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1-(3'-Sulfophenyl)-3-methyl-5-pyrazolone(3-SPMP)

    • Product Name: 1-(3'-Sulfophenyl)-3-methyl-5-pyrazolone(3-SPMP)
    • Factroy Site: Dongjiakou Economic Zone, West Coast New Area, Qingdao
    • Price Inquiry: sales2@boxa-chem.com
    • Manufacturer: Qingdao Haiwan Chemical Co.,ltd
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    Specifications
    HS Code 559650
    Product Name 1-(3'-Sulfophenyl)-3-methyl-5-pyrazolone (3-SPMP)
    Synonyms 3-Methyl-1-(3-sulfophenyl)-5-pyrazolone; 1-(3-Sulfophenyl)-3-methyl-5-pyrazolin-5-one
    Cas Number 119-29-9
    Molecular Formula C10H10N2O4S
    Molecular Weight 254.26 g/mol
    Physical Form Crystalline powder
    Colour White to pale yellow
    Odour Odorless or slight characteristic odour
    Melting Point >300 °C (decomposes)
    Water Solubility Soluble in water; readily soluble in hot water
    Solubility In Organic Solvents Slightly soluble in methanol and ethanol; insoluble in ether and benzene
    Assay Purity ≥98%
    Loss On Drying ≤0.5%

    As an accredited 1-(3'-Sulfophenyl)-3-methyl-5-pyrazolone(3-SPMP) factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Packaged in 25 kg polyethylene-lined fiber drums, sealed under dry conditions to maintain purity and prevent moisture absorption.
    Container Loading (20′ FCL) Load 20′ FCL with 1-(3′-Sulfophenyl)-3-methyl-5-pyrazolone (3-SPMP) in drums, palletized, secured, and ventilated for safe transport.
    Shipping 3-SPMP is typically shipped as a stable powder in sealed, moisture-proof containers at ambient temperature. It is generally not classified as hazardous for transport, though packaging should prevent dust release. Ensure dry storage upon receipt. For international shipments, confirm customs SDS and regulatory compliance.
    Storage Store 1-(3'-Sulfophenyl)-3-methyl-5-pyrazolone (3-SPMP) in a tightly sealed, light-resistant container in a cool, dry, well-ventilated area. Keep away from moisture, heat, and strong oxidizers. Ensure the container is securely closed after each use and protected from direct sunlight to maintain purity and stability.
    Shelf Life The shelf life of 1-(3'-Sulfophenyl)-3-methyl-5-pyrazolone (3-SPMP) is typically two years when stored unopened in a cool, dry, and dark environment.
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    Certification & Compliance
    More Introduction

    1-(3-Sulfophenyl)-3-methyl-5-pyrazolone, abbreviated 3-SPMP, is an arylpyrazolone coupling component supplied primarily as the sodium salt or as a filtered aqueous solution. Commercial designations include 3-SPMP sodium salt and 1-(3-sulfophenyl)-3-methylpyrazol-5-one. The free sulfonic acid corresponds to C10H10N2O4S and a relative molecular mass of 254.26 g mol−1; the anhydrous monosodium salt corresponds to C10H9N2NaO4S and a relative molecular mass of 276.24 g mol−1. Industrial use is concentrated in azo dye manufacture, where 3-SPMP is reacted with diazonium salts to form yellow to orange acid, milling, and leather dyes. The sulfophenyl group confers water solubility to the anionic chromophore and improves substantivity on polyamide and protein substrates. The product is supplied under technical-grade designations rather than a single pharmacopoeial monograph; CAS registry numbers for the free acid and sodium salt should be confirmed with the supplier because the 3-sulfophenyl isomer is frequently grouped within the generic arylpyrazolone family. Public supplier data for 3-SPMP are less complete than for the 4-sulfophenyl analogue, so incoming inspection is usually based on chromatographic purity, water content, isomeric profile, and solution clarity.

    What Limits Coupling Rate and Selectivity in Weakly Alkaline 3-SPMP Solutions?

    Industrial coupling with 3-SPMP is an electrophilic substitution at the C-4 position. The active coupling species is the 5-pyrazolone enolate, formed by deprotonation; its concentration is controlled by the pH of the coupling charge. Below pH 7.5, enolate formation is incomplete and coupling slows, while above pH 9.5 the diazonium salt is increasingly converted to the less-reactive anti-diazotate. Production batch records for pyrazolone coupling therefore hold the charge within a narrow window, typically pH 8.0–9.0, using a recirculating pH-stat loop with sodium bicarbonate or disodium hydrogen phosphate dosing. The jacket temperature is commonly held at 0–8 °C during diazonium addition because diazonium decomposition becomes significant above 10–15 °C. In a 2,000–5,000 L glass-lined reactor, the diazonium salt is usually fed over 60–120 min, making heat removal the principal throughput constraint. A bottom-runoff valve and a baffled agitator operating at 40–70 rpm are typical; higher tip speeds have been associated with foam and with increased dissolution of atmospheric oxygen, which promotes oxidative by-product formation.

    The reaction endpoint is verified by the disappearance of the diazonium absorption band near 450 nm; residual 3-SPMP is measured by reversed-phase HPLC with a C18 column and a phosphate-acetonitrile mobile phase. Common yield losses on production lines arise from nitrosation of the active methylene position by nitrous acid released during diazonium decomposition, from oxidative coupling by dissolved oxygen, and from precipitation of the dye at low temperature. To limit these losses, the 3-SPMP solution is sparged with nitrogen for 15–30 min before diazonium addition and the batch is blanketed with nitrogen during coupling. When dry powder is charged directly into an agitated vessel, local concentration differences can produce pH excursions; therefore, production sites predissolve the material in demineralised water at 10–20 °C before adjusting the coupling pH.

    On a production-scale dye finishing line, the resulting 3-SPMP-based monoazo dye is isolated by salt precipitation or membrane concentration and then dried in a spray dryer with a rotary atomiser. The 3-sulfophenyl group contributes to the anionic character of the dye and to its initial solubility; sodium chloride content after isolation is typically controlled because excess electrolyte reduces the solubility of the dye powder and can suppress exhaustion at the dyeing stage. Standardised washing fastness tests on wool are performed according to ISO 105-C10, but published fastness data for dyes derived specifically from 3-SPMP are limited; shade and wet-fastness comparisons between the 3- and 4-sulfophenyl isomers are usually generated as internal production qualification data rather than published reference datasets.

    Positional Isomer Effects in Sulfoaryl Pyrazolones

    Compared with 1-phenyl-3-methyl-5-pyrazolone, 3-SPMP is water-soluble at coupling pH and does not require solvent addition. The non-sulfonated analogue is usually dissolved in dilute sodium hydroxide or a water-miscible solvent such as methanol; the solvent must be removed or accounted for before coupling, and residual solvent can destabilise the diazonium salt. Compared with 1-(4-sulfophenyl)-3-methyl-5-pyrazolone, 3-SPMP places the sulfonate group at the meta position of the N-phenyl ring. The electronic effect of the meta-sulfonate is primarily inductive, whereas the para-sulfonate can also participate in resonance with the pyrazolone nitrogen. This changes the enolate electron density at C-4 and the aqueous pKa of the pyrazolone, shifting the optimum coupling pH and the ratio of keto to enol tautomers. The steric effect is minimal, but traces of the 4-isomer are relevant because they alter the apparent coupling pH and dye shade. Published kinetic constants for 3-SPMP are limited; process development therefore relies on factorial response-surface experiments that measure dye yield, residual coupler, and residual diazonium salt.

    The single largest difference between 3-SPMP and 4-SPMP is usually observed in shade reproducibility when the isomer ratio is not controlled. A residual 4-isomer content above 0.5 % is often specified in vendor agreements because the two isomers couple at slightly different rates and produce dyes with different aggregation behaviour in concentrated solution. The 3-isomer also tends to remain in solution at higher dye concentration, which can reduce filter blinding during isolation but can increase the drying load on the spray dryer. These effects are not absolute; they depend on the diazonium component, the dye molecular weight, and the final salt content.

    Process routes to 3-SPMP typically involve condensation of 3-sulfophenylhydrazine with ethyl acetoacetate or methyl acetoacetate in aqueous alkaline solution. The intermediate hydrazone is then cyclised to the pyrazolone ring. Industrial isolation is performed by pH adjustment and crystallisation or by spray drying. Because the sulfonic acid group remains ionised over a wide pH range, the product is usually obtained as a sodium salt; free acid forms are less common and are more hygroscopic.

    When 3-SPMP Replaces 4-SPMP in Low-Salt Dye Formulations

    When a manufacturing site replaces 1-(4-sulfophenyl)-3-methyl-5-pyrazolone with 3-SPMP in an existing azo coupling recipe, the first adjustment is usually the pH set point. Because the meta-sulfophenyl isomer can couple at a slightly different optimum pH, the existing bicarbonate feed profile may produce a higher residual coupler at the same reaction time. Process records from batch campaigns indicate that the coupling endpoint should be revalidated by HPLC rather than by visual starch-iodide paper alone; starch-iodide paper detects the diazonium salt but not the residual 3-SPMP. The second adjustment is the precipitation salt profile: 3-SPMP-derived dyes can remain more soluble in the clarified mother liquor, so the sodium chloride addition required for precipitation may increase by 5–10 % relative to the 4-isomer for the same dye molecular weight. This shift has not been uniformly reported across all dye families and should be measured on the specific recipe.

    In dyeing application, 3-SPMP-based acid dyes are used for polyamide and wool. The water solubility contributed by the sulfophenyl group supports dyebath preparation at 80–98 °C in exhaust dyeing equipment, but the 3-isomer can produce slightly higher migration and lower wet-fastness under hot-pressing conditions when compared with a para-sulfonated analogue. Published quantitative fastness data for this narrow isomer pair are limited; dye mills commonly run comparative trials on a laboratory drum dyeing machine with a liquor ratio of 1:10 to 1:20 against the existing 4-isomer product before changing the raw material specification.

    Which Test Methods Are Useful for Vendor Qualification?

    Because 3-SPMP is not a compendial substance, vendor qualification depends on a defined incoming inspection plan. The following acceptance profile is representative of a technical-grade sodium salt used in dye synthesis. Values are not regulatory limits; they are derived from supplier technical datasheets and internal quality agreements. Users should confirm whether the material is the anhydrous sodium salt, a hydrate, or the free sulfonic acid before applying water-content and purity limits.

    Typical vendor qualification profile for 3-SPMP sodium salt
    ParameterTypical acceptance criterionTest method
    HPLC purity, area-normalised≥99.0 %In-house UPLC method, UV detection at 254 nm, calibration per ISO 17025
    Water content≤0.5 %ISO 760
    pH of 10 g/L aqueous solution6.0–8.0ISO 10523
    Insoluble matter in water≤0.1 %Gravimetric, 0.45 μm membrane filtration
    Residual 4-sulfophenyl isomer≤0.5 %HPLC peak-area ratio
    Total chlorine≤0.05 %Combustion ion chromatography

    Storage conditions are typically dry and cool, with sealed polyethylene-lined fibre drums or stainless steel totes. At relative humidity above 60 %, the powder takes up water and may cake; pre-drying in a vacuum tray dryer at 40–50 °C for 8–12 h is used when the water content exceeds the specification. The material should not be mixed with strong oxidising agents, nitrosating agents, or concentrated mineral acids outside controlled coupling or isolation steps. Waste streams containing 3-SPMP should be segregated from acidic nitrite-containing effluents because the combination may generate volatile nitrogen oxides; neutralisation and controlled oxidation are typically applied before discharge under local permits.