| HS Code | 509907 |
| Product Name | Papermaking Dye Domestic Special Grade |
| Appearance | uniform powder or granule |
| Color Shade | as per specified standard color |
| Solubility In Water | soluble in water forming clear solution |
| Ph Value 1 Percent Solution | 6.5 to 8.5 |
| Dyeing Strength | 100% ± 3% relative to standard sample |
| Moisture Content | ≤ 5% |
| Water Insoluble Matter | ≤ 1% |
| Fineness Through 100 Mesh | ≥ 95% |
| Light Fastness | grade 4 to 5 |
| Acid Resistance | stable in pH 3 to 6 |
| Alkali Resistance | stable in pH 8 to 11 |
As an accredited Papermaking Dye Domestic Special Grade factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaged in 25 kg lined woven bags with moisture-proof barrier, ensuring safe handling and reliable papermaking dye performance. |
| Container Loading (20′ FCL) | 20′ FCL shipment of Papermaking Dye Domestic Special Grade, loaded securely in drums/IBCs, palletized, and containerized for safe transport. |
| Shipping | Papermaking Dye Domestic Special Grade ships in sealed, leak-proof drums or bags to prevent moisture contamination and spillage. Use dry, ventilated transport away from incompatible materials. Avoid extreme heat or direct sunlight. Proper labeling, secure loading, and safe handling procedures ensure product integrity and regulatory compliance throughout domestic delivery. |
| Storage | Store in a cool, dry, well-ventilated area away from direct sunlight and moisture. Keep containers tightly sealed when not in use. Avoid contact with oxidizing agents, acids, or alkalis. Maintain stable temperatures, and ensure the storage area is clearly labeled, inaccessible to unauthorized personnel, and equipped for spill containment. |
| Shelf Life | Shelf life is typically 2 years when stored unopened, sealed, in a cool, dry place away from direct sunlight. |
In tissue converting lines producing facial and napkin grades from virgin bleached kraft, addition of the domestic special grade dye into the machine chest occurs only after furnish pH has been stabilized between 4.5 and 6.5; stock temperatures above 55°C at the drying hood can reduce direct dye substantivity and produce shade drift between the wet end and the parent reel. For napkins and towels intended for direct food contact, compliance is established under FDA 21 CFR 176.170 and EU 1935/2004 Article 3.1(a), with colour-fastness validated according to EN 646:2019; where the grade is marketed in China, GB 4806.8-2022 may additionally require sensory and migration testing. Typical addition rates for pastel facial grades fall between 0.005% and 0.05% on bone-dry fiber, while printed napkin backings and deep-shade paper towels require 0.08% to 0.10% at the machine chest, not at the suction breast roll, to avoid asymmetric colour development. The downstream process is stock dyeing followed by high-consistency dilution, forming on a crescent former or twin-wire tissue machine, and drying on a Yankee cylinder; retention is controlled with 0.01%–0.03% cationic polyacrylamide added after the fan pump. A production-scale failure mode observed at these addition levels is intermittent dye transfer to the wet felt and build-up on the creping doctor blade, which increases sheet breaks when the dye load exceeds 0.10% and the anionic charge load in the thin stock begins to destabilize the furnish. Terminal finished product types in this segment include facial tissue, printed napkins, kitchen towels, toilet paper, and disposable wiping grades.
Recycled board mills running mixed waste furnish encounter a retention conflict that is not present in virgin-fiber systems: cationic retention aids are consumed by dissolved colloidal anionic trash before they can fix the dye, so the dye addition point must be shifted from the pulper to the post-dispersion thick-stock line where the interfering load has been partially neutralized. Compliance for colored packaging board is established under EU 94/62/EC with the combined heavy metal concentration of lead, cadmium, mercury, and hexavalent chromium limited to 100 mg/kg, supplemented by REACH Annex XVII substance restrictions when the board is placed on the EU market. For folding cartons that contact dry food, FDA 21 CFR 176.170 and EU 1935/2004 Article 3.1(a) apply, and migration resistance is verified according to EN 646:2019. Formulation addition rates range from 0.02% to 0.20% on bone-dry fiber, with 0.12% typical for greyback duplex board; exceeding 0.20% increases dye loss to the white top layer and raises chemical oxygen demand in the broke pulper, extending recirculation time. Downstream production consists of stock dyeing after thermal dispersion, dilution, forming on a twin-wire machine, and surface sizing where required. Retention is controlled with a dual CPAM/bentonite system at 0.02% and 0.03% respectively, maintaining a zeta potential window between −18 mV and −22 mV on the wet stock. Terminal product types produced from this process include greyback duplex board, folding cartons, book cover stock, and high-bulk display board.
On high-brightness copy paper lines, the dye is injected at the fan pump as a 0.1% aqueous solution at 20–150 ppm on dry fiber, where it adjusts CIELAB b* values toward the blue-violet range to compensate for yellowness from mechanical pulp or starch; compliance testing references ISO 11475:2017 CIE whiteness under D65/10° and ISO 2470-1:2016 diffuse blue reflectance factor. The downstream route is thin-stock tinting, dewatering on a gap former, and surface sizing; online colour spectrophotometer closed-loop control is used to prevent two-sidedness at the reel when the addition exceeds 150 ppm. Terminal products include copy paper, continuous forms, offset printing paper, and envelope stock. Overdosing beyond 200 ppm creates a grey cast and reduces optical brightener response due to ultraviolet-spectrum competition, so the upper dosing boundary is treated as a process limit rather than a shade adjustment range.
| Standard/regulation | Scope | Typical test/limit | Applied to |
|---|---|---|---|
| FDA 21 CFR 176.170 | Paper and paperboard in contact with aqueous and fatty foods | Component review and migration under intended use | Napkins, food trays, folding cartons |
| EU 1935/2004 Article 3.1(a) | Food-contact materials placed on EU market | No constituent transfer endangering health | Napkins, food trays, folding cartons |
| EN 646:2019 | Colour fastness of dyed paper and board intended for food contact | Visual staining assessment after contact with white felt | All food-contact coloured grades |
| GB 4806.8-2022 | China food-contact paper and board | Sensory and migration testing | Export food-contact trays, napkins |
| EU 94/62/EC | Packaging and packaging waste | Heavy metals sum Pb, Cd, Hg, Cr(VI) < 100 mg/kg | Coloured packaging board, trays |
Laminating-grade base paper produced for high-pressure laminate pressing imposes two simultaneous demands on the dye: survival through melamine-formaldehyde saturation at 60%–65% resin solids and no colour transfer during hot pressing at 140°C–150°C and 7–9 MPa. The governing conformance path for the finished laminate includes EN 438-3:2016 and light-fastness testing according to ISO 4892-2:2013 or ISO 105-B02; where blue wool scale ratings of 7 or higher are specified, published data for this specific configuration is limited and mill validation is required. Formulation addition ratio ranges from 0.10% to 0.50% on bone-dry fiber, with the higher values reserved for black and high-contrast décor papers. In downstream production, dye is added to the thick stock after refining, the paper is formed on an inclined-wire machine, and the sheet is impregnated with melamine-formaldehyde resin before being pressed into high-pressure laminate or low-pressure laminate boards. Operational constraints include softened-water dilution when calcium carbonate equivalent hardness exceeds 150 mg/L; dye precipitation in the saturation bath and migration to the press plate have been observed when stock hardness is uncontrolled and the addition ratio is above 0.40%. Terminal products for coloured decor paper are high-pressure laminate sheets, compact boards, edge banding, and decorative surface papers for furniture and flooring.
| Application segment | Addition ratio (% on dry fiber) | Stock pH window | Retention/charge-control system | Primary process limit |
|---|---|---|---|---|
| Tissue and napkin | 0.005–0.10 | 4.5–6.5 | CPAM 0.01–0.03% | Felt staining above 0.10% |
| Recycled folding board | 0.02–0.20 | 6.0–7.2 | CPAM/bentonite dual retention | Anionic trash above 1,200 mg/L COD |
| Printing and writing tinting | 0.002–0.015 | 5.5–7.0 | No retention aid; fan-pump injection | Two-sidedness above 150 ppm |
| Decorative laminate base | 0.10–0.50 | 5.0–6.5 | Cationic wet-strength resin and PAC | Press-plate migration above 0.40% |
When pulp slurry is vacuum-formed into coloured food trays, the dye partitions between fiber surfaces, dissolved polymer in the white water, and the hot-press drainage stream; this partition determines both colour yield and migration risk in the finished moulded pulp. Compliance is evaluated under FDA 21 CFR 176.170, EU 1935/2004 Article 3.1(a), EN 646:2019, and GB 4806.8-2022 for relevant export destinations, while packaging waste requirements under EU 94/62/EC apply to the finished tray as a packaging article. Addition ratio ranges from 0.02% to 0.10% on dry fiber for saturated colours, while pastel tray bodies require only 0.005%–0.02% due to the high surface reflectance of bleached recycled fiber. The downstream process includes batch dyeing in the hydropulper, vacuum forming on porous moulds, and hot pressing at 150°C–170°C for 10–20 seconds; polyaluminium chloride is added at 0.05%–0.10% to reduce anionic charge interference and retain dye during high-dilution drainage. Production-scale limits appear in high-fat food applications, where extraction under fatty simulants may exceed aqueous simulant values; mills without fatty-simulant migration data for this specific configuration should segregate those orders and validate batch-to-batch consistency. Terminal product types include coloured food trays, plates, clamshells, cup carriers, and egg cartons.
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Papermaking Dye Domestic Special Grade is supplied as a spray-dried direct dye formulation under model designation PD-DSG-301. The product is based on a disazo anionic chromophore and is intended for wet-end addition in unbleached and recycled fiber furnishes, including old corrugated containers, bleached chemical pulp, and high-yield mechanical pulp. Typical physical presentation consists of dark blue free-flowing granules with a bulk density of 0.55 to 0.75 g/cm³ after 100 taps. Moisture content is controlled to ≤8.0% by the method described in ISO 787-2, and sieve residue on a 45 µm screen is maintained below 0.1% when tested according to ISO 787-7. The pH of a 1.0% aqueous solution at 25 °C falls between 6.5 and 8.0 under the condition given in ISO 787-9. The product’s water solubility is specified as ≥95% in a 5.0 wt% solution at 50 °C after 30 min of low-shear mixing in a planetary mixer operating at 50 rpm. The reduced electrolyte carry-over target is ≤2.5 wt% sodium sulfate, which limits white-water conductivity increase during closed-loop operation, as measured by ASTM D1125-23 in a 2.0% solution.
| Parameter | Method / standard | Limit / range | Unit |
|---|---|---|---|
| Moisture content | ISO 787-2 | ≤8.0 | % |
| Sieve residue on 45 µm | ISO 787-7 | ≤0.1 | % |
| pH of 1.0% aqueous solution | ISO 787-9 | 6.5–8.0 | — |
| Bulk density after 100 taps | ISO 787-11 | 0.55–0.75 | g/cm³ |
| Water solubility at 50 °C, 5.0 wt% | In-house filtration, 45 µm screen | ≥95 | % |
| Soluble sulfate as sodium sulfate | ISO 787-13 | ≤2.5 | wt% |
| Heavy metals – Pb | ICP-MS after acid digestion | ≤5 | mg/kg |
| Heavy metals – Cd | ICP-MS after acid digestion | ≤2 | mg/kg |
| Heavy metals – Hg | ICP-MS after acid digestion | ≤3 | mg/kg |
| Heavy metals – As | ICP-MS after acid digestion | ≤10 | mg/kg |
Wet-end addition of PD-DSG-301 is typically performed at 0.05% to 0.40% on oven-dry fiber mass. The dye stock solution is prepared at 2.0 to 5.0 wt% using water at 40 to 50 °C; dissolution below 40 °C increases the risk of undissolved aggregates, while prolonged heating above 60 °C accelerates thermal degradation of the disazo chromophore and causes shade drift. The preferred injection point is the suction side of the fan pump, after the cleaner system and before the headbox screen, to limit residence time in the presence of cationic retention aid. In a typical 120 g/m² testliner furnish containing 70% OCC and 30% bleached kraft, dye addition at 0.25% increases colour strength to a reflectance-based target of 42% to 46% absolute at 460 nm after handsheet preparation according to ISO 5269-2. Colour strength is evaluated from spectral reflectance using ISO 5631-1; brightness and shade reversion are monitored by ISO 2470-1 and ISO 5631-1. Dye fixation efficiency, measured as the difference between headbox and tray water soluble dye concentration divided by headbox concentration, was recorded at 0.89 in a single production-scale observation on a 4.8 m fourdrinier producing white-top liner. Published data for this exact closed-loop configuration is limited; the stated value is representative of one production trial and should be verified on-site.
At pH below 4.5, aluminum sulfate present above 0.3 kg/t promotes direct dye precipitation as a dye-alum lake, increasing two-sidedness and reducing retention by up to 10 percentage points. At pH above 8.0, anionic fibre surfaces become more negative, and dye retention decreases unless a cationic fixative is applied after dye injection. When white-water conductivity exceeded 3.5 mS/cm, the same fixation efficiency dropped from 0.89 to 0.71. The product should therefore not be applied to systems operating above 3.5 mS/cm without dilution or bleed. Conductivity is determined by ASTM D1125-23 on filtered white-water samples at 25 °C. The addition sequence should maintain at least 20 s between dye and cationic polyamine retention aid; simultaneous injection in a common line can form sticky deposits on pressure screen baskets and reduces first-pass retention of the dye by 15% to 25% as measured by filtrate colour intensity using ISO 5631-1.
For white-top linerboard, dye addition is commonly split between the top ply and the base ply. The top-ply dosage is 0.20% to 0.35% on dry fibre, while the base ply receives 0.05% to 0.10% to mask greyness from OCC. In tissue grades dyed pastel shades, addition is limited to 0.02% to 0.08% because optical brighteners and cationic softeners compete for fibre surface sites. At tissue addition levels above 0.08%, wet-migration into the Yankee coating can occur, producing visible shade transfer on the doctor blade and reducing crepe uniformity. The dye should be added after any wet-end starch but before the headbox, with 10 to 15 s of line mixing at a line velocity of 2.0 m/s to disperse the stock solution uniformly without excessive shear.
Direct comparison with imported direct dye grades used in the same OCC furnish reveals three operationally relevant deviations. The domestic special grade is supplied with a narrower moisture specification of ≤8.0% versus ≤10.0% for the imported benchmark, which reduces metering weight drift in humid packaging areas. The electrolyte carry-over is set at ≤2.5 wt% sodium sulfate, while imported grades in the same colour index class often carry 6.0 to 8.0 wt%. That difference has a measurable effect on closed white-water conductivity: in a laboratory recirculation study using a retention aid at 0.4 kg/t, the domestic grade raised conductivity by 0.8 mS/cm after 6 cycles, whereas the imported grade raised it by 1.7 mS/cm under identical conditions. The third difference is the dissolution temperature threshold; the domestic special grade dissolves to 95% at 40 °C, whereas the imported benchmark requires 60 °C for the same dissolution yield, which affects steam use in stock preparation. Compared with domestic general-grade direct dyes, PD-DSG-301 has lower filler sensitivity: brightness loss on a filled sheet at 10% precipitated calcium carbonate was 0.6 points on ISO 2470-1 for the special grade, while the general grade lost 1.4 points. Shade deviation under varying freeness from 350 to 550 mL CSF per ISO 5267-1 was ΔEab 1.2 for PD-DSG-301, compared with ΔEab 2.6 for the general grade.
| Parameter | PD-DSG-301 | Imported direct dye | Domestic general grade |
|---|---|---|---|
| Moisture content | ≤8.0% | ≤10.0% | ≤9.0% |
| Sodium sulfate carry-over | ≤2.5 wt% | 6.0–8.0 wt% | 4.0–5.5 wt% |
| Dissolution to 95% | 40 °C | 60 °C | 45 °C |
| White-water conductivity increase after 6 recirculation cycles | 0.8 mS/cm | 1.7 mS/cm | 1.1 mS/cm |
| Brightness loss at 10% PCC filler | 0.6 points | 0.8 points | 1.4 points |
| Shade deviation across 350–550 mL CSF | ΔEab 1.2 | ΔEab 1.5 | ΔEab 2.6 |
In closed white-water loops operating above 3.5 mS/cm, the product’s low electrolyte design mitigates but does not eliminate dye retention loss. Conductivity excursions above 3.5 mS/cm typically arise from high levels of sulfate and chloride in recycled furnish or from wet-end mineral fillers. At 4.0 mS/cm, headbox to tray dye retention decreased to 0.66 in the production trial described above. At 5.0 mS/cm, dye mottling appeared on the fabric side of a 160 g/m² white-top liner, with shade variation of ΔEab 2.1 measured according to ISO 5631-1 across the cross-direction. The operational countermeasure is a partial white-water bleed of 8% to 12% by volume or the addition of process water with conductivity below 1.0 mS/cm to bring the tray water within the target window. If bleed is not possible, dye dosage should be reduced by 0.05 percentage points for every 1.0 mS/cm increase above 3.5 mS/cm, based on linear regression of retention data. However, published data for this specific dosage compensation is limited; mills should confirm with a headbox-to-tray dye audit.
Closed-loop operation also concentrates suspended solids and anionic trash. Cationic demand of the thick stock after chest dilution should be measured with a particle charge detector and kept below 0.8 meq/L before the dye feed point. Above this value, the anionic dye competes with dissolved colloidal material for cationic retention aids and shade variation increases. A polyamine fixative can be applied, but only after a residence delay of at least 20 s following dye injection. Simultaneous addition of dye and polyamine at the same feed pipe was observed to form a gel-like deposit on a 0.25 mm slotted pressure screen, raising differential pressure by 12 kPa over 8 h in a trial on a 2.8 m gap former. This is an operational boundary for the product.
For food-contact paper grades, the compliance boundary is set at 0.25% on oven-dry fibre. At or below this addition level, the product is documented to comply with FDA 21 CFR 176.170 for aqueous and fatty food types when extracted according to EN 645 and EN 647. Above 0.25%, end-use migration testing is required because the disazo chromophore may exceed organoleptic thresholds in fatty food simulants. The product contains no listed SVHC above 0.1 wt% under REACH, as declared in the safety data sheet and based on a compositional audit against the candidate list. Heavy-metal content is controlled to ≤5 mg/kg lead, ≤2 mg/kg cadmium, ≤3 mg/kg mercury, and ≤10 mg/kg arsenic when analysed by inductively coupled plasma–mass spectrometry after acid digestion. These values are supported by a type test certificate and are not repeated as batch certificate items. For paper and board intended for dry food contact, compliance with EN 646 is verified at the accepted addition level. For packaging grades not intended for food contact, the product is suitable for use under standard finished paper oxidation and content criteria, provided that the dye addition does not exceed 0.40% and the final sheet is tested for extractable colour under EN 645.
Storage life is limited by humidity uptake and thermal exposure. Unopened bags stored at 10 to 30 °C and relative humidity below 60% are specified for 24 months. When relative humidity exceeds 60%, the granules absorb moisture and form aggregates; pre-drying in a desiccant-air silo at 35 °C for 2 h is then required before metering. The product is incompatible with strong oxidizing agents, including hypochlorite bleach liquors, and with high-charge cationic polyamines when both are introduced without the stated 20 s residence delay. Avoid preparing dye stock solutions in alkaline borate buffers above pH 9.0, because hydrolysis of the disazo linkage may occur after 6 h at 50 °C, producing shade loss and measurable release of aromatic amines in the mill effluent according to ISO 11350. The working solution should be used within 8 h when prepared at 50 °C, and within 24 h when prepared at 25 °C. Batch-to-batch colour strength is controlled to ±2.0% relative to the certified reference by ISO 5631-1, which permits direct metering without intermediate re-shading at addition levels below 0.25%.
In mills using white-water reuse for stock dilution, the dye concentration in tray water should be monitored at 460 nm after filtration through a 0.45 µm membrane. Absorbance values above 0.12 at 10 mm path length indicate incomplete fixation and a need to reposition the dye feed upstream or to reduce retention aid conflict. This method is not a substitute for standard colour measurement but serves as a rapid on-line check. The product’s granular form generates ≤0.5 mg/m³ respirable dust when transferred at 0.5 m/s vacuum conveying velocity in a contained charging station, measured by gravimetric sampling according to EN 481; local exhaust ventilation should be used to maintain the workplace limit value for inert dust of 10 mg/m³ as a total inhalable fraction.