Nanjing Color Science Co.,Ltd
Section

Products

Solvent Yellow 2

    • Product Name: Solvent Yellow 2
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: sales3@liwei-chem.com
    • Manufacturer: Nanjing Color Science Co.,Ltd
    • CONTACT NOW
    VTB
    Specifications
    HS Code 629049
    Product Name Solvent Yellow 2
    C I Number 11020
    Cas Registry Number 60-11-7
    Ec Number 200-455-7
    Molecular Formula C14H15N3
    Molecular Weight 225.29 g/mol
    Chemical Class Monoazo dye
    Appearance Yellow to orange crystalline powder
    Melting Point 114-117 °C
    Boiling Point 371.4 °C
    Density 1.05 g/cm³
    Water Solubility Insoluble
    Organic Solubility Soluble in ethanol, ether, chloroform, benzene, and oils
    Ph Indicator Range pH 2.9-4.0, red to yellow
    Absorption Maximum 408 nm
    Synonyms Butter Yellow; Dimethyl Yellow; p-Dimethylaminoazobenzene; N,N-Dimethyl-4-phenylazoaniline

    As an accredited Solvent Yellow 2 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Solvent Yellow 2 is packaged in a 25 kg securely sealed, labeled industrial drum for safe handling and transport.
    Container Loading (20′ FCL) A 20-foot FCL container is loaded with Solvent Yellow 2 chemical cargo, securely packed, labeled, and prepared for international transport.
    Shipping Solvent Yellow 2 is generally not UN-classified for transport; ship as non-dangerous goods in sealed, labeled containers. Protect from light, heat, and moisture; avoid dust generation. Follow local carcinogen-handling, environmental, and import regulations, as special requirements may apply.
    Storage Store Solvent Yellow 2 in a cool, dry, well-ventilated, locked area away from direct sunlight, heat, sparks, and open flames. Keep containers tightly closed, clearly labeled, and protected from moisture. Segregate from strong oxidizers, acids, and food, drink, or animal feed. Use secondary containment, avoid dust generation, and follow local hazardous-chemical storage regulations.
    Shelf Life Stable under recommended storage conditions; protect from light, heat, and moisture. Shelf life is not established; use within manufacturer’s specified period.
    Application of Solvent Yellow 2

    Pre-dissolved marker concentrates for middle distillates are prepared by dissolving Solvent Yellow 2 in xylene or heavy aromatic naphtha at 40–50 °C under low-shear agitation. The dye is a water-insoluble monoazo compound with a melting point of 114–117 °C and a molecular weight of 225.29 g/mol; water entrainment into the carrier must be limited because phase splitting causes dye precipitation and potential filter plugging. Concentrate loading is held below the crystallisation threshold for the chosen aromatic stream; industrial masterbatches commonly use 1.0–5.0 wt% dye, and stored solutions require protection when ambient storage drops below 15 °C. In-line dosing into finished distillate uses positive-displacement metering pumps with stainless steel liquid ends and static mixers placed downstream of the injection point. The final marker concentration is set by local excise protocols and generally sits in the low ppm range; no universal single-dose value applies. Homogeneity after injection is confirmed by ASTM D1500 colour measurement or by HPLC-DAD at 410 nm against certified marker standard solutions. Kinematic viscosity is checked by ASTM D445, and cloud point is checked by ASTM D2500 to ensure the marker does not alter product specification. The primary skid-level failure mode is filter clogging when powdered dye is fed directly into low-aromatic paraffinic stocks; a pre-dissolved aromatic masterbatch avoids this bottleneck. Paraffinic carriers with very low aromatic content show reduced dye solubility and require higher dissolution temperatures or a suitable co-solvent; published data for this specific configuration is limited. Solvent Yellow 2 does not contribute lubricity, combustion stability, or oxidation resistance; it is present solely as a fiscal marker. Phase stability should be checked if oxygenated co-solvents are present in the finished petroleum stream because co-solvent addition can reduce dye solubility in the hydrocarbon phase.

    Why Lubricating Grease Colour Coding Requires Pre-Wetted Dye Addition at the Letdown Stage

    In lithium and calcium soap greases, dry Solvent Yellow 2 powder is not added directly into the thickener during saponification because dust generation and local dye concentration produce colour streaks in the finished product. A low-dusting pre-wetted concentrate is prepared in refined mineral oil at 60–80 °C and metered into the finished product after saponification and dehydration. Letdown temperature is held between 100 °C and 120 °C; below this band, reduced oil-phase solubility creates visible striations in the translucent thickener matrix. Above 130 °C, oil separation can increase in some lithium 12-hydroxystearate greases, altering the apparent surface colour and complicating visual grading. Scraped-wall kettles and recirculating shear mixers running at low tip speeds are typical; high-shear rotor-stator devices are not necessary because the dye is dissolved rather than dispersed as a pigment. Final dye level is adjusted by spectrophotometric comparison against a stored reference plaque; precise levels vary with grease transparency, thickener fibre morphology, and oil polarity, and published data for this specific configuration is limited. Worked penetration is controlled by ASTM D217, and oil separation is monitored by ASTM D1742 where applicable. Colour stability under storage is assessed by diffuse reflectance spectrophotometry using CIE L*a*b* geometry; a batch acceptance tolerance of ΔE*ab ≤ 1.0 is applied at final release. Extreme-pressure additive packages should be validated for dye solubility because highly solvating additive oils can produce localised dye depletion during milling or degassing. Solvent Yellow 2 is not a boundary lubricity additive and must not be used as a substitute for grease performance additives. The dry powder should also be isolated from oxidising agents because the monoazo chromophore is oxidatively sensitive at elevated temperature.

    Because the dye melting point of 114–117 °C exceeds the usual paraffin wax melt temperature of 65–90 °C, paraffin wax masterbatch operations use a two-stage sequence. In the first stage, a dye concentrate is prepared in microcrystalline wax at 120–125 °C under high-shear dispersion. The process band is narrow: lower temperatures allow undissolved dye particles to survive, while higher temperatures accelerate thermal darkening in unpurified wax fractions. The concentrate is let down into finished paraffin wax at a typical final dye content below 0.05 wt%; solubility varies with wax oil content and microcrystalline fraction. High-shear dispersion is maintained by a rotor-stator mixer or a recirculation loop through a homogenizing valve. Finished batches are checked for melting point by ASTM D87, congealing point by ASTM D938, and oil content by ASTM D721. Batch-to-batch variance in wax oil content is a major source of colour variation because higher oil content increases dye solubility and reduces bloom tendency. Blooming on candle surfaces is the primary field defect, occurring when the dye addition exceeds the solubility limit in low-oil-content paraffin or when cooling is uncontrolled. Packaging films exposed to bloomed candles show yellow transfer that cannot be removed by ordinary handling. Production lines mitigate blooming by adding a microcrystalline wax fraction of 5–15 wt% to raise oil retention. Final colour is measured on cooled candle cross-sections using a spectrocolorimeter under D65 illumination with 10° observer geometry. If high-speed mould release agents contain polar additives, phase partitioning should be re-checked because surfactant-like release agents can extract dye to the surface. Opaque candle blends containing titanium dioxide require higher dye loadings for an equivalent visual depth, but colour strength cannot be inferred from transparent drawdowns alone.

    Spirit-Based Wood Stain Colour Control with Nitrocellulose Lacquer Diluents

    Nitrocellulose lacquer and spirit-stain systems require Solvent Yellow 2 to be predissolved in a true solvent before film-forming polymers are introduced. The working solution is prepared in ethyl acetate, n-butanol, or 95% ethanol at 30–40 °C. The solution is filtered through a 10–25 μm cartridge before letdown to remove undissolved dye agglomerates. Final dye level in a lacquer base is commonly 50–200 ppm on total solids, adjusted to the required amber depth. Water addition must be limited because the dye is water-insoluble and will precipitate as fine particles when the polar solvent balance drops below the solubility threshold. Acid-catalysed wood coatings must be excluded: the indicator transition of Solvent Yellow 2 occurs between pH 2.9 and 4.0, and acid-rich nitrocellulose from residual cotton linters can shift the shade from yellow to red at the film interface. Washing of lacquer-grade nitrocellulose to neutral pH is a prerequisite for stable colour. The finished stain is inspected by drawdown over white-pine substrate and measured with a spectrophotometer using CIE L*a*b* geometry under D65/10°. Solvent resistance after cure is assessed by ASTM D5402, and adhesion is assessed by ASTM D3359. Finished wood stains are subject to EU Directive 2004/42/EC VOC content limits by category. Solvent Yellow 2 does not contribute to pigment volume concentration because it is a dye; gloss remains a function of nitrocellulose solids and plasticiser content. Reformulators should not use acid-functional adhesion promoters below pH 4.0 in the same formulation without separate stability validation. Dye migration from the cured lacquer into adjacent plastic or sealant surfaces should be tested where the coated wood component is assembled into multi-material articles.

    For oil-based letterpress and screen ink systems, Solvent Yellow 2 functions as a shading dye rather than as a primary pigment. The dye is dissolved in a high-boiling mineral oil or linseed oil vehicle at 1–5 wt% before addition to the finished ink. The mix is passed through a three-roll mill or bead mill primarily to disperse the hydrocarbon resin and pigment phase, not to grind the dye. Shade control is achieved by gravimetric letdown into a base ink, with drawdowns on coated paper measured under ISO 13655-compliant geometry. Blocking resistance and rub-off are assessed by standard print trial protocols; published data for Solvent Yellow 2 in this specific ink formulation is limited. The finished ink is subject to VOC limits under applicable national printing-ink regulations; the dye itself is a low-volatility solid but must be counted in the total volatile fraction if dissolved in VOC solvents. Solvent Yellow 2 should not be used in low-migration food-contact inks unless printing is separated by a functional barrier and compliance is proven under the applicable food-contact regulation. Oxidative linseed-oil systems should be checked for vehicle yellowing because film yellowing can interfere with colour-stability assessments even when the dye itself remains soluble.

    When Rust Preventive Oil Coverage Requires Visible Colour Tracking Without Distorting ASTM D665 Results

    Temporary rust preventive oils use low additions of Solvent Yellow 2 to provide visible confirmation of coverage after dip or spray application. A concentrated masterbatch is prepared in naphthenic base oil at 1–5 wt% at 50–70 °C and dosed into the finished rust preventive at 0.01–0.1 wt%. The dye does not contribute corrosion protection; performance must be validated separately by ASTM D665 for oil-phase protection and by ASTM B117 for salt-spray resistance on coated steel panels. High-polarity rust preventive additives can reduce dye solubility, causing precipitation on cold surfaces below 10 °C. Storage tanks should be agitated by slow recirculation, not air bubbling, because oxidative generation of organic acids in the headspace can shift the dye shade through the indicator transition range. Coverage tracing is inspected under controlled white light, and final film colour is measured by drawing a calibrated film on white steel panels and measuring reflectance with a spectrophotometer. The maximum tinting strength is kept below the threshold that leaves visible surface staining on packaged parts after the rust preventive is stripped. If an alkaline aqueous degreasing step is used, cleanability is assessed by the end user with a standard degreasing panel test; Solvent Yellow 2 is carried with the oil phase and does not intentionally remain on clean steel. This application is incompatible with water-displacing fluids that contain large polar co-solvent fractions unless cloud-point stability is confirmed at the lowest storage temperature. Solvent Yellow 2 should not be used in rust preventives intended for electrical contacts or sensitive alloys if dye retention on metal is unacceptable.

    Downstream systemVehicle/solvent systemCritical processing boundaryPrimary test methods
    Middle distillate tax markerXylene/heavy aromatic naphthaWater ingress limited; low ppm fuel dosageASTM D1500, ASTM D445, ASTM D2500
    Lithium/calcium grease colour codingRefined mineral oil pre-wetLetdown 100–120 °C; no dry powder in saponificationASTM D217, ASTM D1742, diffuse reflectance spectrophotometry
    Paraffin wax masterbatchMicrocrystalline wax concentrateSetpoint 120–125 °C with ±5 °C controlASTM D87, ASTM D938, ASTM D721
    Nitrocellulose wood stainEthyl acetate/n-butanol/ethanolpH > 4.0; limited waterASTM D5402, ASTM D3359
    Oil-based letterpress/screen inkMineral oil/linseed oilDye as solution, not pigment dispersionISO 13655, national VOC printing-ink rules
    Rust preventive oilNaphthenic base oilCold storage > 10 °C; no air bubblingASTM D665, ASTM B117
    Compliance domainBoundary/exclusionReference
    EU food-contact plasticsNot listed in EU 10/2011/EC Annex I; direct food-contact use is excluded unless separately authorisedEU 10/2011/EC
    FDA 21 CFRNo direct food-contact clearance asserted; finished article must be evaluated under applicable FDA food additive regulations21 CFR Chapter I
    REACHFormulator must verify registration status for the relevant tonnage band and communicate identified uses in the exposure scenarioREACH (EC) No 1907/2006
    VOC in decorative wood stainsSolvent carriers in decorative coatings and wood stains are subject to category-specific volatile organic compound limitsEU Directive 2004/42/EC
    Fuel marker protocolsDosing and detection limits are jurisdiction-specific; no single harmonised fuel marker standard applies globallyNational excise and fiscal-monitoring rules
    Free Quote

    Competitive Solvent Yellow 2 prices that fit your budget—flexible terms and customized quotes for every order.

    For samples, pricing, or more information, please contact us at +8615365186327 or mail to sales3@liwei-chem.com.

    We will respond to you as soon as possible.

    Tel: +8615365186327

    Email: sales3@liwei-chem.com

    Inquiry

    Get Free Quote of Nanjing Color Science Co.,Ltd

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

    Certification & Compliance
    More Introduction

    Solvent Yellow 2, designated C.I. 11020 and CAS 1689-82-3, is the para-hydroxy derivative of azobenzene, 4-(phenylazo)phenol, with molecular formula C12H10N2O and molecular mass 198.22 g/mol. EINECS reference is 216-880-6. The material is supplied as a yellow-to-orange crystalline powder or as a wetted presscake; commercial dry-powder and low-dusting granular forms differ in residual moisture, particle-size distribution, and packaging, not in chromophore identity. As a monoazo colorant without sulfonic acid groups, the product is intended for nonpolar and solvent-based matrices such as hydrocarbon oils, waxes, oleoresins, solvent-borne wood stains, marking inks, and selected thermoplastic masterbatches where a green-shade yellow is required and aqueous solubility must remain negligible.

    Two broad supply forms are specified in procurement: general industrial grade and high-purity marker grade. General industrial grade is typically sold on HPLC assay and melting range; high-purity marker grade adds a GC-amenable impurity profile, residual phenol value, and residual aniline value. The substitution of general industrial grade into fuel marker duty is not appropriate without certified impurity data, because residual aniline and phenol can affect extractability and regulatory compliance. Batch-to-batch variance in residual phenol is reduced by washing the isolated presscake with dilute alkali or water; insufficient washing contributes to plasticizer-like bloom in polyolefin film applications.

    What Physical Constants Support Receiving Inspection?

    The batch acceptance protocol for Solvent Yellow 2 should include identity confirmation by infrared spectroscopy or retention-time matching against a certified reference standard, assay by reversed-phase HPLC with area normalization, and melting range determination. The melting interval generally falls at 152–155 °C when measured by capillary method; differential scanning calorimetry under nitrogen at 10 K/min may show the endothermic onset between 150 °C and 154 °C. In ethanol, the long-wavelength absorption maximum is reported near 347 nm; the value shifts with solvent polarity and pH. The molecular mass of 198.22 g/mol and the absence of sulfonic acid groups distinguish Solvent Yellow 2 from water-soluble acid dyes. Water solubility is negligible; solubility in ethanol, toluene, ethyl acetate, and ketones is sufficient for solvent-borne wood stains and hydrocarbon markers. A procurement specification should require a minimum assay of 98.0% by reversed-phase HPLC area normalization and a water content not exceeding 0.5% by Karl Fischer titration. Residual free aniline and phenol are determined by gas chromatography with flame ionization detection or liquid chromatography-mass spectrometry after solvent extraction. The user should specify the limit for each impurity according to the end-use regulation; no universal limit exists across fuel, coatings, and plastic applications.

    Unlike water-soluble acid dyes of similar shade, Solvent Yellow 2 remains in the nonpolar phase during solvent extraction; this behavior is exploited in two-phase marker systems where the aqueous phase must remain clear. The absence of sulfonic acid groups also eliminates strong ionic interactions that complicate filtration in solvent inks and reduces electrical conductivity in hydrocarbon fluids. Compared with organic pigments in the same shade range, the dye dissolves at the molecular level and does not contribute to hiding power or thixotropy; therefore, it is unsuitable where opacity or pigmentary rub resistance is required. In transparent polystyrene and poly(methyl methacrylate) applications, the molecular dye provides high clarity at loadings below 0.5 wt%, but migration in soft PVC and low-density polyethylene is more pronounced than with higher-molecular-weight solvent dyes.

    In solvent systems, the dye is usually introduced as a pre-dissolved concentrate rather than as dry powder. In toluene at 25 °C, Solvent Yellow 2 dissolves readily at 10–15 wt% under moderate agitation; in ethanol, solubility is lower, and the dyestuff may require pre-warming to 40 °C. For oleoresin and wax applications, the dye is added to the molten wax at 80–100 °C, avoiding undissolved particles in the final congealed product. High-shear dispersion is not required for wax dyeing; a side-sweep agitated vessel prevents settling during heat-up. Because the molecule contains a phenolic hydroxy group, prolonged storage in ketonic solvents can lead to darkening via oxidation. In some industrial concentrates, a hindered phenol antioxidant is added at 0.1–0.2 wt% of solution mass where solvent stability is required.

    Fuel marker concentrates and middle-distillate additive packages are prepared by pre-dissolving Solvent Yellow 2 in an aromatic hydrocarbon solvent, typically xylene or high-boiling naphtha, at 20–30 wt% active dye under high-shear mixing at 40–60 °C. Injection of the concentrated dye solution is accomplished with a diaphragm metering pump or a mass flow-controlled gear pump; static mixers downstream of the injection point are recommended to avoid localized dye concentration. The final dosage is metered into fuel at parts-per-million levels and is governed by fiscal marker regulations rather than by the saturation limit of the dye. Because the dye contains no sulfonate groups, it does not partition into the aqueous phase under normal fuel-water contact. Contact with strongly alkaline water above pH 8.0 should nevertheless be avoided; deprotonation of the para-hydroxy group increases water extractability and alters visible hue. Quantitative release testing is performed by HPLC with diode-array detection; visible appearance in finished fuel can be compared with the ASTM D1500 color scale, although that method is not designed for marker confirmation.

    Differences in Chromophore Structure and Processing Behaviour Relative to Selected Solvent Yellows

    Solvent Yellow 2 differs from other monoazo solvent dyes in its para-hydroxy substitution and limited conjugation. Replacement of the para-hydroxy benzene ring with a naphthalene ring, as in Solvent Yellow 14, increases molecular mass and shifts hue bathochromically. Replacement of the hydroxy group with an amino group, as in Solvent Yellow 3, introduces basic character and lowers the melting point. These differences affect processing temperatures, solvent selection, and pH sensitivity. Comparative data are summarized in Table 1.

    PropertySolvent Yellow 2Solvent Yellow 14Solvent Yellow 3
    C.I. number110201205511160
    CAS RN1689-82-3842-07-997-56-3
    Structural classpara-hydroxyazobenzene1-phenylazo-2-naphthol2-methyl-4-[(2-methylphenyl)diazenyl]aniline
    Molecular formulaC12H10N2OC16H12N2OC14H15N3
    Molecular mass198.22 g/mol248.28 g/mol225.29 g/mol
    Melting range152–155 °C131–133 °C102–104 °C

    The para-hydroxy group of Solvent Yellow 2 confers weak acid character and pH-dependent hue; the naphthol group of Solvent Yellow 14 also confers weak acid character but with additional aromatic conjugation. The amino group of Solvent Yellow 3 imparts basic character and can form salts with acids, which modifies solvent extraction behavior. These structural differences mean Solvent Yellow 2 is specified where a lower molecular mass and higher melting point reduce caking in dry-powder storage, but the same para-hydroxy group makes it more sensitive to alkaline aqueous contact than the amino-substituted analogue.

    In aqueous solvent extraction, the partition coefficient depends on pH. At neutral and acidic pH, the undissociated phenol form dominates and the dye remains in the organic layer. Above the pKa of the phenolic group, the phenolate form increases water solubility and can produce an orange-red shift in aqueous extracts. This behavior is characteristic of para-hydroxyazo compounds and is a key distinction from non-phenolic solvent yellows that lack an extractable acidic proton. For this reason, caustic washing of fuel or wax systems is not advised unless the aqueous phase is continuously separated and the pH is maintained below 8.0.

    When Solvent Yellow 2 Is Melt-Processed in Polyolefin and Styrenic Matrices

    Polyolefin masterbatch production using Solvent Yellow 2 is run on twin-screw extruders with L/D ratios between 32:1 and 44:1. The initial barrel zone is maintained below 150 °C to avoid premature melting of the dye, while downstream zones are set between 180 °C and 220 °C for polypropylene and polyethylene. The dye is introduced either as a powder via side feeder at 1–4 wt% active loading in the masterbatch or as a pre-dispersed single-pigment concentrate. Because the melting interval of Solvent Yellow 2 lies at 152–155 °C, the dye melts during compounding and reduces local melt viscosity; this behavior can create temporary lubrication but does not ensure dispersion unless distributive mixing is adequate. Plate-out on screw elements and die lips is encountered when processing at dye loadings above 4 wt% without vent vacuum or when the resin contains residual polymerization catalyst residues; published data for this specific configuration is limited, but periodic screw-pull inspection is recommended. Colorimetric evaluation of molded plaques can follow ASTM D6290-19 for pellet color and ASTM D2244-23 for color differences; yellowness index can be reported per ASTM E313-20 using D65 illuminant and 10° observer. The dye should be pre-qualified by thermogravimetric analysis under nitrogen before sustained processing above 260 °C is attempted.

    The azo linkage is the primary thermal and photochemical weakness. Under elevated temperatures or UV exposure, the carbon-nitrogen double bond can undergo homolytic cleavage, producing aryl radicals and leading to color fade and darkening. In polypropylene, the observed failure mode is a bathochromic shift and loss of green shade before complete color disappearance; this is consistent with chromophore decomposition rather than migration alone. Published quantitative activation energies for this dye in melt matrices are limited.

    Wood stains and solvent-borne varnishes are colored by dissolving Solvent Yellow 2 at 2–5 wt% in a premix of toluene, ethyl acetate, and ketone before addition to the final varnish base. High-speed dispersers with tip speeds of 10–15 m/s are adequate for dissolution; filtration through 10–25 µm bag filters removes undissolved agglomerates. The dye does not contribute to film hardness and should be omitted from exterior UV-exposed coatings unless a benzotriazole UV absorber and hindered amine light stabilizer package is used; even then, lightfastness of this monoazo dye is inferior to high-molecular-weight solvent dyes, and color retention is matrix-dependent. Accelerated weathering according to ISO 4892-2 may be used to compare color retention, but published fading data for this specific formulation is limited.

    Lubricant and process-oil tinting uses low concentrations between 50 mg/kg and 500 mg/kg; the dye is pre-dissolved in a process oil fraction before dosing into the finished lubricant. Batch tinting vessels equipped with circulation loops provide adequate mixing; in-line spectrophotometers can monitor color strength during dosing. Because the dye absorbs in the visible blue region, it masks pale yellow oxidation products in certain light-colored oils, but it does not alter lubricant viscosity or additive performance at these loadings. Pre-filtering the concentrate through 5–10 µm media is recommended to prevent agglomerate carryover.

    Avoid combination with strong oxidizing agents and hypochlorite-based sanitizing agents because the azo bond can be cleaved. In coatings, the dye is stable toward mild organic acids but should not be used in nitrocellulose lacquers containing residual sulfuric acid if long-term storage is required; acid-catalyzed degradation can cause hue drift. In fuel marker packages, the dye is compatible with aromatic solvent carriers and most phenolic antioxidants, but amine-based markers and additives may accelerate color changes under prolonged storage. Compatibility should be tested at 45 °C for 28 days in the final matrix rather than inferred from chemical class alone.

    Regulatory acceptance varies by end-use and region. For food-contact plastics, verification against EU Regulation No 10/2011 and FDA 21 CFR 178.3297 is required; C.I. Solvent Yellow 2 is not universally listed in regional positive lists and must not be assumed compliant. In industrial fuel marking, the dye may be subject to national excise-marker specifications that define minimum purity, extractability, and maximum levels of free aniline and phenol. Users should request a chromatographic impurity profile with residual aromatic amine and phenol concentrations below the limits specified in the applicable marker directive; published cross-jurisdictional limits for this specific dye are limited. Dry powder should be stored in sealed containers below 30 °C and below 60% relative humidity; caking occurs when moisture ingress exceeds the specification limit, and dried material may require re-milling before use. Avoid contact with strong reducing agents and strongly alkaline aqueous media, as azo reduction may liberate aniline and 4-aminophenol under extreme conditions.