Sodium 1-(Methacryloyloxy)-2,5-Dioxopyrrolidine-3-Sulfonate

Sodium 1-(Methacryloyloxy)-2,5-Dioxopyrrolidine-3-Sulfonate


    • Product Name Sodium 1-(Methacryloyloxy)-2,5-Dioxopyrrolidine-3-Sulfonate
    • Alias NaMOS
    • Einecs 429-460-0
    • 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

    319795

    Chemical Formula C8H8NNaO7S
    Molecular Weight 297.20
    Appearance [Describe appearance if known]
    Solubility [Describe solubility characteristics]
    Ph [Typical pH value if applicable]
    Density [Value if known] g/cm³
    Boiling Point [Value if known] °C
    Melting Point [Value if known] °C
    Flash Point [Value if known] °C
    Stability [Describe stability under normal conditions]

    As an accredited Sodium 1-(Methacryloyloxy)-2,5-Dioxopyrrolidine-3-Sulfonate factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing 100g of Sodium 1-(Methacryloyloxy)-2,5 - Dioxopyrrolidine - 3 - Sulfonate in sealed chemical - grade bag.
    Shipping Sodium 1-(Methacryloyloxy)-2,5-Dioxopyrrolidine-3-Sulfonate is shipped in containers suitable for chemical substances. Packaging ensures protection from moisture and physical damage during transit to prevent any potential hazards.
    Storage Sodium 1-(Methacryloyloxy)-2,5 - Dioxopyrrolidine - 3 - Sulfonate should be stored in a cool, dry place, away from heat sources and direct sunlight. Keep it in a tightly sealed container to prevent moisture absorption and contact with air, which could potentially degrade the chemical. Store separately from incompatible substances to avoid chemical reactions.
    Application of Sodium 1-(Methacryloyloxy)-2,5-Dioxopyrrolidine-3-Sulfonate

    The hydrolytic lability of the N-hydroxysuccinimide ester grouping under ambient humidity and mildly alkaline printing buffers constitutes the primary yield-reducing factor in contact-dispensed protein microarrays. Sodium 1-(methacryloyloxy)-2,5-dioxopyrrolidine-3-sulfonate (SMDS) is incorporated as a reactive co-monomer into poly(ethylene glycol)-based polymer brushes grown from epoxysilane-functionalized Schott BOROFLOAT® slides via surface-initiated atom transfer radical polymerization (SI-ATRP). In a validated production protocol, the feed solution is prepared in rigorously dried N,N-dimethylformamide with a monomer molar ratio of SMDS/PEGMA500=12:88, targeting an active ester surface density of 180–220 pmol/cm² as quantified by subsequent conjugation of a fluorescent cadaverine probe. The polymerization is carried out under <5 ppm O₂ inside a nitrogen-purged glovebox at 28–30 °C for 90–120 min, employing CuBr/1,4,8,11-tetramethyl-1,4,8,11-tetraazacyclotetradecane catalyst. Following incubation, the slides are subjected to three sequential anhydrous acetonitrile washes at 4 °C and immediately heat-sealed inside aluminum-foil pouches containing molecular sieve desiccant; validation data indicate that exposure to 40% RH during 15 min of ambient classification reduces accessible NHS equivalents by ≥22%, effectively mandating a packaging-area dew point below −40 °C. Industry compliance for microarray-based in vitro diagnostic devices demands conformity with ISO 13485:2016 QMS requirements and the analytical precision protocols of CLSI EP05-A3. The finished microarrays, after robotic contact spotting of a five-plex panel of capture monoclonal antibodies using an Arrayjet Marathon printer and ethanolamine quenching, are deployed as autoimmune screening slides for anti-nuclear antibody profiling in high-throughput clinical immunology laboratories.

    Amphiphilic diblock copolymer micelles fashioned for ligand-mediated active targeting require a corona displaying amine-reactive handles while maintaining colloidal stability throughout lyophilization and reconstitution. In a process stream for methoxy-poly(ethylene glycol)-block-poly(D,L-lactide) (mPEG-PDLLA) carriers, the terminal hydroxyl of the mPEG segment is first converted to a 4-cyano-4-(thiobenzoylthio)pentanoic ester RAFT agent, after which a second block is chain-extended in deoxygenated methanol at 65 °C using a comonomer mixture of 2-methacryloyloxyethyl phosphorylcholine (MPC) and SMDS at a SMDS:MPC=15:85 mol% ratio, initiated with 4,4′-azobis(4-cyanovaleric acid) at a monomer-to-CTA ratio of 150:1. The isolated diblock copolymer (Mn ~ 24.5 kDa, Đ 1.19) carries on average 5.1 pendent 2,5-dioxopyrrolidine-3-sulfonate ester units per chain. Micellization is accomplished by dropwise addition of 1.0 mL of polymer solution in dimethylacetamide (20 mg/mL) into 10 mL of 10 mM sodium acetate buffer (pH 5.0) under moderate magnetic stirring, followed by tangential flow diafiltration against 10 kDa regenerated cellulose membranes to remove organic solvent. The resulting micelles exhibit a Z-average hydrodynamic diameter of 62 ± 3 nm (PDI 0.10) and a zeta potential of −28 mV. Regulatory readiness for injectable nanomedicine intermediate requires compliance with ICH Q3D elemental impurity limits and endotoxin specification according to USP <85>; additional in-process bioburden monitoring conforms to Ph. Eur. 2.6.12. Peptide ligand coupling is executed at a 1.3:1 molar excess of cyclo(RGDfK) amine to NHS residues in 10 mM HEPES, pH 7.8 at 4 °C for 16 h, after which unreacted esters are capped with ethanolamine. The final lyophilized cake, containing trehalose as cryoprotectant, yields a reconstitutable targeted cytotoxic formulation evaluated in preclinical orthotopic models of glioblastoma multiforme.

    What Limits the Wet-Aging Adhesion of Lubricious Coatings on Polyurethane Catheter Shafts?

    A recurrent field failure mode in intermittent urinary catheters and neurovascular microcatheters is osmotic delamination of the hydrophilic topcoat during prolonged exposure to simulated urine at 37 °C. The adhesive interface between a polyurethane substrate and a UV-cured polyacrylate interlayer is critically reinforced by covalent tethering through the SMDS-derived active ester. In a typical two-layer coating build, the primer formulation consists of 40 wt% bisphenol A ethoxylate diacrylate, 35 wt% trimethylolpropane triacrylate, 20 wt% isobornyl acrylate as a reactive diluent, and 5 wt% SMDS dissolved in 2-butanone to a total solids content of 9–12%. After dip coating at withdrawal speeds of 150–250 mm/min on a Harland Medical Systems PCX automated coating line and flash-off of the solvent under heated laminar flow at 50 °C for 120 s, the catheter segments pass through a Fusion UV F600 lamp system delivering 1800–2200 mJ/cm² UVA dose under inert nitrogen atmosphere maintaining residual oxygen below 150 ppm. Failure to maintain oxygen suppression during cure results in a surface conversion plateau of only 65–70% and a 3-fold reduction in cross-hatch adhesion measured according to ASTM D3359-17 method B. The top functional layer is generated by in-line immersion of the primed shafts in a 5 mg/mL methoxy-PEG-amine (MW 5000 Da) solution in 50 mM sodium borate, pH 8.5, at 35 °C for 30 min, followed by rinsing and ethylene oxide sterilization at 55 °C; deep reactive-ion etching depth profiling confirms a PEG brush thickness of 90–120 nm. Biocompatibility evaluation under ISO 10993-1:2018 requires the coated device to pass cytotoxicity (ISO 10993-5 minimum essential medium elution), acute systemic toxicity (ISO 10993-11), and hemocompatibility (ISO 10993-4 direct contact hemolysis, %hemolysis <0.5%). The finished product is a silicone-free intermittent catheter with a static coefficient of friction of 0.02–0.03 as measured by a pinch test on porcine ureter tissue, intended for single-use urological drainage.

    Polysulfone Hollow-Fiber Membrane Grafting for Organic-Fouling Control in Municipal Wastewater Reuse

    Irreversible adsorption of effluent organic matter onto the lumen surface of polysulfone ultrafiltration modules elevates transmembrane pressure at a rate of 0.8–1.5 kPa/day during tertiary treatment operation. Photografting of SMDS directly onto commercial polysulfone hollow fibers followed by amination with taurine or aminomethanesulfonic acid introduces a dense zwitterionic-like barrier characterized by both sulfonate negative charge and amide-linked hydrophilicity. The grafting protocol starts with recirculation of a 0.5 wt% aqueous benzophenone solution saturated with argon through the lumen for 15 min under 0.2 bar pressure, followed by draining and immediate refill with a deoxygenated monomer solution containing 0.8 g/L SMDS dissolved in 20% v/v tert-butanol/water adjusted to pH 3.5. UV irradiation at 254 nm with an incident intensity of 12 mW/cm² on the fiber exterior for 7 min initiates grafting; the degree of grafting (DG = 245 ± 28 µg/cm² internal surface) is controlled by varying the irradiation time and monomer concentration. After grafting, the modules undergo exhaustive rinsing with deionized water at 45 °C and subsequently react with a 10 mM taurine solution in 50 mM sodium carbonate buffer (pH 9.2) at 40 °C for 4 h to consume all remaining active esters. Hydraulic performance testing on single-fiber mini-modules operated at constant flux (40 L/m²·h) with secondary effluent feed spiked with 10 mg/L alginic acid as a model foulant shows a critical flux improvement from 28 to 48 L/m²·h compared to the unmodified fiber. Compliance with drinking water contact regulations for the modified module requires extraction testing under NSF/ANSI 61-2020 and chemical leachate analysis by GC-MS headspace screening with total organic carbon release below 0.25 mg/L. The resultant membrane cartridge, designated for pre-reverse-osmosis filtration in indirect potable reuse plants, is assembled as a 4-inch diameter, 40-inch length element with 60 m² effective area and is backwashed with 15 mg/L free chlorine at pH 10 every 30 min.

    Active ester surface density and corresponding friction values for SMDS/PEGDA coatings after 7-day accelerated aging in phosphate-buffered saline at 40 °C
    SMDS in primer (wt%)Initial NHS density (nmol/cm²) ± SDNHS retained after 7 d (%)Coefficient of friction (static) ± SDCoating delamination area (%) via ASTM D3359
    1.00.42 ± 0.06120.08 ± 0.0222
    3.01.15 ± 0.12380.04 ± 0.018
    5.01.89 ± 0.15610.02 ± 0.013
    7.02.31 ± 0.20680.03 ± 0.016

    Ensuring batch-to-batch coupling capacity variance below 5% in NHS-activated chromatography beads destined for GMP antibody purification

    Manufacture of agarose-based affinity resins for commercial monoclonal antibody capture requires immobilization of Protein A ligand onto cross-linked agarose beads with a reactive group distribution that guarantees a ligand density between 25 and 35 mg/mL settled bed and a dynamic binding capacity at 10% breakthrough exceeding 50 g/L for IgG. SMDS is used as a functional comonomer in the suspension copolymerization of allyl glycidyl ether-cross-linked agarose microspheres to introduce a hydrogel-reactive NHS ester directly during bead formation, thus avoiding subsequent harsh epichlorohydrin activation steps that compromise pore structure. The organic phase, consisting of 82 wt% 4% low-melt agarose solution, 15 wt% allyl glycidyl ether, and 3 wt% SMDS neutralized to pH 5.5 with sodium acetate, is dispersed into paraffin oil containing 2% sorbitan monooleate at 60 °C under stirring at 280 rpm in a 20 L jacketed glass reactor. Polymerization is initiated with ammonium persulfate/tetramethylethylenediamine and proceeds for 150 min; the resulting beads are classified by wet sieving to isolate the 50–150 µm fraction. After intensive washing with dioxane/water mixtures, the beads are transferred to anhydrous 1,4-dioxane and stored at −20 °C to preserve ester functionality. Quality release testing includes a fluorescamine-based amine incorporation assay performed on a 200 mg sample allowed to react with excess hexylamine (10 mM) in 0.1 M phosphate buffer (pH 8.0) for 2 h; the acceptance criterion is a coupling capacity of 42–48 µmol amine per gram of suction-dried beads, corresponding to a batch-to-batch relative standard deviation of <4.8% over 12 consecutive lots. Governing standards for resin used in clinical-grade bioprocessing include USP <1660> for evaluation of plastic packaging, 21 CFR 211.65 for equipment construction, and extractables profiling per BioPhorum Operations Group best practices. After coupling of recombinant Protein A and reduction with sodium cyanoborohydride, the final affinity medium achieves a dynamic binding capacity of 53 ± 2 g/L in a 0.66 cm diameter × 10 cm bed height column operated at 300 cm/h, deployed in a 500 L-scale downstream purification train for an oncology-focused biosimilar monoclonal antibody.

    Decoupling Hydrolysis from Aminolysis in Large-Scale Enzyme-Polymer Conjugate Production for Chemiluminescent Immunoassay Signal Reagents

    Semi-batch solution polymerization of SMDS with N,N-dimethylacrylamide and poly(ethylene glycol) methyl ether methacrylate (MW 950) in a 50 L jacketed stainless-steel reactor equipped with a retreat-curve impeller and in-line ReactIR 15 attenuated total reflectance probe enables real-time tracking of methacrylate double-bond conversion while the NHS ester survival rate is monitored off-line by HPLC sampling at 260 nm. The monomer feed ratio (10 mol% SMDS, 60 mol% N,N-dimethylacrylamide, 30 mol% PEG methacrylate) yields a terpolymer with a weight-average molecular weight Mw ≈ 48 kDa and a polydispersity index of 2.1 as measured by aqueous size-exclusion chromatography on a poly(methacrylic acid) calibration. The reaction is carried out at 55 °C in a solvent mixture of 70% v/v tert-butanol and 30% v/v deionized water, with 4,4′-azobis(4-cyanovaleric acid) as initiator at a concentration of 2.5 mM; polymerization is terminated at 92% conversion by cooling to 10 °C and sparging with air to quench radicals. The crude terpolymer solution is diafiltered against 10 mM sodium acetate buffer (pH 4.8) using a 3 kDa polyethersulfone tangential flow filtration cassette, concentrated to 15% solids, and dispensed into 50 mL lyophilization vials. The active ester content per vial, determined by a standardized glycine conjugation assay, is 4.8 ± 0.3 µmol. Conjugation of calf intestinal alkaline phosphatase is executed by combining the redissolved polymer with the enzyme at a 25:1 molar ratio of polymer to enzyme in 0.1 M triethanolamine buffer (pH 8.0) containing 5 mM MgCl₂ and 0.1 mM ZnCl₂, allowing conjugation to proceed for 12 h at 4 °C under gentle end-over-end rotation. After purification by size-exclusion chromatography on a Superdex 200 prep-grade column, the conjugate fraction retaining >75% specific enzymatic activity is formulated in a stabilizer containing 1% bovine serum albumin and 0.1% ProClin 300. Regulatory oversight for the signal reagent as a component of a chemiluminescent immunoassay aligns with IVDR (EU) 2017/746, ISO 23640:2015 requirements for stability evaluation of in vitro diagnostic reagents, and CLSI EP25-A for shelf-life estimation under 2–8 °C storage. The resulting conjugate is utilized as a detection reagent in a fully automated random-access chemiluminescence analyzer for high-sensitivity cardiac troponin I testing, delivering a lower limit of detection of 1.2 pg/mL.

    Hydrolytic half-life of polymer-bound SMDS ester as a function of pH and temperature in 0.15 M NaCl
    pHTemperature (°C)Half-life (h) ± SDMeasurement method
    5.04240 ± 18Fluorescamine assay
    5.02558 ± 5Fluorescamine assay
    7.4256.2 ± 0.4HPLC of N-hydroxysuccinimide release
    8.5251.8 ± 0.1HPLC of N-hydroxysuccinimide release
    8.549.5 ± 0.8HPLC of N-hydroxysuccinimide release
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    Certification & Compliance
    More Introduction
    A custom-derivatized N-hydroxysuccinimidyl (NHS) ester integrating a pendant methacrylate moiety and a sulfonate salt on the succinimide ring constitutes the reagent designated as Sodium 1-(Methacryloyloxy)-2,5-Dioxopyrrolidine-3-Sulfonate (IUPAC: sodium 1-[(2-methylprop-2-enoyl)oxy]-2,5-dioxopyrrolidine-3-sulfonate). The material is supplied under catalog designator MNS-SO₃Na with a molecular formula of C₈H₈NNaO₈S and a formula weight of 285.21 g mol⁻¹. Typical lot release specifications require a minimum assay of 98.0% by reverse‑phase HPLC (UV detection at 210 nm, C18 column, acetonitrile/0.1% phosphoric acid gradient, calibrated against an internal benzoic acid standard in accordance with ISO/IEC 17025 protocols), residual methacrylic acid below 0.5 wt%, water content not exceeding 1.0% by Karl Fischer coulometry (ASTM E203), and heavy metals ≤10 ppm as lead by ICP‑MS (USP ⟨231⟩ / EPA Method 6020B). The lyophilized powder is stored under dry argon at −20 °C in septum-sealed amber vials; once opened, the material must be equilibrated to ambient temperature inside a glovebox maintained at ≤5 % RH to prevent premature hydrolysis of the activated ester. Solubility in deionized water at 25 °C exceeds 50 mg mL⁻¹, yielding a solution pH of 5.0–7.0 at 1 wt%.

    Why Does Protection of the Succinimidyl Ester Dictate Aqueous Polymerization pH Windows?

    The NHS ester hydrolyzes with half-lives on the order of minutes to hours depending on pH and temperature. At 25 °C in 0.1 M phosphate buffer, the pseudo-first-order hydrolysis rate constant (kobs) for the analogous non-sulfonated N-succinimidyl methacrylate has been reported as 2.3 × 10⁻⁴ s⁻¹ at pH 7.4, rising to 1.1 × 10⁻³ s⁻¹ at pH 8.0. The presence of the electron-withdrawing sulfonate group at the 3-position of the succinimide ring further polarizes the ester carbonyl, rendering the leaving group a stronger conjugate acid and accelerating hydrolysis relative to the unsubstituted NHS ester. Therefore, any aqueous radical polymerization intended to preserve pendant NHS functionality must be conducted at a pH ≤6.0. A 50 mM acetate buffer (pH 5.5) with 0.15 M NaCl has proven adequate for maintaining >85% ester integrity after 4 h at 25 °C when the monomer concentration is 5 wt%. In contrast, attempts to copolymerize at pH 7.0 result in loss of >50% of the NHS groups within 30 min as determined by the decrease in absorbance at 260 nm (characteristic of the N-hydroxysuccinimide leaving group). The requisite low-pH polymerization window must be reconciled with the redox initiation system; ammonium persulfate (APS) and N,N,N′,N′-tetramethylethylenediamine (TEMED) are effective at pH 5.5, but the initiation rate is 30–40% lower than at neutral pH, necessitating a 1.5‑fold increase in APS concentration to 0.75 mM to achieve gelation within 15 min. When using conventional N-succinimidyl methacrylate (water-insoluble, requiring 10–20 vol% DMF or DMSO), the organic co-solvent suppresses hydrolysis but introduces protein denaturation risks for subsequent bioconjugation. The sodium sulfonate substituent eliminates co-solvent demand, enabling fully aqueous protocols.

    When Crosslinking Density Demands Exceed Simple Copolymerization: Leveraging Dual Reactivity in Interpenetrating Networks

    The monomer functions as a heterobifunctional building block: the methacrylate group participates in chain-growth polymerization, while the NHS ester permits post-polymerization conjugation with primary amines (e.g., lysine residues, ethylenediamine). In a representative hydrogel formulation, 10 wt% acrylamide and 2.5 mol% N,N′-methylenebisacrylamide (MBA) were copolymerized with 1.0 mol% of the sulfonated NHS methacrylate monomer in acetate buffer (pH 5.5) using 0.5 mM APS/0.25 mM TEMED at 25 °C. After 60 min, the resulting gel was equilibrated in 0.1 M sodium bicarbonate (pH 8.3) and immersed in a 0.5 wt% ethylenediamine solution for 2 h. Oscillatory shear rheometry (parallel-plate, 1 Hz, 1% strain) recorded storage modulus G′ values pre- and post-amine treatment. G′ increased from 2.1 ± 0.3 kPa to 14.6 ± 0.8 kPa, consistent with a 6‑fold enhancement in effective crosslink density calculated from the Flory-Rehner equation using the phantom network model. The orthogonal crosslinking scheme avoids the kinetic competition inherent in simultaneous free-radical polymerization and amine‑NHS addition, a limitation observed when the non-sulfonated analogue is used because of poor water compatibility and phase separation. Incompatibilities must be observed: the monomer must not be combined with amine-bearing buffers (Tris, glycine) during polymerization or storage. Even trace ammonia in ammonium persulfate stocks can trigger premature crosslinking; freshly sublimed APS with an ammonia content <50 ppm is recommended.

    Copolymerization Reactivity Ratios and Retained NHS Functionality: A Continuous-Flow Synthesis Parameter Set

    A deep-dive into copolymerization behaviour is warranted because small shifts in monomer feed ratio alter both the density of reactive esters along the backbone and the sequence distribution, which directly impacts subsequent bulk conjugation efficiency. For the non-sulfonated N-succinimidyl methacrylate (NHSMA) with acrylamide in DMF at 60 °C, reactivity ratios of rNHSMA = 0.73 and rAAm = 1.18 have been documented (J. Polym. Sci. A Polym. Chem. 1997, 35, 2427). The sulfonated variant, bearing a permanent negative charge, exhibits a markedly different reactivity profile in aqueous media. Although published values for the exact monomer are limited, batch copolymerization in water at 25 °C initiated by APS/TEMED (0.75 mM/0.38 mM) at pH 5.5 indicates that at feed ratios of 5–10 mol% sulfonated monomer, high conversion (>90%) is reached within 20 min with NHS retention of 88 ± 4% as determined by UV quantification of liberated N-hydroxysulfosuccinimide after base hydrolysis. Production-scale continuous flow has been implemented on a pilot line employing a 1/4″ OD PTFE tubular reactor with a static mixing element (Kenics-type, 12 elements, L/D = 1.5) thermostatted at 20 °C. The aqueous monomer stream (15 wt% total monomer, pH 5.5) is combined in-line with a separately tempered initiator solution to achieve a residence time of 8 min at a flow rate of 15 mL min⁻¹. Under these conditions, conversion reaches 92–95% with a polydispersity index of 2.4. Exotherms must not exceed 35 °C; a recirculating chiller combating a thermal load of approximately 120 W m⁻¹ of reactor length is required. Premature crosslinking or microgel formation is suppressed by incorporating 50 ppm of 4-methoxyphenol (MEHQ) in the monomer feed and sparging with nitrogen to maintain dissolved oxygen below 0.5 mg L⁻¹ (measured with an optical probe per ISO 5814). The viscosity of the reaction mixture at the outlet is 12–15 mPa·s (Brookfield LV, spindle #1, 60 rpm), a manageable range for subsequent tangential flow filtration steps. Compared to 2-acrylamido-2-methylpropanesulfonic acid (AMPS), which introduces sulfonate charge without a post-modifiable handle, the dually reactive monomer provides an amine-coupling site. Compared to glycidyl methacrylate (GMA), which demands 60–80 °C and a prolonged ring-opening step for amine attachment, the NHS ester reacts at 4–25 °C, preserving thermally labile biomolecules.
    Comparison of Amine-Reactive and Sulfonate Monomers (Aqueous Conditions, pH 7.4 at 25 °C, unless noted)
    PropertySodium 1-(Methacryloyloxy)-2,5-Dioxopyrrolidine-3-SulfonateN-Succinimidyl Methacrylate (NHSMA)2-Acrylamido-2-methylpropanesulfonic acid (AMPS)Glycidyl Methacrylate (GMA)
    Water solubility (g L⁻¹)>50< 0.5>200< 10
    Amine-reactive half-life (h)0.8–1.21.5–2.0Not applicable4–6 (requires pH >9, 60 °C)
    Radical reactivity ratio with acrylamide (r₁/r₂)Approx 0.8–1.1 / 1.00.73 / 1.18 (in DMF)0.95 / 1.051.1 / 0.9
    Protein-friendly conjugation buffer50 mM HEPES, pH 7.0–7.5, no co-solventRequires 10% DMFNo coupling site0.2 M carbonate, pH 9.5, 37 °C
    Regulatory registration threshold (REACH, t/yr)1–10 (phase-in substance)1–10>1,000 (registered)100–1,000
    In polymer-supported bioconjugate workflows, the sulfonated NHS monomer allows direct coupling in 10 mM PBS (pH 7.2) without protein precipitation, a constraint observed with NHSMA formulations where DMF exceeds 5% v/v. Lysine-NHS coupling efficiency measured by fluorescamine assay following a 2 h incubation reaches 65–75% on hydrazine-fuctionalized surfaces, whereas GMA-modified surfaces require overnight incubation at 37 °C to achieve 40% coupling under identical protein loading. The permanent anionic charge also reduces nonspecific protein adsorption by a factor of 3–4 as quantified by SPR (Biacore T200, CMS chip, BSA at 1 mg mL⁻¹) compared to neutral NHS-containing films. In nonwoven membrane coating applications, the dual reactive monomer is deposited from a 2 wt% aqueous solution containing 0.1 wt% photoinitiator (Irgacure 2959) and cured under UV-A (365 nm, 50 mW cm⁻²) in a nitrogen-blanketed conveyor system. Residual NHS ester post-cure, determined by AT-IR peak intensity at 1735 cm⁻¹ relative to an internal sulfonate band at 1040 cm⁻¹, remains 92% of its pre-cure value, enabling downstream amine functionalization with oligonucleotides. This contrasts with epoxy-based coatings, where secondary ring-opening under ambient humidity reduces effective epoxy titer by 10–15% within 24 h.

    When the Monomer Is Introduced into Latex Particle Synthesis: Sulfonate Surface Charge versus Buried Ester Accessibility

    Seeded emulsion polymerization in the presence of the sulfonated NHS monomer at a 2 wt% charge relative to the core monomer (styrene/n-butyl acrylate, 1:1) using sodium dodecyl sulfate (2 g L⁻¹) and APS (0.5 wt% based on monomer) at pH 4.5 yields particles with z-average diameter 78 ± 5 nm and a narrow PDI (0.05) after 3 h at 70 °C. Because the sulfonate group preferentially orients toward the aqueous phase, approximately 40% of the NHS ester groups reside in the particle interior as determined by a dual-labelling strategy with a membrane-impermeable fluorescent diamine and a lipophilic analogue. Consequently, when the target biomolecule exceeds 5 kDa, surface-accessible NHS groups alone govern coupling yield, and the effective conjugation capacity is 60% lower than predicted from bulk monomer incorporation. This spatial distribution is reversed if the monomer is used in a soap-free precipitation polymerization, where copolymerization with methacrylic acid yields surface-enriched ester groups. The monomer must never be dried in a convection oven at temperatures above 30 °C because solid-state NHS rearrangement can generate unreactive isomeric species. Lyophilization in a shelf freeze-dryer with a condenser temperature of −85 °C and a final chamber pressure of 0.05 mbar is the preferred isolation method for laboratory quantities.