| HS Code | 103418 |
| Product Name | Direct Orange S |
| Color Index | C.I. Direct Orange 26 |
| Cas Number | 3626-36-6 |
| Chemical Class | Disazo direct dye |
| Appearance | Orange powder |
| Water Solubility | Soluble in water |
| Application | Dyeing of cotton, viscose, paper and leather |
| Dyeing Temperature | 80-90 °C |
| Ph Range | 6-8 |
| Moisture Content | ≤5% |
| Dye Content | ≥95% |
| Packaging | 25 kg bag |
| Shelf Life | 24 months |
As an accredited Direct Orange S factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Direct Orange S is packaged in 25 kg net multi-ply paper sacks with polyethylene liners, sealed for safe transport and storage. |
| Container Loading (20′ FCL) | Direct Orange S is packed in dry, intact bags or pallets, loaded into a clean 20′ FCL container, secured, and protected from moisture. |
| Shipping | Direct Orange S is generally shipped as a non-dangerous-goods solid dye in sealed, labeled containers. Protect from moisture, heat, and sunlight; segregate from oxidizers. Use standard freight, and verify the SDS, UN classification, and local regulations before shipment. |
| Storage | Store Direct Orange S in a cool, dry, well-ventilated area away from direct sunlight and moisture. Keep containers tightly closed when not in use to prevent dust generation and contamination. Separate from strong oxidizing agents, acids, and alkalis. Use appropriate secondary containment, label clearly, and follow local regulations and the SDS. Avoid inhaling dust; wear suitable PPE during handling. |
| Shelf Life | Stable under recommended storage conditions; typically has a shelf life of 24 months when kept cool, dry, and protected from light. |
In cotton knit exhaust dyeing, Direct Orange S is introduced as an anionic disazo colorant whose substantivity for cellulosic fibre relies on controlled electrolyte screening rather than mordant chemistry. In production jet equipment operating at liquor ratios of 1:8 to 1:12, the dye is added at 0.5–2.5% owf for batch depths; pale shades require 0.2–0.5% owf, medium shades 0.8–1.5% owf, and deep shades 2.0–3.0% owf. Anhydrous sodium sulfate is metered in three portions at 60°C, 75°C, and 90°C to a total of 20–60 g/L, and soda ash is held at 1.0–2.0 g/L to stabilize the slightly alkaline bath. The substrate is loaded at 40°C, heated at 1.0–1.5°C/min, held at 95–98°C for 45–60 min, then cooled to 60°C before a cationic fixative aftertreatment at 2–4 g/L and 45°C for 20 min. Without aftertreatment, wet crocking values on deep shades commonly fall below acceptable retail cutoffs, and residual unfixed dye in the spent bath contributes to high wastewater colour load. Production lots should not be combined with sodium hydrosulfite or other reducing agents, because reductive cleavage converts the disazo structure to lower-colour fragments and may create an aromatic amine testing obligation under REACH Annex XVII Entry 43 via EN ISO 14362-1:2017.
| Standard | Test scope | Operational condition |
|---|---|---|
| EN ISO 105-C06:2010 | Wash fastness | A2S, 40°C, 30 min |
| EN ISO 105-X12:2016 | Crocking fastness | Dry and wet, 9 N vertical load |
| EN ISO 105-B02:2014 | Light fastness | Xenon arc, blue wool reference scale |
| EN ISO 14362-1:2017 | Azo colourant reductive cleavage | Fibre extraction and non-extraction methods |
Package dyeing of viscose rayon requires lower circulation temperatures and lower electrolyte loads than cotton because wet viscose loses tensile strength above 90°C and high salt concentrations can retard dye migration inside the package. The dye is dosed at 0.5–2.0% owf into a package dyeing vessel filled at liquor ratio 1:6 to 1:10; anhydrous sodium sulfate is added only after the bath has reached 60°C and only to 10–30 g/L. Bleached viscose yarn is wound on stainless steel or polypropylene dye tubes at a uniform density of 350–380 g/L; soft edges or non-uniform winding produce channeling that appears as pale internal bands on production packages. Flow reversal is set to 4–5 cycles/min, with differential pressure held at 0.8–1.2 bar, while the bath is heated at 0.7–1.0°C/min to 85–90°C and held for 30–40 min. After cooling to 45°C, a cationic fixative is applied at 3–5 g/L and pH 5.5–6.5 for 20 min. The compliance framework includes ZDHC MRSL screening for dyestuffs and fixatives, REACH Annex XVII Entry 43 testing by EN ISO 14362-1:2017 when the final article is placed on the EU market, and fastness checks by EN ISO 105-C06:2010 wash test and EN ISO 105-X12:2016 crocking test. Terminal formats include viscose rayon embroidery yarn, decorative ribbon tape, and woven lining fabrics; these applications accept moderate wet fastness and require low crocking on pale to medium depths.
Stock dyeing for packaging board uses the wet-end cationicity of the paper machine to retain the anionic disazo chromophore before headbox deposition, not after size-press surface treatment. Direct Orange S is dissolved at 5–15 g/L in hot water at 60–80°C and metered into the thick-stock chest at 0.2–1.5 kg/t dry pulp; the target pH is 4.5–6.0, and alum is maintained at 0.5–2.0% on dry fibre while a cationic retention aid is added at 0.01–0.05% on dry fibre. The machine chest consistency is held at 3.0–3.5%, and the dyed stock travels through a fan pump and pressure screen before deposition on the forming fabric; high shear after dye addition can destroy flocculated dye-retention complexes, so the dye injection point is located after the last high-shear screening stage where practical. Drying-induced migration produces a two-sided colour difference on heavier board grades above 250 g/m²; the effect is controlled by limiting wet-web drying rate in the first dryer section and by surface sizing after the dryer. Compliance for food-adjacent packaging is checked through FDA 21 CFR 176.170 for aqueous and fatty food contact, EU Regulation (EC) No 1935/2004 Article 3, and EN 646:2019 for colour fastness of dyed paper and board intended for food contact. Terminal products include coloured folder stock, poster board, paper bags, napkin tissue, and non-food packaging board where an orange shade is required without surface coating.
A formulation containing Direct Orange S at 0.5–5.0 wt% exhibits pH-dependent solubility loss when the waterborne vehicle drops below pH 6.5, because the sulfonate groups become partially protonated and the dye aggregates into particles that block 10 µm membrane filters. The dyestuff is predissolved as a 5–15 wt% stock in deionized water at 60–80°C and cooled to 30°C before addition to an acrylic or polyurethane dispersion held at pH 7.5–9.0. Mixing uses a high-shear disperser at 1,000–2,000 rpm for 30 min, followed by filtration through a 10 µm absolute-rated filter; viscosity is adjusted with propylene glycol or glycerin after dye addition to avoid premature shear-thinning of the vehicle. Stability testing includes centrifugation at 3,000 rpm for 15 min and a 5-day storage cycle at 50°C; precipitation at the meniscus indicates incompatible co-solvent or pH drift. For art and stationery materials, the finished ink is assessed under EN 71-3:2019+A1:2021 for migration of elements, EN 71-9:2005+A1:2007 for organic chemical requirements in toys intended for children under three years, and ASTM D4236 labeling for chronic health hazards. Terminal products include marker refill inks, stamp pad inks, paper stationery inks, and watercolor brush-pen formulations; the dye is not recommended for outdoor signage inks due to limited light fastness.
When the stain base is compounded at pH below 6.5, the sulfonate groups on Direct Orange S remain partly protonated, lowering dye solubility and causing specking in spray application. The dye is incorporated at 2–15 g/L in a water/alcohol/glycol ether stain or at 0.1–0.5 wt% in a ready-to-use acrylic/polyurethane dispersion; predissolution is conducted at 50–70°C under mild agitation before pH is corrected to 7.0–8.5 with ammonia or 2-amino-2-methyl-1-propanol. The stain is spray-applied at 1.5–2.0 bar with a 1.2–1.5 mm nozzle, flashed for 10 min at room temperature, and dried at 60°C for 30 min. Because direct dyes remain water-soluble after drying, a crosslinked acrylic or polyurethane topcoat is required to prevent stain bleed into perspiration or saliva simulants; without crosslinking, migration tests under EN 71-3:2019+A1:2021 and EN 71-9:2005+A1:2007 can fail on children’s wooden toys. The US retail route uses ASTM F963 heavy-metal migration protocols for toy substrates, and ASTM D4236 labeling for art or craft wood products. Terminal products include interior wood picture frames, craft wood components, decorative furniture trim, and wooden toys in markets where the complete coating system passes the relevant toy safety standard. Published data for this specific crosslinker–dye combination is limited; mill trials should include a 6-month migration and light exposure study before production lock.
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Direct Orange S is classified as C.I. Direct Orange 26, C.I. 29150, and is supplied as a water-soluble anionic azo dye. Commercial material is normally standardised against an in-house reference at 100% or 150% relative depth, with low-dusting granular and powder grades available. A 1% aqueous solution of the commercial grade is commonly controlled in the pH range 7–9, and the dye exhibits a visible absorbance maximum in the region 480–500 nm in deionized water; the exact value shifts with salt form, pH, and standardising diluents. Because commercial formulations contain electrolyte and diluents, published saturation solubility data for the neat dye are limited, but stock solutions at 5–15 g/L in demineralised hot water are routinely prepared in automated dispensing systems. The product is not a pigment dispersion: it dissociates into negatively charged chromophore ions and requires cellulose, paper pulp, leather, or another substrate with accessible hydrogen-bonding sites.
In package dyeing of cotton yarn, the primary processing conflict is the inverse relationship between exhaustion and migration. Package densities of 0.38–0.42 kg/L in inside-out flow machines with liquor ratios of 1:8–1:12 create high resistance to liquor exchange. Direct Orange S responds to anhydrous sodium sulfate at 5–30 g/L or sodium chloride at 2–12 g/L, but rapid salt dosing above 1 g/L/min has been observed in production lots to increase package edge shading and core-to-edge depth variation. Preferred operating conditions begin at 40–50°C with 0.2–0.5 g/L tetrasodium pyrophosphate or 0.5–1.0 g/L soda ash for hardness control, ramp to 90–95°C at 1–2°C/min, and dose electrolyte in three or four equal portions at 10–15 min intervals. Flow reversal every 2–4 min is typical. Batch-to-batch variation in direct dye strength is controlled by spectrophotometric dosing systems with in-liquor absorbance verification; the acceptable relative strength tolerance is normally ±3% against the reference. Hardness above 150 mg/L as CaCO₃ should be treated with a chelating agent, because calcium and magnesium ions can reduce solubility and precipitate the anionic dye in high-concentration dosing zones. Production records from high-density package machines indicate that process failures are more often caused by electrolyte shock than by insufficient total salt; stepwise salt addition improves levelness but extends total cycle time by 20–30 min.
In beater dyeing of bleached kraft and recycled fiber, Direct Orange S is added at 0.2–1.0% on dry fiber at stock consistency 2.5–3.5%. Retention requires a cationic mordant or retention aid; alum addition at 1–2% on dry fiber and pH 4.5–5.5 produces measurable fixation, while residual colour in white water is checked by absorbance against a calibration curve at the mill-specific wavelength of maximum absorbance. Polyamide-based wet-strength resins and high cationic charge demand can cause variable retention and mottling on recycled grades; the dye addition point should be moved upstream of alum and cationic starch to avoid premature flocculation. For leather drum dyeing, Direct Orange S is applied in retanning or dyeing drums at 50–60°C for 30–45 min with 0.5–1.5% on shaved weight; penetration is generally superior to acid dyes on vegetable-tanned stock, but wet fastness after fatliquoring remains lower than that of metal-complex acid dyes. The product is not recommended for synthetic-fiber dyeing without a cellulosic component because the anionic chromophore has negligible affinity for polyester, polypropylene, or unmodified polyamide in neutral-to-alkaline baths. Stock solubility in hard water should be checked by filtration through a 25 μm screen before addition to the machine; precipitates at this point indicate hardness or cationic contamination.
Direct Orange S can be applied on woven cotton or viscose by pad-steam methodology when a mill requires short-lot shading of orange earth tones. A typical wet-on-wet sequence uses a two-roll or three-roll padder with nip pressure set to deliver 60–80% liquor pickup; the pad bath contains 20–50 g/L urea or a migration inhibitor such as 0.5–1.0 g/L sodium alginate to reduce colour migration during intermediate drying. After padding, the fabric enters a predryer at 100–120°C and is then steamed at 101–103°C for 30–90 s. Unlike exhaust dyeing, salt is not the primary driving force in pad application, but electrolyte in the pad bath can improve fixation on highly swollen viscose and should be limited to 5–10 g/L to avoid dried-back marks at cylinder drying sections. Drying before steam fixation must be uniform to within ±5°C across the web; variation above this window has been associated with side-to-side depth differences on production pad-steam ranges. Continuous processors using direct dyes should measure shade in both the wet and dry states because Direct Orange S shifts visibly with moisture and after cationic aftertreatment. The pad bath should be checked for viscosity and foam, because foam in a continuous padder produces skittery dyeing and reduced depth.
On cotton knits, Direct Orange S is used as a low-cost shading component in browns, rusts, and dull oranges. The migration index is sufficient for jet dyeing at 1:8–1:15 liquor ratio, but the dye’s wet fastness in the unfixed state is limited. A cationic fixative applied at 2–4% on weight of fiber for 30 min at 40–60°C and pH 5–6 improves wash fastness by one to two grey scale steps under ISO 105-C10, while slightly reducing lightfastness under ISO 105-B02. Fixative selection must avoid amine-based formaldehyde donors if the finished textile is destined for formaldehyde-sensitive markets; non-formaldehyde polymer fixatives are preferred. Unfixed Direct Orange S can exhibit dry crockfastness of 3–4 and wet crockfastness of 2 under ISO 105-X12 before aftertreatment. Aftertreatment improves wet crock ratings but may stiffen hand and reduce sewability, which should be assessed with needle-force measurements on a laboratory overlock machine. The operational boundary for knit goods is that depths above 2.5% on weight of fiber show diminishing fixation efficiency and higher unfixed dye in effluent; such depths require longer rinsing and a separate post-treatment bath to avoid crocking failure on dyed-to-match finished goods. Batch-to-batch differences in cotton maturity and wax content alter available hydrogen-bonding sites; pretreatment with pectinase or alkaline scouring should be standardised to a desired weight loss of 3–6% before dyeing.
The principal difference between Direct Orange S and reactive orange chemistries is fixation mechanism. Reactive dyes form covalent bonds with cellulose under alkaline conditions at pH 10.5–11.5 and require wash-off at 60–95°C to remove hydrolysed dye. Direct Orange S remains physically adsorbed on cellulose and can be applied at neutral-to-weakly alkaline pH 7–8. The trade-off is wet fastness: under ISO 105-C10, many reactive oranges show ratings of 4–5 at 1/1 standard depth, whereas Direct Orange S in the unfixed state is generally rated 2–3. Compared with acid dyes such as C.I. Acid Orange 7, Direct Orange S has affinity for cellulose and is not exhausted onto protein or polyamide from a strongly acidic bath; acid dyes typically require pH 4–5 and are unsuitable for cotton. Direct Orange S also differs from solvent-soluble orange colorants in that it is not suitable for polyolefin or plasticised PVC without a dispersing or keying system. The product’s water solubility makes it simpler to strip than reactive or vat dyes: alkaline reduction or hypochlorite treatments remove a large fraction of unfixed dye, but the same solubility increases effluent colour load and requires compliance with discharge limits for colour units.
| Parameter | Direct Orange S (C.I. Direct Orange 26) | Reactive orange reference | C.I. Acid Orange 7 reference |
|---|---|---|---|
| Primary substrate | Cotton, viscose, paper, leather | Cotton, regenerated cellulose | Wool, silk, nylon |
| Fixation mechanism | Physical adsorption, hydrogen bonding | Covalent bond under alkali | Ionic bond, acid bath |
| Application pH | 7–8 | 10.5–11.5 fixation; 6–7 neutralisation | 4–5 |
| Wash fastness ISO 105-C10 | 2–3 unfixed; 3–4 after fixative | 4–5 | 2–3 on wool |
| Light fastness ISO 105-B02 | 2–3 | 5–6 | 2–3 |
| Migration/leveling | Moderate | Lower after alkali fixation | High |
| Stripability | Readily stripped | Difficult after fixation | Moderate |
Effluent streams from Direct Orange S application contain unexhausted dye, salt, and fixing-agent residues. The colour unit at discharge can be reduced by adsorption on activated carbon or Fenton oxidation, but sulfonated azo dye degradation products require monitoring for aromatic amines under the purchaser’s wastewater permit conditions. Direct Orange S should not be premixed with cationic fixatives or cationic softeners in the same bath, because precipitation occurs even at low concentrations; separate baths and intermediate rinsing are required. Strong reducing agents such as sodium hydrosulfite destroy the azo chromophore and are used for stripping, but residual reducing agent must be fully rinsed before redyeing to avoid shade instability. Storage in unopened containers at 10–30°C and relative humidity below 60% prevents caking; aged lots should be restandardised against reference before use. Published data for the exact unfixed fraction of Direct Orange S in continuous pad-steam configurations is limited; mills should establish process-specific effluent correlation through daily absorbance sampling rather than relying on generic direct-dye emission factors.
When Direct Orange S is blended with direct yellow and direct black or grey components, the shade at 2–4% total depth may be highly sensitive to batch-to-batch strength variation in the orange component. A strength deviation of ±3% can shift the CMC ΔE by more than 0.5 under D65 illumination in ternary brown shades; therefore mill laboratories commonly pre-dispense Direct Orange S from sealed bins with 0.1 g balance accuracy. In heavy-depth black formulations, the orange component is often limited to 0.2–0.8% on weight of fiber to avoid a reddish flare under tungsten lighting. Direct Orange S can exhibit metamerism against reactive orange references under store lighting; shade approval should include measurements under D65, TL84, and A light sources using a bench-top spectrophotometer with specular reflection included.
Stock solution preparation has a direct effect on shade reproducibility. Direct Orange S powder should be pasted with cold demineralised water before hot water at 70–80°C is added, then stirred for 10–15 min. Filtration through a 25 μm or 50 μm screen removes undissolved standardising diluents that could block dosing valves. Stock solutions at 10 g/L are commonly held for 48 h at 5–30°C; longer holding can allow microbial growth in non-preserved liquors, producing reducing conditions that degrade the azo chromophore. In automated dispensing, gravimetric or volumetric dosing pumps should be calibrated with 0.1% repeatability; a drift above 0.5% of target weight per day produces visible batch-to-batch shade differences in pale depths. Spectrophotometric control of dyebaths uses 10 mm flow-through cells and absorbance calibration curves prepared in the linear range; a correlation coefficient below 0.999 invalidates the curve for production use. Batch corrections should be limited to 0.2% on weight of fiber per addition cycle because the direct dye’s leveling behaviour cannot compensate for large salt-split corrections.
A key difference between Direct Orange S and other direct orange dyes is the level of salt sensitivity. Some direct orange products shift hue at high electrolyte concentrations due to aggregation, whereas Direct Orange S retains a more stable hue under salt addition at 5–30 g/L sodium sulfate when dosed gradually. The shade on cotton is also affected by aftertreatment: cationic fixatives can cause a redder or duller cast; therefore production approval must evaluate the final shade after fixation rather than the unfixed dyeing. Compared with direct oranges that are copper-complexed or resin-bonded, Direct Orange S generally has lower lightfastness under ISO 105-B02 but produces a cleaner shade and is easier to strip. Published colour-fastness data for the exact commercial blend varies among suppliers; a mill-specific fastness trial at 1/1 standard depth is required before adoption.
Operational boundaries include incompatibility with strong oxidising agents, which can oxidize the azo linkage and weaken shade, and with cationic materials in the same bath. Direct Orange S is not suitable for continuous dyeing with high-concentration sodium hypochlorite in the same line because residual hypochlorite can fade the shade within minutes. In storage, keep the product away from moisture and direct sunlight; use sealed stainless steel or lined mild steel containers. The product should be restandardised at least every 12 months when stored in opened containers.