| HS Code | 591380 |
| Productname | Lithol Rubine 4BPG |
| Colorindexname | Pigment Red 57:1 |
| Colorindexnumber | C.I. 15850:1 |
| Chemicalclass | Monoazo lake pigment |
| Lakemetal | Calcium |
| Physicalform | Powder |
| Colorshade | Blue-shade red |
| Specificgravity | 1.8-1.9 |
| Oilabsorption | 45-55 g/100 g |
| Ph | 7-9 |
| Moisturecontent | ≤1.0% |
| Watersolublematter | ≤1.0% |
| Tintingstrength | 100% standard |
| Lightfastness | Good |
| Heatresistance | 180-200 °C |
| Acidresistance | Good |
| Alkaliresistance | Poor to moderate |
| Mainapplication | Printing inks, paints, plastics |
As an accredited Lithol Rubine 4BPG factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Lithol Rubine 4BPG packaging consists of 25 kg net multiwall paper bags, palletized and shrink-wrapped for transport. |
| Container Loading (20′ FCL) | A 20′ FCL container loaded with palletized Lithol Rubine 4BPG, properly secured, kept dry, and compliant with chemical shipping regulations. |
| Shipping | Ship Lithol Rubine 4BPG as a non-hazardous pigment in moisture-resistant, sealed containers, protected from heat, sunlight, and contamination. It typically has no UN number or transport hazard class; verify the current SDS and applicable ADR/IMDG/IATA/local rules before dispatch. |
| Storage | Store Lithol Rubine 4BPG in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and ignition sources. Keep containers tightly closed and clearly labeled. Prevent dust generation and contact with strong oxidizing agents. Separate from food, feed, and drinking water. Use appropriate personal protective equipment when handling. Maintain good housekeeping and follow local regulations. |
| Shelf Life | Stored sealed in a cool, dry, dark place, Lithol Rubine 4BPG typically has a shelf life of approximately three to five years. |
Lithol Rubine 4BPG (C.I. Pigment Red 57:1, CAS 5281-04-9) is dispersed in oxidation-drying sheet-fed offset inks at pigment loadings of 15–20 wt% of the finished ink. The mill base is processed through three-roll mills with front-roll temperatures of 35–40°C and hydraulic nip pressures of 0.8–1.2 MPa, followed by let-down to press tack; fineness is held at ≤ 10 µm on a Hegman gauge per ISO 1524. Tack remains between 8 and 12 Inkometer units at 30°C and 400 rpm under ASTM D4361. Loadings above 20 wt% raise tack beyond the specified ceiling and correlate with picking on uncoated board at press speeds above 12,000 sheets/h. The sulfonated calcium lake is alkali-sensitive: when fountain solution pH exceeds 7.0, bleed becomes measurable by contacting printed strips with wetted paper under a 1 kg load for 24 h per ISO 2836. Production presses therefore hold fountain solution pH at 4.8–5.5 and conductivity at 800–1,200 µS/cm. Water pickup is limited to 20–35% emulsion volume per ASTM D4942; above this range, dry-print density decreases by more than 0.15 and tonal value increase moves outside the limits of ISO 12647-2. Because the pigment does not meet the process-magenta coloristic requirements of ISO 2846-2, it is specified for spot red, warm red, and maroon packaging inks. Terminal products include folding cartons, paper carrier bags, coated cover stock, and greeting cards with post-print aqueous coating or UV varnish to reduce rub transfer.
Solvent-based flexographic inks built on nitrocellulose/polyurethane binders accept Lithol Rubine 4BPG at 10–14 wt% of press-ready ink. Mill-base dispersion is executed in horizontal bead mills charged with 0.6–0.8 mm yttrium-stabilized zirconia beads at tip speeds of 8–12 m/s; the mill base carries 25–30 wt% pigment before reduction. Press-ready fineness is held below 5 µm per ISO 1524, because larger particles cause doctor-blade streaking in gravure and anilox wear in flexo. Ink viscosity is maintained at 18–25 s DIN 4 mm at 25°C per ISO 2431, either by periodic cup checks or by automated solvent addition on wide-web presses. The reduction blend contains n-propyl acetate, ethanol, and ethyl acetate; ester content above 40% at sustained ink-pan temperatures above 30°C induces plate-out of the calcium lake after roughly 6–8 h of continuous running. Corona-treated biaxially oriented polypropylene or polyethylene film is held at 38–42 mN/m wetting tension per ASTM D2578. Dried ink adhesion is evaluated by tape pull per ASTM D3359 method B, with no more than 5% removal of the printed image. In extrusion-laminated structures, retained solvent measured by headspace gas chromatography per ISO 11890-2 must remain at ≤ 5 mg/m² before lamination; higher levels reduce laminate bond strength below 2.0 N/15 mm in T-peel testing per ASTM F904. Because the pigment is a sulfonated azo lake, direct food-contact positions are avoided unless a functional barrier is validated by migration testing under EU Regulation (EC) No 1935/2004. Finished materials include snack-food wrapper outer webs, soap label film, bouquet wrap, and paper-based ice-cream pouches in non-contact layers.
High-load polyolefin masterbatches of Lithol Rubine 4BPG are produced at pigment loadings of 30–40 wt% in an LDPE carrier with a melt mass-flow rate of 20 g/10 min at 190°C under 2.16 kg per ISO 1133-1. Compounding is carried out on co-rotating twin-screw extruders with L/D 40 and screw diameter 50–75 mm; barrel profiles move from 160°C at the feed throat to 190–200°C at the die, with screw speeds of 400–650 rpm and specific energy input of 0.18–0.25 kWh/kg. Melt filtration uses a 100/200/100 mesh screen pack, and pre-screen pressure is held between 60 and 120 bar. A pressure rise above 2 bar/h during a run indicates incomplete dispersion or screen blinding and requires higher shear, lower throughput, or vent maintenance. The pigment’s thermal boundary appears at this stage: production records show that extended residence above 200°C shifts the shade yellower and reduces the red CIELAB a* value by 0.5–1.0 on standard injection-molded PP plaques. Let-down into polypropylene is performed at 2–4 parts masterbatch per 100 parts resin, yielding 0.6–1.2 wt% pigment in the final part. Dispersion quality in blown film is checked by screen-pack pressure rise on a 200-mesh breaker and by speck counting on 50 µm film; acceptable production film contains fewer than 5 specks larger than 20 µm per 100 cm². Controlled injection-molding trials show that fill speeds above 200 mm/s can induce gate blush and streaking at pigment loadings above 1.2 wt% in polypropylene homopolymer with a melt flow rate of 12 g/10 min per ISO 1133-1. The pigment is not specified for thin-wall food-contact packaging processed above 220°C, where degradation and migration risk move outside normal converter limits.
Calendered and plastisol PVC convert Lithol Rubine 4BPG primarily as a pre-dispersed paste in DINP at 10–15 wt% pigment, not as dry powder. Plastisol batches hold Brookfield RVF viscosity between 2,500 and 4,500 mPa·s at 25°C with spindle 4 at 20 rpm; the paste is added during low-speed let-down to avoid shear exotherm above 35°C, which destabilizes the sulfonated lake. Fusion proceeds in a Mathis oven at 190°C for 60 s or on calendar rolls at 150–170°C with dwell time not exceeding 90 s. The pigment shows a plasticizer-bleed boundary at 1.0 wt% in a 50 phr DINP-plasticized PVC film: compression blotting against white plasticized PVC under 5 kPa at 70°C for 24 h produces visible transfer above that loading, while lower loadings remain below the visual threshold. This limit defines the operational window for marbled sheet, upholstery film, and indoor decorative wall covering. Because C.I. Pigment Red 57:1 has limited lightfastness in reduced tint, service is restricted to indoor applications; xenon-arc exposure of a 1:10 TiO₂ reduction per ISO 4892-2 shows pronounced fading before 300 h. The pigment is therefore not recommended for outdoor membrane, automotive interior skins, or window profiles. Terminal products include stationery covers, vinyl tablecloth base film, bookbinding foil, and decorative piping for non-food contact end uses.
Polyester/epoxy hybrid powder coatings formulated with Lithol Rubine 4BPG at 2–4 wt% require a narrow cure-window discipline. Premix extrusion runs on a co-rotating twin-screw extruder at 90–110°C with residence time below 60 s; melt temperatures above 110°C initiate a measurable shift toward a yellower red. The cooled extrudate is milled in an air classifying mill at rotor speeds of 4,000–6,000 rpm, targeting a D50 of 30–40 µm by laser diffraction per ISO 13320. Application to cold-rolled steel or aluminum uses corona or tribo guns at film builds of 60–80 µm. Cure schedules of 180°C for 15 min or 200°C for 10 min are standard; overbake at 200°C for 20 min must be validated by ΔE measurement per ISO 7724-3 against a retained panel, because the calcium lake loses red chroma in reduced tint. Gloss at 60° incidence per ISO 2813 is specified above 85 gloss units; a D50 above 50 µm lowers gloss below 80 gloss units and increases orange peel. Acid value of the hybrid resin is maintained between 70 and 80 mg KOH/g, because residual carboxyl content in the cured matrix influences surface bronzing of the pigment. The application is limited to indoor decorative hardware, lighting fixtures, and metal furniture; outdoor architectural exposure is excluded.
Neutral-pH aqueous graphic arts dispersions represent a restricted but relevant use for Lithol Rubine 4BPG. The pigment is dispersed in styrene-acrylic solution or emulsion resins at 12–18 wt% with dispersant demand of 8–12% active on pigment weight; the premix is processed in a vertical bead mill using 0.8–1.0 mm zirconia-silica beads to a fineness below 5 µm per ISO 1524. pH is deliberately held at 6.8–7.5; if pH rises above 8.0, the calcium lake bleeds into the vehicle and stains unprinted areas in wet-stack tests. Final flexographic inks run at 25–35 s with a #2 Zahn cup per ASTM D4212, and drying in high-velocity hot-air dryers at 60–80°C and 2–5 m/s supports print speeds of 100–200 m/min on tissue and coated paper. Rub resistance is measured on a Sutherland rub tester per ASTM D5264 with a 4 lb weight for 100 cycles; acceptable transferred ink area is below 10%. The pigment is used for paper napkins, tissue, gift wrap, and paper bags, but it is not specified for outdoor signage because xenon-arc exposure per ISO 4892-2 shows unacceptable fading in pale tints.
Cosmetic use of Lithol Rubine 4BPG corresponds to D&C Red No. 7 in the United States and CI 15850:1 in the EU. The pigment is dispersed in castor oil or ester-based emollients at 10–20 wt% for lipstick and cream blush; triple-roll milling at nip pressures of 0.5 MPa produces fineness below 15 µm per ISO 1524. For nail lacquer, the lake is predispersed in butyl acetate/ethyl acetate solvent systems with nitrocellulose resin to avoid visible streaking at 1–3 wt% pigment in the finished lacquer. Batch certification requirements under 21 CFR 74.1307 include trace-metal control; typical certificate-of-analysis limits are Pb ≤ 20 ppm, As ≤ 3 ppm, and Hg ≤ 1 ppm by ICP-MS per USP <233>. The EU status under Regulation (EC) No 1223/2009 Annex IV must be confirmed for the exact product category and maximum concentration, since Annex IV entries are amended periodically. The pigment is not permitted in all cosmetic areas; eye-area restrictions and mucous-membrane restrictions vary by jurisdiction and require a finished-product safety assessment.
| Regulatory reference | Listing | Key limit / scope | Test method |
|---|---|---|---|
| 21 CFR 74.1307 | D&C Red No. 7 (CI 15850:1) | Pb ≤ 20 ppm; As ≤ 3 ppm; Hg ≤ 1 ppm | USP <233> ICP-MS |
| Annex IV of Regulation (EC) No 1223/2009 | CI 15850:1 | Product-category specific; verify current Annex IV entry | Cosmetic product safety assessment |
| REACH Annex XVII entry 43 | Azo colorant restriction | No restricted aromatic amine above 30 ppm | Reductive cleavage GC-MS |
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Lithol Rubine 4BPG is supplied as a blue-shade calcium monoazo lake pigment conforming to C.I. Pigment Red 57:1 and CAS 5281-04-9. The pigment belongs to the β-oxynaphthoic acid (BONA) lake class and is manufactured as a low-dusting powder with specific gravity 1.55–1.65 when tested according to ISO 787-10. Its colouristic position in a 1:5 TiO₂ reduction typically falls between a* 45–55 and b* −5 to 5 under D65/10° spectrophotometric conditions per ISO 13655-1:2009. The main application fields are sheetfed offset inks, solventborne lamination inks, masterbatches, and rigid PVC compounds processed below 200 °C. In comparison with uncoated PR57:1, the 4BPG surface-controlled grade is expected to show lower dusting and lower mill fines generation; as-received sieve residue on a 45 µm screen is typically ≤ 0.1 % by ISO 787-7. The product does not contain barium or titanium as deliberate constituents; calcium levels are typically 6.0–7.5 % by mass. Published data for this exact surface-treatment configuration is limited, and direct batch-certificate values should be confirmed with the supplier.
In solventborne lamination ink manufacture, volatile content and aqueous-extract pH are controlled because residual moisture above 2.0 % can alter nitrocellulose solution viscosity and promote cylinder corrosion in three-piece tinplate packaging. Table 1 lists the typical specification window for surface-treated PR57:1 grades; individual production lots should be verified against the supplier batch certificate.
| Parameter | Test method | Typical range |
|---|---|---|
| Volatile matter, 105 °C | ISO 787-2 | ≤ 2.0 % |
| Oil absorption | ISO 787-5 | 38–45 g/100g |
| pH of aqueous extract | ISO 787-9 | 7.0–8.5 |
| Sieve residue, 45 µm | ISO 787-7 | ≤ 0.1 % |
| Specific gravity | ISO 787-10 | 1.55–1.65 |
| Relative tinting strength | ISO 787-24 | 100 ± 3 % |
Oil absorption below 45 g/100g supports higher pigment loading in oxidation-drying sheetfed ink formulations without exceeding target flow curves. The aqueous-extract pH range of 7.0–8.5 buffers varnish acidity and reduces acid-catalyzed breakdown of alkyd ester linkages during storage at 40 °C. Varnishes with free acid above 25 mg KOH/g can destabilize the calcium lake and produce hard settlement during prolonged storage; production-scale experience recommends pre-testing such high-acid vehicles before full mill base release.
Dispersion of 4BPG in high-speed solventborne ink lines is typically performed with a Cowles-type dissolver at peripheral tip speed of 18–22 m/s before bead milling. In a vertical bead mill charged with 0.8 mm yttria-stabilized zirconia beads and operating at 12 m/s agitator speed, a 45 wt% pigment loading in a nitrocellulose/ethanol flexographic vehicle reaches a Hegman grind of 6.5 within 40 min. Production-scale observations show that reducing tip speed to 8 m/s during the pre-dispersion stage leaves oversized agglomerates that raise downstream filter pressure above 0.4 MPa after 30 min, a failure mode caused by incomplete wetting of the pigment surface. Conversely, extended milling beyond 90 min increases paste viscosity by more than 40 % as fresh surface area adsorbs vehicle resin. Batch-to-batch viscosity at 25 °C in a toluene/isopropanol resin system is therefore controlled between 80–120 mPa·s at D = 250 s⁻¹ on a cone-plate rheometer.
In sheetfed offset ink manufacture, 4BPG is typically incorporated at 18–22 wt% in a linseed oil/alkyd varnish. Laray tack values under 400 rpm roller speed generally fall between 8–12 g·m at 25 °C, depending on free acid content and varnish polymer architecture. Pre-wetting the pigment with 5–7 wt% of the total alkyd vehicle reduces dusting and shortens full dispersion time by 20–30 % relative to dry powder addition. The surface treatment also produces lower mill-base yield stress than untreated PR57:1; in a toluene/isopropanol gravure vehicle at 20 wt% pigment, the 4BPG mill base exhibits a Herschel-Bulkley yield stress of 3–6 Pa, compared with 8–14 Pa for a standard untreated PR57:1 of similar oil absorption. This permits higher pigment loading by 5–8 percentage points before exceeding a No. 4 Zahn cup viscosity of 25 s at 25 °C.
Polyolefin letdown evaluation on a 25:1 L/D twin-screw extruder at melt temperature of 180–200 °C indicates that 4BPG remains within an acceptable colour shift of ΔE ≤ 1.5 for 20 min residence time. Above 200 °C the monoazo lake begins to lose chroma and darkens due to partial decomposition of the azo chromophore. This thermal threshold is lower than quinacridone magenta PR122, which retains colour stability above 260 °C in polyolefin systems. Pre-drying at 80 °C for 6 h is required when storage relative humidity exceeds 60 %, because free moisture in the pigment powder can cause screw slippage and surface porosity in extruded strands. The pigment is not suitable for engineering polymers processed above 240 °C or for polyamide systems where acidic melt conditions accelerate lake metal exchange.
Differences between 4BPG and other red pigments become most visible in solventborne lamination inks. C.I. Pigment Red 57:1 has higher tinctorial strength but lower lightfastness than C.I. Pigment Red 122. In a 1:10 TiO₂ reduction, 4BPG typically measures 4–5 on the Blue Wool Scale under ISO 105-B02, while PR122 reduction maintains 7–8 under the same exposure conditions. Solvent bleed testing in toluene/ethyl acetate mixtures shows moderate bleed for 4BPG after 24 h at 25 °C, whereas PR122 remains visually non-bleeding. The trade-off is cost and colour purity: 4BPG provides a cleaner blue-shade red at standard ink film thicknesses of 1.5–2.5 µm without the rheology flattening sometimes observed with high-surface-area quinacridone grades. Table 2 summarizes the comparative behaviour under standard test methods.
| Property | 4BPG PR57:1 | Standard uncoated PR57:1 | PR122 quinacridone |
|---|---|---|---|
| Oil absorption, g/100g | 38–45 | 40–50 | 40–60 |
| Heat stability in polyolefin, °C | ≤ 200 | 180–200 | > 260 |
| Full-shade lightfastness, Blue Wool Scale | 4–5 | 4 | 7–8 |
| Solvent bleed in toluene/ethyl acetate | Moderate | Moderate | Low |
| Shade position | Blue-shade red | Red | Magenta |
These differences are measured on a continuous basis only where outdoor weathering or retort packaging is involved. For general ink rub resistance and lamination bond strength, the lower free metal content of 4BPG has not produced statistically significant changes in dry-bond peel strength when measured in N/15 mm according to ASTM F88-21. However, the moderate solvent bleed of PR57:1-based inks means that reverse-print lamination structures should be screened for migration into heat-sealable polyethylene sealants at 60 °C.
Rigid PVC extrusion trials on a counter-rotating twin-screw extruder with 22:1 L/D and screw diameter 50 mm show that 4BPG can be processed at melt temperatures up to 190 °C with a calcium-zinc stabilizer at 4.0 phr. Below 4.0 phr stabilizer, early colour shift of ΔE > 2 occurs after 15 min hold-up. The pigment is preferably added as a 50 wt% predispersion in DOP or DIDP; dry powder addition causes surface specks in calendered sheet at line speeds above 20 m/min. It is incompatible with lead-based stabilizers because metathesis can form lead lithol rubine with altered shade and reduced lightfastness.
Because the monoazo lake structure is sensitive to moisture and prolonged shear, storage should be in sealed polyethylene-lined paper sacks at 10–30 °C and relative humidity below 60 %. Moisture pickup above 2.5 % causes lumping and requires oven drying at 60–80 °C before dispersion. Dust-air mixtures require explosion control measures in accordance with ATEX Directive 2014/34/EU. Rubber compound use is established in natural rubber and SBR at 1.0–2.5 phr; rheometer t90 values differ by less than 0.5 min from an unfilled control at 2.0 phr, but formulators must account for the calcium content when adjusting zinc oxide and stearic acid ratios.
4BPG is subject to general industrial chemical inventories and falls under REACH registration obligations as CAS 5281-04-9; downstream users are responsible for verifying substance-specific restrictions in their formulation jurisdictions. Under RoHS Directive 2011/65/EU, lead, cadmium, and mercury are each controlled to 100 mg/kg or less in homogeneous material, and hexavalent chromium is controlled to 1000 mg/kg or less. Where food-contact applications are contemplated, compliance with EU Regulation 10/2011 Annex I or appropriate national positive lists must be confirmed, because lake metal exchange under acidic food simulants can release calcium and trace metals. Published data for this specific 4BPG surface treatment under migration testing is limited; solvent extraction followed by ICP-OES per EN 71-3 is used as a screening method for soluble metal limits in ink films. The grade is not recommended for toys or childcare articles without additional migration testing under EN 71-3:2019+AC:2020 migration limits for colourants in intended surface coatings.