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Brilliant Red BBC

    • Product Name: Brilliant Red BBC
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: sales3@liwei-chem.com
    • Manufacturer: Nanjing Color Science Co.,Ltd
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    VTB
    Specifications
    HS Code 133022
    Productname Brilliant Red BBC
    Synonym Direct Brilliant Red BBC
    Dyeclass Direct dye
    Colorindexname C.I. Direct Red 224
    Colorshade Brilliant red
    Physicalform Powder
    Watersolubility Soluble in water
    Ionicnature Anionic
    Mainsubstrates Cotton, viscose, paper, leather
    Applicationmethod Exhaust dyeing with electrolyte
    Typicalph Neutral to slightly alkaline
    Lightfastness Moderate
    Washfastness Moderate

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

    Packing & Storage
    Packing Brilliant Red BBC is supplied in 25 kg net-weight fiber drums with moisture-barrier liners and securely sealed lids.
    Container Loading (20′ FCL) Brilliant Red BBC is palletized, securely stowed, and moisture-protected inside a 20-foot FCL container for safe export shipment.
    Shipping Ship in accordance with the SDS and applicable transport regulations. Keep containers closed, labeled, upright, dry, and protected from heat, sunlight, and moisture. Avoid spills; use appropriate PPE and emergency procedures. If classified as hazardous, follow UN packing, marking, labeling, and documentation requirements.
    Storage Store in a cool, dry, well-ventilated area, away from oxidizers, acids, alkalis, direct sunlight, and ignition sources. Keep containers tightly closed, properly labeled, and protected from moisture and physical damage. Use secondary containment and separate from food, feed, and incompatible materials. Store only in original or compatible containers. Avoid dust generation and accumulation. Follow the manufacturer’s SDS and local regulations.
    Shelf Life The shelf life of Brilliant Red BBC is generally 24 months under recommended storage conditions; check manufacturer’s label for expiration.
    Application of Brilliant Red BBC

    In sheetfed offset lithography, Brilliant Red BBC is charged into a medium-oil alkyd vehicle after separate wetting of the pigment surface with a low-viscosity alkyd or mineral oil. The pigment is C.I. Pigment Red 48:2, a calcium lake of 4-[(5-chloro-4-methyl-2-sulfophenyl)azo]-3-hydroxy-2-naphthoic acid. That lake structure contributes high colour strength but also carries sulfonate groups that make water pickup a critical production variable. A typical sheetfed formulation carries the pigment at 14–18 wt%, while heatset formulations operate at 12–15 wt% to account for lower dry film thickness and higher press speed. Tack is measured on a falling-rod tackmeter in accordance with ISO 12644, and water pickup is evaluated by ASTM D4942. The production risk is excessive ink emulsification with the dampening solution: when water uptake rises above the press target, print density drops and dot gain increases. The pigment is pre-dispersed on a three-roll mill, typically at a first pass pressure of 0.2–0.4 MPa and a final pass at 0.8–1.2 MPa, but actual settings depend on vehicle viscosity and batch viscosity recovery. Plate blinding is uncommon if the free acid value of the alkyd vehicle remains controlled, because acid-catalysed ion exchange at the calcium lake surface can increase yield value and body. The processed ink is used in folding cartons, posters, magazine covers, and non-food commercial printing. For indirect food contact, migration testing under EU 10/2011 or FDA 21 CFR 175.300 is required; the pigment is not presumed compliant without a barrier layer. Published data for this specific trade name in low-migration sheetfed systems is limited, so qualification runs on the target press are required.

    How Does Melt Temperature Above 200°C Trigger Plate-Out in Rigid PVC Extrusion?

    Dry-blend letdown into rigid PVC requires heat history documentation because the calcium lake can release water of hydration and shift hue above a threshold. In a Brabender torque rheometer per ASTM D2538, melt temperature is kept at 180–200°C for pipe and profile compounds. The pigment is added at 0.5–1.5 phr on PVC resin in dry blends; for plasticized PVC film and leather cloth, the loading is reduced to 0.3–0.8 wt%. Dry pigment is pre-sieved through a 100 µm screen before dry blend mixing to reduce agglomerate carryover. Plate-out appears as a pink deposit on die lips and calibrator walls when pigment agglomerates are not dispersed in the primary melt, and the condition is aggravated by residence time above 200°C. Batch-to-batch pH drift is checked by ISO 787-9 because an out-of-specification aqueous suspension pH can change dispersion behaviour in PVC stabiliser packages. The pigment is not recommended for exterior weatherable profiles, because the lake type shows limited lightfastness in long-term outdoor exposure. Published data for this specific trade name in rigid PVC weathering is limited. The product is used in non-load-bearing pipes, interior profiles, electrical conduit, and dark-coloured technical mouldings where outdoor lightfastness is not the controlling specification.

    For single-screw injection moulding operations, a 50% pigment masterbatch is let down at 2–4 wt% into polypropylene homopolymer or impact copolymer. Masterbatch is produced on a co-rotating twin-screw extruder with L/D 40:1 and strand pelletizing. The filter pressure value is determined in accordance with EN 13900-5, and a rise above 0.5 MPa during the first 10 min indicates inadequate pigment wetting or an overloaded screw. Melt temperature is normally held below 220°C for polypropylene; above this temperature, residence time must remain under 90 s because the calcium lake can decompose at the upper boundary of the processing window. Published data for this specific configuration is limited, so each masterbatch lot is checked against a sealed reference plaque. The final mouldings are used in non-food crates, appliance housings, closures, and technical furniture components. For toy applications, EN 71-3:2019 batch migration testing is required before acceptance. For electrical and electronic equipment housings, the heavy metal restrictions of RoHS Directive 2011/65/EU apply to the pigmented polymer compound, not to the pigment alone, and incoming lot certificates are normally requested from the pigment supplier.

    When Solvent-Borne Flexographic Inks Require Non-Low-Migration Red Tonality

    A nitrocellulose/polyurethane binder system disperses Brilliant Red BBC by bead milling at 2,000–3,000 rpm for 45–90 min, depending on chamber volume and media size. Final ink pigment content is normally 3–5 wt% for flexo and 5–8 wt% for gravure dilution curves. Viscosity at press side is adjusted to 18–25 s in a 4 mm DIN cup at 25°C. Printability is checked with a laboratory IGT or flexo proof press using test prints referenced to ISO 2834-1. The major processing constraint is solvent strength: high ketone fractions above 20 wt% in the final reduction solvent can extract low-molecular-weight azo species and shift the visible red shade toward blue, while slow-evaporating glycol ethers increase residual solvent retention on film. After a 30 min press stop, re-solubility is evaluated on the plate; excessive pigment settlement in the anilox cells appears as lowered colour strength and requires a defined wash-up cycle. The product is used in surface-printed non-food labels, shrink wrap, and outer packaging where migration control is not the controlling specification. Applications involving food contact require a functional barrier and migration verification under the applicable packaging regulation.

    Compliance checklist for downstream qualification of Brilliant Red BBC
    Standard or regulationScopeRequired downstream control
    EN 71-3:2019Migration of elements from toy componentsBatch analysis for Pb, Cd, As, Ba, Sb, Hg, Cr, Se before toy use; limits depend on material category
    EU REACH Annex XVII entry 43Azo colourants that may release restricted aromatic aminesFinished textile and leather articles must not release amines above 30 mg/kg per EN ISO 14362-1:2017
    EU 10/2011Plastic materials and articles for food contactPositive-list absence requires migration verification and barrier performance; no presumption of compliance
    RoHS Directive 2011/65/EUElectrical and electronic equipment materialsHeavy metal limits apply to the final polymer compound; supplier certificate for Pb, Cd, Hg, Cr(VI) is normally requested
    ISO 787-9pH value of pigment aqueous suspensionIncoming quality control for batch-to-batch pH drift; pH outside specification can alter dispersion in aqueous and solvent systems

    Powder Coating Gel Time, Pinholing, and Overbake Yellowing

    In powder coating manufacture, premix extrusion at 90–110°C compound barrel temperature disperses the pigment into a 50:50 epoxy-polyester hybrid binder. The pigment loading for RAL 3000-series reds is typically 3–6 wt% in the final coating powder. Gel time is measured at 180°C in accordance with ISO 8130-6; a gel time below 90 s is likely to promote pinholing at film thicknesses above 70 µm. Overbake response is evaluated at 220°C for 20 min, and the colour difference is assessed against a reference panel. Brilliant Red BBC is limited to indoor uses, because accelerated weathering under QUV-B 313 conditions produces measurable fade for this lake type. Published data for this specific trade name in exterior powder coatings is limited. The cured film is used for indoor metal furniture, shelving systems, partition frames, and non-exposed appliance components. Outdoor architectural powder coating specifications require a weatherable pigment replacement rather than an overbake adjustment.

    Sulfur Cure Reversion Begins at the Azo Lake Surface in NBR Compounds

    When added at 1.0–2.0 phr on total rubber hydrocarbon, Brilliant Red BBC is incorporated on a two-roll mill at 40–50°C with a nip gap of 0.5–1.0 mm. The milled batch is then compounded with sulfur, accelerators, and activators. Vulcanisation is monitored on a rotorless curemeter in accordance with ISO 6502; at 1.0 phr the effect on t90 is normally below 5% compared with an unpigmented control, but at 2.0 phr the lake surface can adsorb accelerator fragments and shift scorch time. Surface exudation is assessed after storage for 7 days at 40°C in a closed container. Loadings above 2.0 phr are operationally constrained by bloom formation on the cured article. The pigment is used in non-food rubber goods, automotive gaskets, industrial mats, and conveyor belt covers. Contact with light-coloured rubber stocks requires evaluation because the pigment can transfer during vulcanisation and storage.

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    Certification & Compliance
    More Introduction

    Brilliant Red BBC is the commercial designation for a standardised acid dyestuff of the monoazo class, indexed as C.I. Acid Red 151, CAS 6406-56-0, molecular mass 479.42 g/mol. The dry product is a red-brown anionic powder whose tintorial strength is normalised to 100% against the current manufacturer’s reference. The standard model is a non-dusting powder intended for automated dyehouse dosing and manual weighing; a roller-compacted granulate may be specified where airborne dust control is critical. The dye molecule carries sulphonate groups and therefore exhausts onto substrates that expose protonated amino groups in aqueous acid media. It is not a solvent-soluble colorant, not a pigment dispersion, and not a covalently fixing reactive dye. The dry powder presents a bulk density of 0.45–0.60 g/cm³ and a pH in 1% aqueous suspension of 5.0–7.0, determined according to ISO 787-9.

    Each production lot is standardised in a horizontal ploughshare mixer with baffled intensifier elements to a batch size of 500–2,000 kg. Tintorial strength is measured in triplicate by UV-Vis spectrophotometry; the relative standard deviation of the method is below 1.0%. Retention samples are stored at 40 °C and 75% relative humidity for 4 weeks as an accelerated stability check. A strength shift greater than 2.0% triggers re-standardisation review before release. Each batch is linked to a control sample retained for 36 months.

    What Are the Point-of-Supply Acceptance Criteria?

    Specification compliance is verified by the methods listed in Table 1. The values are batch-release criteria; certificates of analysis report the measured value for each production lot. Appearance is assessed by visual comparison to the sealed reference standard under daylight-equivalent illumination. Tintorial strength is determined by UV-Vis spectrophotometry at λmax in the range 515–525 nm; the exact wavelength is batch-specific. Moisture is measured by gravimetric loss on drying at 105 °C according to ISO 787-2. Water-insoluble matter is determined by hot water extraction and filtration through a 10 μm membrane, reported as mass percent. pH is measured on a 1% aqueous suspension using ISO 787-9. Banned aromatic amines are extracted and quantified according to EN 14362-1:2017 and must not exceed the REACH Annex XVII limit of 30 mg/kg per amine.

    ParameterTypical release limitTest method
    AppearanceDark red to red-brown powderVisual comparison to sealed reference
    Tintorial strength100% ± 2.5% relative to referenceUV-Vis spectrophotometry at 515–525 nm
    Moisture≤ 5.0% by massISO 787-2
    Water-insoluble matter≤ 0.5% by massHot water extraction, 10 μm filtration
    pH of 1% aqueous suspension5.0–7.0ISO 787-9
    Banned aromatic amines≤ 30 mg/kg per amineEN 14362-1:2017
    Lead≤ 10 mg/kgISO 11885 ICP-OES
    Cadmium≤ 1 mg/kgISO 11885 ICP-OES

    For wool and nylon exhaust dyeing, a typical production dyebath is set at a liquor ratio of 1:10 to 1:20, with 1.0–3.0% dye on mass of fibre, 1.0–2.0 g/L anhydrous sodium sulphate, and sufficient acetic acid/sodium acetate buffer to hold pH between 4.0 and 5.5. On wool yarn packages, the bath is raised at 1.5 °C/min to 95 °C and held for 45 min; on nylon-6,6, the temperature is raised to 98 °C and held for 30–45 min depending on package density. A non-ionic or anionic levelling agent of the fatty alcohol ethoxylate class is used at 0.5–1.0 g/L for high-density yarn packages. Exhaustion is checked by UV-Vis absorbance at λmax; residual dyebath absorbance above 0.05 AU indicates under-exhaustion and should be corrected by pH reduction or extended hold time. On chrome-retanned leather, the dye is applied in the dye drum at 0.5–2.0% on shaved weight at 60 °C for 40–60 min; fixation is improved when the bath pH is maintained at 3.8–4.2 after dye addition and before basification with sodium formate.

    Exhaustion on wool follows a Langmuir-type profile; at pH 4.0 the initial uptake rate is approximately 0.8% of applied depth per minute over the first 10 min, but this rate is highly dependent on liquor ratio and fibre surface charge. In package dyeing, the rate is moderated by the levelling agent because radial flow through the package produces a concentration gradient; a temperature hold at 70 °C for 15 min is inserted when package density exceeds 350 g/L. Non-ionic auxiliaries with a cloud point below 90 °C should not be used in high-temperature nylon dyeing because phase separation may carry dye to the machine lid and create condensation marks. Anionic naphthalene sulphonate condensates are preferred at 0.5–1.5 g/L; their presence reduces unlevelness but can retard exhaustion by up to 10% at pH 5.5.

    Solution Preparation Limits and Dyebath Stability Under Process Water Hardness

    Brilliant Red BBC is dispersed as a paste in cold water at 20–30 °C before dilution. Direct contact with live steam is not recommended because local overheating above 70 °C can produce gelatinous particles that deposit as specks on package and beam surfaces. Stock solutions above 5.0 g/L in process water containing more than 120 mg/L calcium carbonate are subject to viscosity rise; a sequestering agent based on polyphosphate or polyacrylate is added at 0.2–0.5 g/L before dye introduction. The dyebath is sufficiently stable for 8 h at 80 °C within pH 4.0–6.5; outside this window hydrolytic strength loss can exceed 3% per hour. Avoid adding cationic fixatives before full exhaustion because the resulting anionic-cationic complex forms a red-brown precipitate that can blind the filter elements of package dyeing machines. The dye is incompatible with strong reducing agents such as sodium hydrosulphite above 60 °C; shade stripping is therefore controlled at 50–60 °C with a buffered reduction assistant.

    In product-selection comparisons, Brilliant Red BBC differs from C.I. Acid Red 18 and C.I. Acid Red 73 in electrolyte sensitivity and build-up behaviour. C.I. Acid Red 18 requires higher salt loadings to reach equivalent exhaustion and shows greater migration after wet contact on wool; C.I. Acid Red 73 produces a yellower red hue and is more prone to shade drift in leather drum processes when free iron is present in process water. A replacement for C.I. Acid Red 18 in an existing recipe begins at a strength-equivalent ratio of 0.8:1.0; the colour model must be recalibrated because the absorption maximum differs by 10–15 nm. Brilliant Red BBC does not form covalent bonds with cellulose and is not a direct replacement for reactive red dyes; on polyamide at depths above 1.0% owf, an aftertreatment is required to achieve wet fastness values above grade 3 according to ISO 105-C06.

    When the Dye Is Applied in Narrow-Ratio Beam Dyeing of Nylon Automotive Fabric

    Beam dyeing of nylon-6,6 automotive fabric at liquor ratios below 1:6 imposes circulation and levelness constraints. The dyestuff is pre-dissolved in a side tank and dosed over 20 min at 0.8–1.5 L/min, while the main pump maintains lattice circulation at or above 2.5 L/kg/min. The fabric is wound on perforated beams with an open-area ratio above 25%; this prevents differential pressure spikes above 1.5 bar and reduces the risk of edge-to-centre shade variation. The temperature ramp is limited to 1.0 °C/min from 50 °C to 85 °C and 0.5 °C/min from 85 °C to 98 °C. Production trials have documented centre-to-selvedge red-shift drift when the heating rate exceeds 1.5 °C/min on high-density beam batches. After the hold step, rinsing is started only when the extracted dyebath absorbance at λmax is below 0.02 AU; premature rinsing transfers unfixed dye to the beam core and increases outer-lap redness.

    Aftertreatment Reactions with Tannin and Syntan Systems on Nylon-6,6

    At depths above 1.0% owf, the wet fastness of Brilliant Red BBC on polyamide is improved by an aftertreatment with a syntan of the phenol-sulphonic acid type or, for higher wash fastness, a two-step syntan/cationic fixative sequence. The aftertreatment is run in a fresh bath at 70–80 °C for 20 min at pH 3.5–4.5. A residual anionic dye load must be removed before the cationic step; otherwise the resulting complex forms a surface deposit that lowers crock fastness under ISO 105-X12. On nylon-elastane blends, the product should be tested according to ISO 105-C06 and ISO 105-E04 for perspiration; published data for this specific blend configuration is limited, so a plant trial on the target knitted construction is required before bulk production. The aftertreatment does not alter the hue substantially on nylon-6,6, but a slight yellow shift of 0.2–0.5 CIELAB Δb* may occur on nylon-6.

    Regulatory compliance is supported by batch-specific analysis for banned aromatic amines according to EN 14362-1:2017 and, for leather, ISO 17234-1:2015. The product is not cleared as a food-contact colorant under Regulation (EC) No 1935/2004; use in food packaging requires a specific migration evaluation. Store in sealed HDPE containers at 10–30 °C and relative humidity below 60%. Open containers exposed to higher humidity should be dried at 35 °C before weighing to prevent strength errors from moisture sorption. Re-test interval is 24 months from the production date when stored in original packaging.