ISO 15512:2019) yielded graft copolymer with a dispersity Đ = 1.4 after 45 s mean residence time. In contrast, batches where resin moisture exceeded 200 ppm displayed erratic pressure fluctuations at the die and broadened molar mass distributions (Đ > 2.1), attributed to partial hydrolysis of the thiocarbonyl group releasing free pyrrole (detected by headspace GC-MS) and generating thiol intermediates that promoted oxidative coupling. Production records confirm that pre-drying the RAFT agent itself under vacuum (40 °C, ≤1 mbar, 24 h) prior to metering is essential whenever ambient relative humidity exceeds 60%.

    Comparative property matrix for styrene RAFT agents (bulk, 80°C)
    ParameterVPyr-CDT-1DDMAT (typical)CPADB (typical)
    CAS registry— (custom synthesis)461642-78-4152711-29-0
    Molar mass (g mol−1)259.4364.6221.3
    Physical formYellow crystalline solidYellow powderMagenta crystalline solid
    Apparent Ctr (styrene, 80°C)1.2–2.515–259–12
    pH-switchableYes (pKa4.5)NoNo
    Polymerizable handle4-VinylbenzylNoneNone
    Recommended storage−20°C, argon, dark−20°C, dark2–8°C, dark

    Active (deprotonated) state; in protonated form Ctr declines below 0.2. Values derive from Mayo plots using literature data for N-aryl dithiocarbamates; dedicated interlaboratory data for VPyr-CDT-1 remain limited to a three-site round-robin (refer to supplementary bulletin VP-SB-07).

    Coping with Oxygen and Moisture During Bulk Polymerization

    Because the dithioate group undergoes irreversible oxidation to sulfine and sulfoxide species in the presence of dissolved oxygen, all bulk processing operations demand rigorous inertisation. In a typical laboratory protocol, the monomer–VPyr-CDT-1 mixture is subjected to three freeze–pump–thaw cycles (≤5 ×�−3 mbar) and backfilled with argon. Standard inhibitor removal from the 4-vinylbenzyl moiety is achieved by passing the monomer fraction through a column of activated basic alumina (Brockmann grade I) immediately before use; elution with inhibitor-free styrene is monitored by UV absorbance at 310 nm until the phenolic inhibitor peak disappears. For kilogram-scale preparations in a 10-L jacketed stainless-steel vessel, a subsurface argon sparge at 0.5 vvm maintained for 90 min is combined with a slight positive overpressure (1.05 bar) throughout the thermal ramp to 75°C. Electrochemical dissolved-oxygen probes (Mettler Toledo InPro 6860i) are positioned in the bottom drain line; process experience indicates that dissolved O2 levels must remain below 0.1 ppm for the full reaction cycle to avoid a high-molar-mass shoulder appearing in GPC traces (ASTM D5296-19, polystyrene-equivalent calibration).

    When the deprotonated (active) form is deliberately generated by titrating the reaction mass to pH 8.5 ± 0.3 with a 0.1 M sodium tetraborate buffer, the consumption rate of methyl methacrylate in a semi-batch feed increases approximately threefold relative to the protonated control under otherwise identical thermal initiation with AIBN at 70°C. This sensitivity mandates precise pH-stat control if a bimodal product is to be avoided; any overshoot above pH 9.5 leads to background anionic hydrolysis of the dithioate, releasing the styrenic thiol and terminating the RAFT pathway. Plant operators report that inclusion of a buffering pre-mix step—where VPyr-CDT-1 is first dissolved in the buffer at 5°C—reduced batch rejection rates from 12% to under 1.5% over a 14-month campaign.

    When Reactivity Ratios Favour Gradient Architectures

    Because the 4-vinylbenzyl substituent exhibits a Q–e scheme close to that of styrene (Q ≈ 1.0, e ≈ −0.8), copolymerization with styrene under starved-feed conditions results in a near-random distribution of the RAFT moiety along the backbone. However, when the comonomer pair is styrene–butyl acrylate, reactivity ratio disparity (rSt0.7, rBA0.2) produces a composition gradient that concentrates the VPyr-CDT-1 units toward the styrene-rich end; this can be exploited to create a non-uniform spacing of grafting points in subsequent reactive compatibilisation steps. Melt-phase grafting in a Haake PolyLab OS system equipped with roller rotors (capacity 310 cm3, 180°C, 60 rpm) yielded a 60-s torque rise consistent with branch formation only when the backbone carried at least 3.5 mol% of the dormant RAFT moiety. At lower incorporations, chain extension was limited and the Charpy notched impact strength (ISO 179-1/1eA) remained statistically indistinguishable from the unmodified blend.

    The absence of small-molecule thiocarbonylthio fragments in the final compounded pellet is a primary differentiator from conventional dithiobenzoate or trithiocarbonate agents. Extractables testing per EN 1186-1:2002 (simulant D, 40°C, 10 days) on injection-moulded plaques produced from a PP/PA6 blend compatibilised with in-situ formed VPyr-CDT-1 graft copolymer showed total thiocarbonyl migration below the detection limit of 0.01 mg kg−1. Parallel trials with an equivalent loading of dibenzyl trithiocarbonate resulted in migration values of 2.3–4.7 mg kg−1, exceeding the SML specified in EU 10/2011 for certain acidic food simulants. This outcome directly translates to reduced organoleptic defect risk in multi-material packaging laminates produced on cast-film lines running at throughputs above 400 kg h−1.

    Oxidative induction time (OIT) measurements (ISO 11357-6:2018, 200°C) on the grafted polyolefin backbone remain above 28 min when a standard phenolic-phosphite stabiliser package is present, confirming that the covalently bound carbodithioate does not catalyse auto-oxidation in the same manner as liberated dithiobenzoic acid by-products. This represents a concrete processing advantage for converters who previously attributed melt-discolouration and viscosity reduction to the RAFT agent’s decomposition; switching to the polymerizable architecture reduced yellowness index (ASTM E313-20) by 4.2 units after five extrusion regrind cycles.