| HS Code | 732815 |
| Product Name | Brilliant Red 2BL |
| Synonyms | Direct Brilliant Red 2BL; C.I. Direct Red 81; C.I. 28160 |
| Color Index Name | C.I. Direct Red 81 |
| Color Index Number | 28160 |
| Cas Number | 6459-94-5 |
| Einecs Number | 220-028-9 |
| Molecular Formula | C29H19N5Na2O8S2 |
| Molecular Weight | 675.59 |
| Chemical Class | disazo direct dye |
| Appearance | red to dark red powder |
| Solubility | soluble in water |
| Ph | 7.0-9.0 |
| Moisture Content | ≤5.0% |
| Insoluble Matter | ≤0.5% |
| Dye Content | ≥95% |
| Storage Conditions | store in a cool, dry, well-ventilated place |
| Application | dyeing and printing of cotton, viscose, paper, leather and silk |
As an accredited Brilliant Red 2BL factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Brilliant Red 2BL is supplied in 25 kg sealed, moisture-resistant fiber drums with plastic liners and clear hazard labels. |
| Container Loading (20′ FCL) | Brilliant Red 2BL loaded in a 20-foot full container load, packed securely for chemical shipment with proper labeling and documentation. |
| Shipping | Shipment: Brilliant Red 2BL dye, generally non-hazardous unless SDS states otherwise. Use sealed, labeled containers; protect from moisture, heat, and sunlight; include SDS and proper documentation; comply with applicable DOT/IATA/IMDG regulations. |
| Storage | Store Brilliant Red 2BL in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and open flames. Keep containers tightly closed, clearly labeled, and protected from moisture and dust. Store only in original or compatible containers. Segregate from strong oxidizers and incompatible materials. Use secondary containment, avoid spills, and follow local regulations and the safety data sheet. |
| Shelf Life | Stable under recommended storage conditions; typical shelf life is 24 months when kept cool, dry, and protected from direct light. |
In loose-stock and top dyeing of wool for melange or solid-colour worsted yarn, Brilliant Red 2BL is exhausted from a weakly acidic float onto pre-scoured fibre. Commercially supplied as the sodium salt of C.I. Acid Red 249 (C.I. 18134, CAS 6416-66-6), the dye is an unmetallised monoazo acid dye with sulphonic acid solubilising groups; stock solutions are prepared by pasting with demineralised water and dissolving at 80–90 °C at 1–5% w/v. The wool substrate is scoured with nonionic detergent at 40–50 °C and rinsed until residual surfactant does not interfere with dye uptake; package density in radial-flow machines is adjusted to avoid channeling. Exhaustion is carried out at a liquor ratio of 1:10–1:20 with 0.5–3.0% owf dye, 5–10% owf sodium sulphate, and an acetic acid/sodium acetate buffer giving pH 4.5–5.5. The bath is set at 40 °C, held for 10–15 min, raised at 1.0–1.5 °C/min to 98 °C, and held for 45–60 min. Strike is limited below 60 °C; migration becomes significant above 80 °C, which improves levelness in package and top dyeing but requires controlled heating through 60–85 °C to avoid skittery dyeing on wool blends. After exhaustion, the bath is cooled to 60 °C before overflow rinse; sudden cooling below 40 °C on loose stock can cause fibre compaction and subsequent carding faults. Wet fastness is assessed according to ISO 105-C06 A2S or C2S, perspiration according to ISO 105-E04, rubbing according to ISO 105-X12, and light according to ISO 105-B02:2014 at 1/1 standard depth. The unmetallised monoazo chromophore is classed as moderate light fastness; published fastness data for this specific configuration are limited, but after-treatment with 2–4% owf of a cationic fixing agent at 70–80 °C for 20 min raises wet fastness by approximately 0.5–1.0 grey-scale step. The same cationic agent must never be added to the dyebath because dye–fixing-agent precipitation causes filter blocking in package machines and uneven surface deposition. Hard water above 100 mg/L as CaCO₃ requires 0.5–2 g/L tetrasodium EDTA or condensed phosphate; otherwise shade dulling and filter blocking increase.
The pH-control strategy on nylon 6 semi-dull circular knits determines whether Brilliant Red 2BL covers physical barre or intensifies it; the dye is applied only after pre-scouring with 1–2 g/L sodium carbonate and 0.5–1 g/L nonionic surfactant at 60–70 °C to remove spin finishes and knitting oils. The substrate has amino end-group content in the range of 30–50 mmol/kg, which provides cationic dye sites under acid conditions; adsorption of the anionic dye is therefore controlled by pH, temperature, and added retarder. A typical jet or overflow bath is set at 30–40 °C with 1:10–1:15 liquor ratio, 0.5–2.0% owf dye, 2–4% owf ammonium sulfate, and enough acetic acid to start at pH 6.0–6.5. During heating at 1 °C/min to 98 °C, ammonium sulfate hydrolyses and shifts the bath to pH 4.0–4.5, limiting rapid strike. Hold time is 30–45 min at 98 °C; nylon 6 withstands this temperature, whereas nylon 66 may be processed similarly but benefits from the same upper limit to avoid setting creases. Barre coverage is the main process conflict: differences in yarn draw ratio, texturing conditions, or fibre morphology produce differential uptake. A mildly anionic levelling agent at 0.5–1.0 g/L competes for amino sites, retards initial strike, and improves apparent levelness, but overdosing above 1.5 g/L reduces final depth and requires longer hold time. Dye migration at 98 °C is sufficient for correction of minor shade variation, but severe barré from mixed yarn lots cannot be fully masked. After cooling to 60–70 °C, the fabric is rinsed and fixed with 2–3% owf of a synthetic tanning agent or cationic dye-fixing agent at 70 °C for 20 min and pH 4.0–4.5. Fastness is evaluated using AATCC TM107 for water, AATCC TM15 for perspiration, AATCC TM61 2A for accelerated laundering, and ISO 105-B02 for light. The red chromophore is applicable to lining, tricot, hosiery, and sportswear where moderate light fastness and wet fastness after fixation are acceptable. Do not combine with cationic softeners or fixing agents in the dyeing bath; precipitation with the unmetallised acid dye occurs immediately and deposits on fabric contact points in jet machines.
| Substrate | pH control system | Maximum temperature | Holding time | Dye concentration | Key process constraint |
|---|---|---|---|---|---|
| Wool loose stock/top | Acetic acid/sodium acetate, 4.5–5.5 | 98 °C | 45–60 min | 0.5–3.0% owf | Migration above 80 °C controls levelness; cool before rinse |
| Nylon 6 knit | Ammonium sulfate/acetic acid, start 6.0–6.5, final 4.0–4.5 | 98 °C | 30–45 min | 0.5–2.0% owf | Barre coverage; avoid anionic retarder overdose |
| Silk hank/piece | Acetic acid, 4.0–5.0 | 85–90 °C | 30–40 min | 1–3% owf | Fibre strength loss above 90 °C at low pH |
Leather crust stock at pH 3.8–4.2 after chrome retanning accepts Brilliant Red 2BL in the same float without intermediate washing, provided the retanning bath has been drained to the required 150–200% water float at 40–50 °C. The anionic dye is added at 2–4% owf on shaved weight together with 0.5–1.0% owf of a naphthalene-sulfonate levelling agent; the drum runs at 8–12 rpm for 30–40 min to allow penetration through the grain and corium. Fixation is then initiated by adding 0.5–1.0% owf formic acid diluted 1:5 with water in two or three portions over 20 min, bringing the float to pH 3.4–3.6. A final run of 20–30 min yields exhaustion typically above 90%, indicated by a nearly clear float; fixation below pH 3.2 or formic acid added too rapidly causes grain bronzing and uneven surface dye aggregation. Feed sequence is critical: the dye must be added before cationic fatliquors, chromium syntans, or cationic retanning agents; if cationic products are already present, the sulfonated dyestuff precipitates as a lake on the grain and creates dark streaks. For suede and split leather, a longer penetration phase at 40–45 °C is used, followed by surface fixation. Rubbing fastness is assessed according to ISO 11640:2018, perspiration fastness according to ISO 11641, and light fastness according to ISO 105-B02. The dyed leather is applicable to upholstery, garment, and shoe upper specifications where uniform penetration and moderate light fastness are required.
Because silk loses tensile strength at elevated temperature in acid baths, the critical constraint in hank and piece dyeing is not dye exhaustion but fibre integrity. Degummed silk is entered at 40 °C into a bath containing 1–3% owf Brilliant Red 2BL, 5–10% owf sodium sulphate, and acetic acid to pH 4.0–5.0; the temperature is raised at 1 °C/min to 85–90 °C and held for 30–40 min. Processing at 98 °C or below pH 3.5 accelerates silk degradation, reduces lustre, and increases yarn breakage in star-frame and overflow machines. After dyeing, the material is rinsed at 40 °C; if wet fastness is specified for scarves or embroidery threads, treatment with 1–2% owf cationic fixing agent at 60–70 °C for 15–20 min is applied. Light fastness remains in the moderate range, so the red shade is used for apparel and decorative silk rather than curtain or automotive fabric.
Surface-sized woodfree paper introduces a charge-control problem when Brilliant Red 2BL is metered into a starch or polyvinyl alcohol size press liquor at 0.05–0.5% of size solids; the anionic dye forms an ionic complex with cationic poly-DADMAC or glyoxalated polyacrylamide, which immobilises the colour and improves bleed resistance. To avoid coagulation in the supply tank, the cationic fixative is added after starch cooking and cooling below 60 °C, with high-shear mixing; the dye is then dosed as a 1% solution under recirculation. The size liquor pH is held at 6.5–7.5 because acid hydrolysis of starch below pH 4.5 reduces viscosity, alters pickup, and causes blade scratches on the size press. At 0.1–0.3% poly-DADMAC on oven-dry paper, bleed fastness improves, but higher addition levels cause two-sided retention differences and a dulling of the red hue. In beater dyeing, the dye is added at 0.05–0.2% on dry pulp after refining, followed by alum or a cationic retention aid; end uses are coloured writing paper, file folders, tinted tissue, and laminating base stocks where water fastness after drying is the primary specification.
Unless the anodic oxide layer is freshly formed and pore-regular, Brilliant Red 2BL uptake on aluminium is non-uniform and commercially unusable. The preferred oxide layer has a pore diameter of 10–30 nm and film thickness of 5–20 µm, typically produced in 15–20 wt% sulfuric acid at 18–22 °C and 1.5 A/dm². After anodising, the aluminium is rinsed in demineralised water at pH 5.5–6.5, then immersed in a dye bath containing 1–5 g/L Brilliant Red 2BL at 50–60 °C for 10–20 min, with pH adjusted to 5.0–6.0 using acetic acid/sodium acetate. Lower pH accelerates surface adsorption and produces uneven shading; higher pH reduces dye uptake and weakens final depth. Sealing follows in hot demineralised water at 96–100 °C for 30–45 min or in nickel acetate 5–10 g/L at 70–80 °C for 15–20 min; incomplete sealing causes dye bleed under humidity and lowers fastness. Electrolyte aluminium content above 15–20 g/L reduces pore regularity, causing non-uniform dye uptake. Light fastness for coloured anodic coatings is evaluated according to ISO 2135:2016; the unmetallised red chromophore is applicable to interior trim, appliance facings, signage, and cosmetic packaging, but not to exterior architectural components requiring high UV resistance.
| Parameter | Range | Control point |
|---|---|---|
| Oxide film thickness | 5–20 µm | Lower thickness reduces dye capacity; higher thickness may crack on bending |
| Pore diameter | 10–30 nm | Sulfuric acid anodising at 18–22 °C yields regular pores |
| Dye concentration | 1–5 g/L | Higher concentration shortens time but increases surface adsorption risk |
| Dye bath pH | 5.0–6.0 | Acetic acid/sodium acetate buffer |
| Dye bath temperature | 50–60 °C | Above 60 °C increases rate but reduces bath stability |
| Dyeing time | 10–20 min | Extended time has no benefit after pore saturation |
| Sealing | 96–100 °C water or 70–80 °C nickel acetate | Incomplete sealing causes bleed |
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Brilliant Red 2BL is a commercial designation for a water-soluble reactive dye preparation supplied primarily as low-dusting granules or spray-dried powder for cellulosic fibre coloration. The visible spectrum of an aqueous solution shows a principal absorption band in the 520–540 nm region; the exact λmax is salt-form and pH dependent. The 2BL designation does not identify a single Colour Index constitution across all suppliers, so mill certificates must be checked for the reactive group, electrolyte content, and standardization agent. Typical release documents report dye strength by UV-Vis spectrophotometry against a retained reference, insolubles by mesh retention, and moisture by drying to constant mass. The product is used in package, jig, and continuous pad operations; it is not a disperse dye, acid dye, or pigment dispersion, and it should not be prediluted in hard water containing more than 150 mg/L CaCO₃ equivalent.
On a 1,200 kg package dyeing spindle with internal circulation at 2–3 L/kg/min, the dominant process variables are salt migration time, alkali metering rate, and fixation hold. The dye is charged to the expansion tank as a filtered solution at 70–80°C. Sodium chloride is added in three equal portions over 20–30 min to reach 50–80 g/L. Exhaustion before alkali addition is held at 70–80% to avoid tailing across the package radius. Soda ash solution is then metered at 0.4–0.6 g/L/min until the bath reaches pH 10.8–11.2. Run time after alkali addition is limited to 45–60 min at 60–70°C; longer fixation increases hydrolyzed dye concentration in the bath but does not improve depth. The spent bath is sampled at 520–540 nm to calculate fixation efficiency from the residual absorbance after correction for hydrolysis products.
Package density should be maintained at 360–420 g/L for cotton yarn. Higher density reduces flow at the core and produces a radial shade bore of more than 0.5 ΔE CIELAB measured on the D65/10° observer. In two-stage rope washing after exhaust dyeing, the first wash box operates at 95–98°C with 1.0–2.0 g/L nonionic detergent for 10–15 min; the second box runs at 80°C with overflow rinse. Final rinse absorbance above 0.05 at the λmax indicates insufficient flow or excessive load density and requires lowering the packing density or increasing fresh-water inflow.
Stock solutions for laboratory recipe development are prepared with demineralized water at 25–35°C using low-shear stirring; high-shear dispersers are unnecessary and can generate foam that alters volumetric dosing. Solutions are buffered to pH 7.0 before spectrophotometric strength evaluation. The measured strength is accepted only when the reference and sample are read at the same λmax and normalized to dry weight. Insolubles are checked by filtration through a 125 µm sieve; insoluble matter above 0.5% is sufficient to cause streak formation in continuous padding. Moisture is determined by oven drying at 105°C to constant mass; granular lots above 5.0% moisture are held for re-drying because flowability in automatic dispensing systems declines.
In continuous pad-steam dyeing, the chemical pad mixes Red 2BL with alkali, salt, urea, and wetting agent. To limit hydrolysis before fixation, the trough volume is held below 30–50 L for a 1.8 m wide range running at 40–60 m/min. Liquor pickup is set at 60–80%. A typical reduced-alkali pad contains 5–10 g/L sodium carbonate, 1–3 g/L sodium hydroxide, and 50–80 g/L urea. The fabric then enters a saturated-steam fixation chamber at 101–103°C for 8–12 min. The critical risk is dwell time after in-line mixing; in high-temperature troughs, the reactive species can lose 10–20% of strength within 30 min if the dye and alkali are precombined. Modern ranges therefore meter alkali at the nip using a static mixer immediately before the liquor trough. Exhausted pad liquor should be discarded after 45 min; shade variation across the fabric width of 0.3 ΔE CIELAB or more indicates that hydrolysis products are forming in the recirculation loop.
| Property | Method / instrument | Acceptance criterion |
|---|---|---|
| Strength vs reference | UV-Vis at λmax in deionized water | 95–105% |
| Moisture | Oven drying at 105°C | ≤5.0% |
| Insolubles | 125 µm sieve retention | <0.5% |
| Aqueous solubility | Cylinder method at 25°C | report g/L |
| pH of 10 g/L solution | Glass electrode at 25°C | 6.0–8.0 |
| Wash fastness of dyed cotton | ISO 105-C06 A1S | meets buyer minimum |
| Crock fastness | ISO 105-X12 | meets buyer minimum |
| Light fastness | ISO 105-B02 | reported |
Substitution of a vinyl sulfone red with a 2BL-type preparation changes the alkali and drying profiles. Vinyl sulfone systems typically rely on higher alkali reserve; the 2BL formulation requires a lower sodium carbonate level and controlled after-pad drying to avoid migration. Cylinder dryers are profiled to leave 20–25% residual moisture at the steamer inlet. If the fabric is over-dried below 10% moisture, fibre accessibility decreases and surface bronzing appears in deep shades. Compared with direct non-reactive reds of similar shade, Red 2BL provides covalent fixation to cellulose; however, unfixed hydrolyzed dye must be removed by soaping because the residue acts as a fibre-surface pigment and reduces crock fastness measured by ISO 105-X12. The colorimetric difference after wash-off is characterized by the fastness rating and by the ΔE shift after 3 industrial washes.
Package dyeing of cotton sewing thread with Red 2BL operates at 1:6 to 1:10 liquor ratio on high-pressure spindles. The dye is dissolved at 70–80°C and filtered before injection into the expansion tank. Injection rate is limited to 2–4 L/min per 100 kg of yarn to prevent concentration shock at the core. A production failure mode observed on high-density spindles is layer-to-layer shade variation of 0.6 ΔE CIELAB when alkali is injected through the spindle base. The correction moves the alkali injection point to the pressure-side circulation line and inserts a neutral circulation phase of 15 min before temperature ramp.
Granular Red 2BL is hygroscopic; storage above 65% relative humidity increases moisture and reduces flowability in automatic dispensing systems. Warehouses should maintain 20–30°C and 40–60% RH. Opened containers are returned to sealed polyethylene liners immediately after weighing. Dusting potential is controlled by granulation; full-shift breathing-zone particulate monitoring is conducted according to occupational hygiene protocols. The aqueous dispersion shows low foaming under typical circulation; viscosity of a 100 g/L stock solution at 25°C is usually below 50 mPa·s, which is compatible with piston-dosing pumps and static mixers. Compatibility with anionic wetting agents is acceptable; strong cationic aftertreatment agents should not be mixed with the neat solution because precipitation can occur.
| Process variable | Exhaust package dyeing | Continuous pad-steam |
|---|---|---|
| Substrate preparation | scoured/bleached cotton packages | scoured/bleached open-width fabric |
| Liquor ratio / pickup | 1:6–1:10 | 60–80% pickup |
| Sodium chloride | 50–80 g/L | 0–20 g/L as required |
| Sodium carbonate | 10–15 g/L | 5–10 g/L |
| Additional alkali | none | 1–3 g/L sodium hydroxide |
| Fixation | 60–70°C for 45–60 min | 101–103°C steam for 8–12 min |
| Wash-off | two-stage soaping at 95–98°C | counterflow wash boxes with soaping at 95°C |
| Potential failure | core shade bore from rapid alkali injection | tail-to-head shade variation from hydrolysis |
On jig dyeing of woven cotton poplin, the same dye is applied at 1:3 to 1:5 liquor ratio with double-end jig circulation. Alternating immersion cycles are set to 8–12 passes after salt addition and 6–8 passes after soda ash addition. The greatest risk is end-to-end shade deviation caused by dye hydrolysis in the trough between passes; fresh alkali is added in two portions rather than as a single liquor charge. Fabric temperature at the roll is maintained below 40°C during sampling to avoid drying creep.