| HS Code | 116062 |
| Productname | Lithol Rubine 4BPC |
| Colorindexname | Pigment Red 57:1 |
| Colorindexnumber | 15850:1 |
| Chemicalclass | Monoazo calcium lake |
| Appearance | Red powder |
| Hue | Bluish red / magenta |
| Specificgravity | 1.6-1.8 |
| Oilabsorption | 35-50 g/100 g |
| Moisturecontent | <=1.0% |
| Ph | 7.0-9.0 |
| Watersolublematter | <=1.0% |
| Lightfastness | 4-5 (blue wool scale) |
| Heatstability | 160-180 C |
| Acidresistance | 3 (1-5 scale) |
| Alkaliresistance | 2 (1-5 scale) |
| Soapresistance | 3 (1-5 scale) |
| Migrationresistance | Low to moderate |
| Dispersion | Good |
As an accredited Lithol Rubine 4BPC factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Lithol Rubine 4BPC is supplied in 25 kg multi-wall paper sacks with polyethylene liners, labeled and sealed for safe transport. |
| Container Loading (20′ FCL) | Lithol Rubine 4BPC pigment is palletized, shrink-wrapped, and securely loaded into a dry 20-foot FCL container for ocean shipment. |
| Shipping | Lithol Rubine 4BPC is shipped as a non-hazardous pigment preparation. It is not subject to UN dangerous-goods classification; no UN number, hazard label, or placard is required. Use sealed, labeled containers to prevent moisture and contamination, protect from heat and direct sunlight, and handle according to normal industrial hygiene practices. |
| Storage | Store Lithol Rubine 4BPC in a cool, dry, well-ventilated area away from direct sunlight, heat, moisture, and ignition sources. Keep containers tightly closed when not in use, and avoid dust generation or inhalation. Store only in original or suitable labeled containers, separate from oxidizing agents and incompatible materials, and away from food, feed, or drinking water. Use appropriate PPE and follow local regulations. |
| Shelf Life | Lithol Rubine 4BPC typically has a shelf life of 5 years when stored cool, dry, well-ventilated, and away from sunlight and moisture. |
In sheetfed offset ink manufacturing, Lithol Rubine 4BPC is incorporated into alkyd-phenolic resin varnishes and high-boiling mineral oil systems where the calcium lake structure supplies high color strength for high-volume commercial print runs. Regulatory compliance is anchored to the EuPIA exclusion policy for heavy metals and to REACH Regulation (EC) No 1907/2006; when the pigment is used as process magenta in four-colour ink sets, colorimetric conformance is evaluated against ISO 2846-1:2017 on the reference substrate specified in the standard. The formulation addition ratio in sheetfed ink falls between 15 wt% and 22 wt% of total paste ink mass, with the lower range used for transparent modified magenta and the upper range for high-intensity spot red. Production on a manufacturing line typically begins with a high-speed disperser running at 18-20 m/s tip speed to wet the pigment in varnish, followed by a three-roll mill set to produce a fineness of grind below 10 µm measured by Hegman gauge per ASTM D1210. Inkometer tack is then adjusted to 8-12 units at 1 minute per ASTM D4361. Finished products include sheetfed offset inks and heatset web offset inks used in commercial brochures, direct mail, periodicals, and non-food folding cartons. The operational boundary is set by lightfastness: when evaluated by ISO 105-B02, Lithol Rubine 4BPC typically exhibits Blue Wool ratings below 4, restricting exterior signage and extended-UV-exposure print applications.
| Application segment | Primary standard/code | Measured or controlled parameter | Typical range |
|---|---|---|---|
| Sheetfed offset ink | ISO 2846-1:2017, ASTM D1210 | Fineness of grind | 5-10 µm |
| Water-based flexographic ink | ISO 2431:2019 | DIN 4 mm cup viscosity | 30-60 s |
| Rigid PVC calendering | EN 71-3:2019+A1:2021 | Melt processing temperature | 165-185 °C |
| Sulfur-vulcanized rubber sole compound | ASTM D5289-19a | Cure T90 shift from control | ±2 min |
Production-scale calendering of rigid PVC colored with Lithol Rubine 4BPC requires control of melt temperature because the pigment can undergo shade drift and strength loss when dwell time above 200 °C is extended. Calender rolls are therefore held at 165-185 °C to balance fusion against pigment degradation. Compliance for PVC articles destined for the European market is evaluated under REACH Regulation (EC) No 1907/2006; for toys or childcare articles, migration of certain elements is tested according to EN 71-3:2019+A1:2021. Although the industrial grade is not positioned for direct food contact, formulators must confirm specific migration limits if the colored PVC enters food-contact packaging under EU Regulation (EC) No 1935/2004 and EU Regulation (EU) No 10/2011. The addition ratio in calendered rigid PVC is typically 0.8-2.0 phr (parts per hundred resin), with 1.5 phr producing an opaque red in thin films of 0.2-0.4 mm; additions below 0.5 phr are suitable only for tinting because the pigment has high tint strength and shade control becomes difficult. The downstream production sequence uses a high-speed hot mixer to 105-115 °C, a twin-screw or kneader compounding stage for pre-gelation, a two-roll mill at 150-170 °C, and a multi-roll calender. Dispersion below 40 µm agglomerate size is verified by press-out because undispersed red specks are a known failure mode on film lines. Finished products include indoor vinyl flooring, wall covering, stationery films, and non-food packaging sleeves. A process limitation is that Lithol Rubine 4BPC may contribute to plate-out on calender rolls when stabilizer packages contain high levels of calcium stearate, as the calcium lake structure can co-precipitate with metal soaps; roll surface deposition should be monitored during extended campaigns.
Because the calcium lake surface is sensitive to aqueous pH above 9.5, Lithol Rubine 4BPC in water-based flexographic and gravure inks is predispersed in alkali-soluble acrylic resin solutions with pH maintained between 8.5 and 9.5; prolonged exposure to stronger alkali can strip the lake structure and reduce color strength. The regulatory anchor for such inks is REACH Regulation (EC) No 1907/2006 and, for printed paper and board not in direct food contact, the EuPIA Good Manufacturing Practice guideline for food packaging inks. Formulators should obtain a supplier declaration for the absence of restricted aromatic amines and heavy metals before use in packaging-adjacent layers. The formulation addition ratio in final flexographic ink is 5-10 wt% pigment, while the pigment concentrate for letdown typically carries 20-30 wt% loading in acrylic resin vehicle. Production uses a high-speed disperser followed by a bead mill with zirconia media; grind fineness is controlled to 5-10 µm and viscosity is adjusted to 30-60 s on a DIN 4 mm cup at 20 °C per ISO 2431:2019. Finished products are surface-printed paper bags, gift wrap, coated paperboard cartons, and low-UV-exposure label stock. The ink is not suitable for outdoor signage or labels with high lightfastness requirements because weathering will fade the red faster than high-performance magenta pigments.
Sulfur-cured SBR and natural rubber compounds containing Lithol Rubine 4BPC show low-cost red coloration, but the calcium salt chemistry can interact with accelerators and retarders, so incoming batches should be evaluated for cure rheology at 160 °C using ASTM D5289-19a. A shift in T90 beyond ±2 min from the control batch indicates the need to adjust accelerator level. The relevant compounding standard is ASTM D3182-21 for mixing and preparing standard vulcanized sheets, while EU-bound rubber articles intended for prolonged skin contact must be checked against REACH Regulation (EC) No 1907/2006 and the REACH Annex XVII restrictions on polycyclic aromatic hydrocarbons in certain consumer articles. The addition ratio is 1-3 phr, with 2 phr standard for opaque red shoe soles; above 3 phr the pigment can bloom to the surface after vulcanization because solubility in the rubber matrix is limited. The production process involves internal mixer pre-mastication at 110-130 °C, addition of zinc oxide and stearic acid, two-roll mill addition of sulfur and accelerators at 60-80 °C, and press curing at 140-160 °C. Dispersion is evaluated by torn-surface visual inspection against a six-step reference panel. End products include footwear soles, rubber mats, erasers, and industrial gaskets where lightfastness demands are low. The pigment is not recommended for peroxide-cured EPDM because the metal-salt structure may consume free radicals and alter crosslink density.
Twin-screw compounding of EVA-based masterbatches with Lithol Rubine 4BPC at 30 wt% loading becomes sensitive to screw torque and melt temperature; the pigment may retain moisture, so pre-drying at 80-100 °C for 2 h is recommended when storage humidity exceeds 60 % RH. EU industrial masterbatch production is governed by REACH Regulation (EC) No 1907/2006; for non-food polyolefin articles, the applicable test for heavy metal extractables is EN 71-3:2019+A1:2021 if articles are classified as toys. Food-contact film under EU Regulation (EU) No 10/2011 generally excludes Lithol Rubine 4BPC without a specific migration authorization. The addition ratio in the masterbatch is 20-30 wt%, while the final polyolefin article uses 0.5-1.5 wt% pigment; above 1.5 wt% in LDPE film, there is increased risk of surface bloom and screw slippage in blown film extrusion. Compounding is performed on a co-rotating twin-screw extruder with L/D 40:1, screw speed 300-600 min⁻¹, barrel temperatures 170-200 °C, and vacuum venting at -0.06 to -0.08 MPa; the melt is strand-pelletized after water bath cooling. Finished products include refuse sacks, carrier bags, binder covers, and non-food household articles. The compound is unsuitable for high-temperature engineering polymers processed above 250 °C, as shade dulling and gas evolution may exceed acceptable limits.
For flexible PVC screen printing inks, Lithol Rubine 4BPC requires a thixotropic resin system that maintains a viscosity plateau between 8,000 cP and 18,000 cP at 20 s⁻¹. If viscosity drops below the lower boundary, the pigment settles in the mesh and produces mottled prints; if viscosity rises above 20,000 cP, mesh clogging occurs on 90-120 threads/cm screens. Regulatory compliance for such printing inks is anchored to REACH Regulation (EC) No 1907/2006, the EuPIA exclusion policy for heavy metals, and for printed articles intended for the European consumer market, REACH Annex XVII restrictions on certain azo colourants. Each batch certificate should list lead, cadmium, mercury, and chromium(VI) below the supplier's agreed limit. The addition ratio in screen ink is 6-12 wt% pigment, with 10 wt% typical for a full-strength red; lower loadings down to 3 wt% are used for extended-mesh halftone reproduction. Production uses a planetary mixer for pre-dispersion, followed by a triple-roll mill or bead mill to a fineness of grind below 15 µm; the ink is then adjusted with cyclohexanone or other high-boiling solvents to a flash point above 60 °C depending on application. Finished products include screen-printed flexible PVC banners, point-of-sale graphics, and indoor decorative films. The operational boundary is determined by lightfastness: Lithol Rubine 4BPC is not advisable for outdoor point-of-sale signage that requires stable UV performance, as ISO 105-B02 ratings typically remain below 4 in this binder system.
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Lithol Rubine 4BPC is a calcium toner pigment classified as C.I. Pigment Red 57:1 (CAS 5281-04-9), produced from 4-[(4-methyl-2-sulfophenyl)azo]-3-hydroxy-2-naphthoic acid. The alphanumeric suffix identifies a manufacturer-specific controlled-particle-size grade rather than a structural departure from the calcium salt chemistry. The grade is specified for lithographic and gravure ink systems, polyolefin masterbatch, and selected rubber and PVC applications where viscosity control, low-dust handling, and controlled soluble-salt release are critical. Unlike barium or strontium toners of similar azo chemistry, the calcium salt exhibits a bluer masstone and higher tinctorial strength at equal pigment volume concentration when assessed against a retained reference standard using ISO 787-24:1988. The pigment is supplied in presscake, granular, and low-dusting powder forms; the exact form affects dispersibility in high-viscosity vehicles and should be selected according to the manufacturing line configuration.
The primary differentiation is particle size distribution. Commercial certificates of analysis for high-performance C.I. Pigment Red 57:1 grades list laser diffraction D50 values between 0.20 µm and 0.35 µm and D90 values below 0.65 µm; unmodified grades may show D90 values above 1.0 µm. The narrower distribution lowers the millbase yield value at equal pigment volume concentration in offset vehicles, reducing tack and permitting 2–4 wt% higher pigment loading without exceeding the target flow curve. Rheological evaluation using a cone-and-plate viscometer at 25 °C per ISO 2884-1:2006 reveals shear-thinning behaviour typical of flocculated pigment dispersions; the controlled surface treatment of the 4BPC grade retards flocculation during letdown in high-viscosity rosin-modified phenolic vehicles.
Overgrinding in a 5 L horizontal bead mill using 0.8 mm yttria-stabilized zirconia beads at speeds above 1,500 rpm can reduce primary crystal size and increase surface area beyond the stabiliser capacity. The resulting viscosity surge and gloss loss in sheetfed inks has been documented when mill residence time exceeds 35 min for a 150 kg batch at 15 wt% pigment loading and chamber temperatures above 45 °C. This failure mode is the principal reason the pigment is used in short pass cycles rather than extended recirculation milling; the processing window is narrow because the calcium lake structure is mechanically soft compared with high-performance organic pigments such as quinacridones or diketopyrrolopyrroles.
In high-speed sheetfed offset formulations, the pigment is incorporated at 15–18 wt% into a vehicle of modified rosin ester and linseed oil alkyd; dispersion is performed on a three-roll mill with roll temperatures maintained at 25–35 °C and nip pressures between 0.8 MPa and 1.2 MPa. Colour is assessed with a spectrophotometer using D65/10° geometry according to ISO 13655:2017; production ink batches are matched to a retained reference standard with ΔEab tolerances set below 1.0. The 4BPC grade provides a blue-shaded red masstone with a yellowish pink tint tone; exact tint coordinates vary with the acid number of the rosin ester and the cobalt-manganese drier concentration. Printing trials on sheetfed presses with blanket temperatures of 25–30 °C show that the 4BPC grade reduces piling on the blanket compared with unmodified 4B toner when fountain solution pH is maintained between 4.7 and 5.3. Water pick-up on an IGT emulsification module should remain below 20 % after 10 min; if water pick-up exceeds 25 %, the pigment surface can be stripped from the vehicle and shade loss occurs. This interaction with dampening solution is a critical control point on multi-unit presses running alcohol-free fountain concentrates.
Colourimetric control of Lithol Rubine 4BPC in offset inks is performed with a laboratory proofing apparatus such as an IGT or Prüfbau printability tester under ISO 2834-1:2020. The ink is evaluated on coated paper with a surface pH of 7.0–8.0 and a gloss level of 65–70 Gardner units. The pigment is compared against the reference standard in both masstone and 10:1 tint to titanium dioxide; the tint tone is more sensitive to dispersion state than masstone, and uncontrolled flocculation produces a visible shift of 2–3 ΔEab units in the tint. Batch-to-batch variation in particle size can shift millbase rheology; therefore, a 5 kg pilot dispersion is run before a full 150 kg production millbase on three-roll mills with automatic hydraulic nip control.
Incoming raw-material release for Lithol Rubine 4BPC normally uses the following specification ranges. These values are consolidated from supplier documentation for controlled calcium C.I. Pigment Red 57:1 toners; the manufacturer certificate of analysis should be reviewed for lot-specific data before release to production.
| Parameter | Test method | Typical specification |
| pH of aqueous extract | ISO 787-9:2019 | 7.0–9.0 |
| Matter volatile at 105 °C | ISO 787-2:2021 | ≤ 2.0 % |
| Oil absorption | ISO 787-5:1995 | 40–55 g/100 g |
| Residue on 45 µm sieve | ISO 787-7:2009 | ≤ 0.1 % |
| Specific gravity | ISO 787-10 | 1.50–1.60 |
| Relative tinting strength | ISO 787-24:1988 | 95–105 % |
Residual soluble salts and moisture content are not merely release criteria; they affect ink performance in high-speed heatset drying ovens. When moisture exceeds 2.0 %, water can disrupt wetting of the pigment by the rosin-modified phenolic vehicle and increase pinhole formation in the printed film. Consequently, the pigment should be pre-dried at 60–70 °C for 4–6 h if storage relative humidity exceeds 60 % and the ink is to be run through a heatset dryer with a web temperature higher than 140 °C. Direct exposure to steam humidification lines in the pressroom is also undesirable because the calcium lake is slightly hygroscopic.
Compared with C.I. Pigment Red 57:1 grades that contain barium sulfate extender, the 4BPC grade is supplied without resin binders or extender pigments. This absence of inert fillers permits lower oil absorption and greater flexibility in varnish formulation; however, the pigment is more prone to dusting if dry handling systems do not use local exhaust ventilation. In paste ink formulations, combination with barium sulfate extenders should be evaluated for ion exchange at the calcium lake surface; laboratory screening can reveal a loss of tinctorial strength of 10–15 % after 48 h storage at 40 °C when the resin acid number exceeds 20 mg KOH/g.
| Property | Lithol Rubine 4BPC | Conventional calcium 4B toner | C.I. Pigment Red 3 |
| Colouristic character | Blue-shaded red, yellowish pink tint at 10:1 reduction | Similar masstone, broader particle size distribution | Yellow-red, lower tinctorial strength |
| Rheology in offset vehicle | Lower tack at equal pigment volume concentration due to controlled particle size | Higher tack and increased flocculation risk | Not typically used in sheetfed offset |
| Lightfastness | Blue Wool Scale 3–4 in alkyd paints per ISO 105-B02 | Blue Wool Scale 3–4 | Blue Wool Scale 4–5 in masstone in selected systems |
| Regulatory status | Requires article-specific migration testing for food contact | Same | Different positive-list status depending on region |
Replacement is feasible only in short-dwell-time melt processing. The pigment has a lower thermal threshold than quinacridone and many Naphthol AS reds. In polypropylene injection moulding with melt temperatures of 200–220 °C and residence times below 5 min, Lithol Rubine 4BPC can produce a clean red shade at 0.3–0.5 wt% final pigment content. At melt temperatures above 240 °C, colour strength declines and the shade drifts toward orange; decomposition products may affect odour and mechanical properties. Processing trials on a 25 mm twin-screw extruder with an L/D ratio of 40:1, screw speed of 250 rpm, and throughput of 12 kg/h indicate that the pigment should be added as a 40 % masterbatch in LLDPE carrier rather than as direct powder addition. Direct powder feeding can create agglomerates larger than 45 µm, which survive in the extrudate and reduce filter life in injection-moulded articles.
Rigid PVC calendering at 170–190 °C can be performed with Lithol Rubine 4BPC when the stabiliser system contains calcium-zinc or organotin compounds; lead-stabilised PVC should be avoided because of potential ion exchange at the pigment surface and subsequent colour shifts. The pigment has limited resistance to hydrogen chloride released during PVC degradation; therefore, processers must maintain stabiliser concentration above the minimum supplier recommendation. In sulfur-cured rubber, the pigment is added at 1–2 phr; cure systems with accelerators such as MBTS and DPG can cause shade shifts if the cure temperature exceeds 170 °C for more than 10 min. The pigment does not interfere with vulcanisation kinetics at these levels, but the calcium lake can react with stearic acid and slightly reduce scorch time. Published data for this specific grade in sulfur-cured rubber is limited, and factory mixing trials are required before replacing an incumbent rubber-grade red pigment.
Thermal exposure above the stated processing boundaries produces a measurable hue shift rather than an immediate loss of chroma. The azo chromophore undergoes thermal degradation through cleavage of the hydrazone form of the lake; the reaction releases fragments that can discolour the polymer matrix and generate plate-out on metal cooling rolls. In extrusion coating of pigmented polyolefin webs, plate-out is visible on the chill roll after 20–30 min of continuous operation when the melt temperature exceeds 230 °C. The deposit comprises low-molecular-weight degradation products and calcium carbonate residues; it can be removed only by solvent-assisted wiping with an alkaline detergent. This operational boundary is particularly severe on tandem extrusion lines where polymer stagnates in the adapter and die lips.
The pigment is not recommended for outdoor applications requiring weathering beyond 12 months. Conventional calcium 4B toners typically show Blue Wool Scale ratings of 3–4 in alkyd paints per ISO 105-B02, and controlled-particle-size variants do not materially improve photostability. Ultraviolet exposure causes darkening and shade drift before significant mass loss; therefore, the product is restricted to indoor printing ink, packaging, and consumer articles not exposed to direct sunlight during service.
Migration testing under EU Regulation 10/2011 and FDA 21 CFR 175.300 is required before any direct food-contact use. Lithol Rubine 4BPC is not intrinsically approved for direct food-contact coloration; the pigment should be separated from food by a functional barrier of at least 10 µm of approved polymer or paperboard unless article-specific migration testing demonstrates compliance. Published data for the exact 4BPC designation in these configurations is limited, and reliance on generic C.I. Pigment Red 57:1 data is not sufficient for regulatory submission.
For electrical and electronic applications using pigmented polyolefin components, the following regulatory test matrix is used to qualify the coloured compound rather than the pigment alone.
| Regulatory area | Standard or method | Condition to verify |
| Restricted heavy metal migration | EN 71-3:2019+A1:2021 | Lot-specific extraction limits |
| RoHS restricted substances | IEC 62321-5:2013, 2011/65/EU | Lead, cadmium, mercury, hexavalent chromium |
| REACH Annex XVII | EC 1907/2006 | Restricted azo dyes, lead carbonates, sulfates |
| Food-contact migration | EU 10/2011, FDA 21 CFR 175.300 | Article-specific migration testing required |
In solvent-based packaging gravure inks, Lithol Rubine 4BPC is dispersed at 8–12 wt% in nitrocellulose-polyurethane vehicles. Ethyl acetate and isopropanol blends can cause slight bleeding of the pigment onto adjacent films if residual free calcium ions are high; the low soluble-salt specification reduces but does not eliminate this tendency. Formulators should avoid amine-based additives with pH above 9.0 because the pigment may dissolve slightly and stain the print plate. A barrier varnish or overprint lacquer is typically required where the printed surface contacts alkaline aqueous solutions. The product is not considered suitable for waterborne packaging inks intended for direct food contact, where bleed resistance in alkaline media is a prerequisite and phenolic-free binder systems may not provide sufficient wetting of the pigment surface.