| HS Code | 920579 |
| Product Name | Silicone Leveling Agent RH-T1245 |
| Chemical Composition | Polyether-modified polysiloxane |
| Appearance | Colorless to light amber transparent liquid |
| Active Content | 100% |
| Viscosity At 25 C | 500-1500 mPa·s |
| Density At 25 C | 1.02-1.06 g/cm³ |
| Refractive Index At 25 C | 1.430-1.450 |
| Ionicity | Nonionic |
| Solubility | Soluble in aromatic hydrocarbons, esters, ketones, and alcohols; insoluble in water |
| Surface Tension | 21-23 mN/m at 0.1% concentration |
| Flash Point | >100°C |
| Storage Temperature | 5-40°C |
| Shelf Life | 24 months |
As an accredited Silicone Leveling Agent RH-T1245 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Silicone Leveling Agent RH-T1245 is supplied in 25 kg net polyethylene drums with inner liners for safe storage and transport. |
| Container Loading (20′ FCL) | Silicone Leveling Agent RH-T1245 loaded in a 20′ FCL container, securely packed in drums with proper labeling for sea transport. |
| Shipping | Silicone Leveling Agent RH-T1245 is typically shipped as a liquid in sealed, labeled drums or IBC totes, protected from freezing, moisture, and direct sunlight. Transport according to the SDS and local regulations; include proper labeling, safety data sheets, and shipping documentation, and avoid damage or leakage during handling. |
| Storage | Store in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and open flames. Keep containers tightly closed when not in use. Protect from freezing and moisture. Store separately from strong acids, alkalis, and oxidizing agents. Do not store with food, feed, or beverages. Follow local regulations and label instructions. |
| Shelf Life | RH-T1245 shelf life is approximately 12 months in its original unopened container, stored cool, dry, and protected from direct sunlight. |
At 0.10–0.25 wt% on total formulation weight, RH-T1245 is added during the letdown stage of polyester-melamine coil coatings applied by three-roll reverse coaters running at 2,000–4,500 m/h; the leveling agent lowers dynamic surface tension gradients across profiles with dry film build from 5 µm to 25 µm and peak metal temperatures kept at 216–249°C for 30–50 s. Production-scale reverse roll coaters with chrome-plated transfer rolls at 0.5–1.0 µm Ra suppress roll split and ribbing when the additive is present, whereas roll-cleaning residues and chrome-free pretreatment inhomogeneities otherwise promote crater chains at 1,500 m/h and above. Compliance verification follows EN 10169:2022 for continuously organic-coated flat steel products, ASTM D4147-99(2021) for drawdown application characteristics, and EN 13523-25:2022 humidity-resistance testing after alkaline cleaning. The downstream production process includes alkaline wash, non-rinse thin-film pretreatment, primer application, topcoat application, and crosslinking in four-zone catenary ovens; terminal parts include pre-painted galvanized roof and wall cladding, appliance wrapper panels, and garage door slats.
Above 0.30 wt%, panel stack blocking and polyurethane lamination peel trials indicate migratory siloxane at the topcoat/primer interface can reduce foam adhesion, and published data for the interaction with chrome-free pretreatments is limited. The addition rate is therefore lowered to 0.10–0.15 wt% when coil stock is destined for insulated sandwich panels requiring after-foaming within 72 h of coating.
In 2K acrylic polyurethane refinish clearcoats, RH-T1245 is incorporated at 0.2–0.6 wt% on resin solids after catalyst addition and before viscosity adjustment; production-scale mixing uses slow-speed agitation at 1,000–1,500 rpm to avoid air entrainment. Liquid surface tension is checked with ASTM D1331-20 and EN 14370:2004, while cross-cut adhesion after sanding and recoat is evaluated per ISO 2409:2013 and ASTM D3359-17; volatile organic content is maintained under EU 2004/42/EC Stage B limits for refinish products. The application window uses 1.3 mm HVLP fluid tips at 2.0–2.5 bar inlet pressure for 50–70 µm clearcoat films, followed by force-drying at 60°C for 30 min or ambient drying overnight. The additive is adjusted so that liquid surface tension remains above 26 mN/m measured by EN 14370:2004; lower values from excess polydimethylsiloxane correlate with recoat adhesion loss. Terminal products include basecoat/clearcoat refinish systems for passenger vehicles and commercial transport. Addition above 0.6 wt% is not recommended where recoatability after 7 days natural weathering is tested, because siloxane migration into the polar intercoat boundary can cause detachment under ISO 2409:2013 cross-cut loading.
When aqueous wood finishes exhibit pH drift above 8.5 during summer line operation, RH-T1245 is post-added at 0.3–0.6 wt% on liquid coating mass after pH adjustment to 7.5–8.2 and dispersed under 15–20°C high-shear mixing to prevent microfoam and pigment-binder destabilization; compliance is limited to toy-contact furniture surfaces under DIN EN 71-3:2019+A1:2021 and EU 2009/48/EC, and the resulting waterborne acrylic/polyurethane lacquers are curtain-coated or spray-applied as interior furniture topcoats, children’s room trim paints, and toy finishes.
At 0.10–0.35 wt% on total formulation weight, RH-T1245 is dissolved into the urethane acrylate oligomer phase before monomer dilution, then processed on single or dual roller coaters with closed doctor chambers applying 10–50 g/m² at 8–12 m/min. Curing uses gallium-doped mercury lamps at 120 W/cm with measured UVA output of 250–350 mJ/cm²; below 300 mJ/cm², flow-induced striations become more severe when belt temperature exceeds 32°C, and the silicone leveling agent suppresses surface-tension gradients without acting as an oxygen scavenger or defoamer. Compliance for parquet and furniture foil applications follows DIN EN 927-2:2020 for exterior wood coating performance and DIN 68861-1:2011 for furniture surface classification. Terminal products include UV-cured parquet topcoats, pre-finished flooring panels, and digitally printed furniture foils overcoated with UV varnish.
In TGIC-free polyester/HAA architectural powder topcoats, RH-T1245 is dry-blended at 0.3–0.8 wt% before co-rotating twin-screw extrusion at 1,200–1,800 kg/h with melt-zone temperatures controlled at 80–110°C; the process then transfers the melt to a chill roll at 10–15°C and through a pin mill to particle size D50 35–45 µm with fines below 8% under 10 µm. Powder topcoats are applied electrostatically at 60–80 kV corona and cured at 180°C for 15 min; compliance is assessed under EN 13438:2013, Qualicoat Specifications, and AAMA 2604 for architectural aluminium profiles. Terminal products include window and curtain-wall aluminium extrusions and MDF decorative panels. Above 0.8 wt%, gloss measured by ISO 2813:2014 at 60° can become inconsistent across the cure window, and impact resistance evaluated by ASTM D2794-93(2019) may show no improvement; published data for the specific HAA system with RH-T1245 is limited, so addition above 0.8 wt% requires line trial confirmation.
Gravure ink foam nucleation at 180–250 m/min transfer speeds in NC/PU solvent-based inks for BOPP and PET is suppressed by RH-T1245 at 0.5–1.5 wt% on ink weight after letdown and low-shear pumping at 0.5–1.0 bar; compliance for food-contact packaging is governed by EU 94/62/EC and SR 817.023.21, while seal-strength after extrusion lamination is verified by ASTM F88/F88M-21. Terminal structures include snack food wrappers, retort pouches, and shrink sleeves; addition above 1.5 wt% is avoided because bond strength at the print/lamination interface can fall below 2.5 N/15 mm.
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RH-T1245 is supplied as an organomodified polydimethylsiloxane leveling agent for solventborne coating systems in which surface-tension-driven defects such as craters, orange peel, picture framing, and retraction from low-energy substrates must be controlled without excessive bulk-film plasticization. The product belongs to the polyether-modified polysiloxane class and is conventionally introduced during letdown after pigment dispersion to limit chain scission under sustained high-shear conditions. Its primary function is interfacial: it reduces surface tension differentials across the wet film while the coating remains open, allowing spray droplet patterns, roll striations, and brush marks to flow out before solvent flash-off or gelation.
Because complete public certificates of analysis for RH-T1245 are not consolidated in regulatory or producer portals, the following data are expressed as class-typical benchmarks for solventborne polyether-modified polydimethylsiloxanes with medium-to-high active-matter content. They are not batch-certified release limits unless confirmed by the manufacturer’s certificate. Product-specific exact values for the model RH-T1245 require a batch certificate or retained sample from the selling distributor.
| Parameter | Class-typical range or observation | Test method |
|---|---|---|
| Delivery form | Clear to slightly hazy amber liquid | Visual assessment |
| Non-volatile matter | 50–100 wt% | ISO 3251:2019 |
| Dynamic viscosity | 100–3,000 mPa·s at 25 °C | ISO 3219:2021 |
| Density | 0.95–1.05 g/cm³ at 20 °C | ISO 2811-1:2023 |
| Flash point | >100 °C | ISO 1523:2002 |
Regulatory compliance documentation for solventborne additive shipments normally includes REACH registration data for the solvent, silicone backbone, and polyether chain components. Evaluation for food-contact use is not implied by the absence of a specific declaration; a separate suitability statement from the producer is required when the coated article is regulated under EU 1935/2004 or FDA 21 CFR 175.300.
In production-scale solventborne alkyd and acrylic melamine operations, the additive is commonly pre-diluted before incorporation into large letdown tanks. A 1:5 to 1:10 dilution in xylene, methoxypropyl acetate, or butyl acetate is typical. The diluted stream is fed through a bottom-valve circulation loop or dosed under the liquid surface to avoid foam entrainment. Field practice with similar polyether-modified polysiloxanes indicates that adding the product directly to a pigment concentrate at dissolver tip speeds above 15 m/s can reduce crater-control efficiency, requiring higher use levels to recover surface uniformity. In a 2,000-L letdown vessel equipped with an anchor stirrer operating at 25–40 min⁻¹, addition after the final resin charge is preferred.
In high-viscosity epoxy polyamide primers, direct addition of undiluted RH-T1245 is not recommended when the coating temperature is below 25 °C. A localized concentration gradient created by undiluted additive can generate surface defects that are not fully re-dissolved by the existing aromatic and ketone solvent package. Pre-dilution at 1:5 to 1:10 in xylene or methyl isobutyl ketone lowers the feed viscosity to below 2,000 mPa·s and permits dosing through a static mixer upstream of the filling line. Pre-diluted batches should be consumed within 8 h or stored in sealed stainless vessels under dry nitrogen to prevent moisture uptake and solvent evaporation. The pre-dilution solvent selection should match the letdown solvent balance; a solvent that is too fast can cause air entrainment at the filling nozzle, while a very slow tail solvent can persist in the dried film and increase solvent retention.
The performance difference between RH-T1245, high-molecular-weight polyacrylate leveling agents, and fluorocarbon-modified polyacrylates is most visible under high-speed coil coating application. The following comparative data are drawn from published additive-class benchmarks and are not certified for RH-T1245 unless confirmed on the exact binder and cure schedule.
| Property | Organomodified silicone RH-T1245 category | High-molecular-weight polyacrylate | Fluorocarbon-modified polyacrylate |
|---|---|---|---|
| Surface tension at 0.3 wt% addition in acrylic melamine clearcoat | 24–28 mN/m | 30–32 mN/m | 20–24 mN/m |
| Crater suppression in high-solids polyester melamine | High | Moderate | High |
| Recoatability after 24 h dry without sanding | GT 1 to GT 2 depending on dosage and cure | GT 0 to GT 1 | GT 2 to GT 3 with possible dewetting |
| Gloss at 60° after overbake 150 °C for 30 min | Unchanged to +2 GU | Unchanged | Possible haze or gloss loss |
| Increase in surface slip at equal dosage | Measurable | Low | High |
In coil coating lines operating above 80 m/min with peak metal temperatures exceeding 232 °C, the flow window is extremely short. When a high-molecular-weight polyacrylate is replaced by RH-T1245, crater resistance can improve at lower addition levels, but the formulator usually must reduce the separate slip-control additive because the silicone leveling agent contributes additional surface slip. The recoatability boundary is more sensitive with RH-T1245: in amine-cured or melanine-cured systems, the first coat can pass cross-hatch adhesion after 24 h, but a second coated layer may fail if the first was cured beyond 48 h and no scuffing is performed.
In two-component polyurethane clearcoats, the practical addition range is narrower than in alkyd systems. At 0.1 wt% total formulation, long-wave texture may decrease; at 0.4 wt%, recoat adhesion can drop below GT 2 in ISO 2409:2020 after a 24 h or longer inter-coat interval. The failure response is not linear: above a formulation-specific threshold, additional RH-T1245 does not improve leveling but sharply increases inter-coat dewetting and surface slip. Published data for the exact threshold of RH-T1245 is limited; the common safe ceiling for re-coatable clearcoats using similar polyether-modified polydimethylsiloxanes is 0.25 wt%.
Equilibrium surface tension does not reliably predict leveling under air-atomized spray application. Dynamic surface tension measured at surface creation rates between 1 bubble/s and 10 bubble/s is more relevant because the wet film is reapplied continuously across the substrate. Organomodified silicone leveling agents reduce surface tension faster at high surface creation rates than conventional polyacrylates, which mainly level long-wave flow after film deposition. RH-T1245 can therefore control short-wave craters and pin-holing that appear immediately after spray application when the film is still highly mobile.
The polyether side-chain content determines the additive’s compatibility with medium-polarity binders. Insufficient polyether content causes excessive surface segregation, leading to a weakly bound interfacial layer that lowers recoatability. At addition levels above 0.5 wt% in two-component polyurethane clearcoats with co-solvent content below 5 wt%, storage separation or silicone-induced haze may occur. Low-temperature storage should remain above 5 °C; freezing may create phase separation that does not fully reverse on thawing. High-temperature storage should remain below 40 °C to avoid color development and viscosity drift.
Operational boundaries include avoiding combination with amine-functional silanes or high-amine epoxy curatives during pigment dispersion. Premature reaction can gel the additive or reduce interfacial activity. Compatibility with short-oil alkyd and acrylic melamine systems is generally acceptable, while long-oil alkyds with low aromatic content can show reduced clarity at loadings above 0.3 wt%. Published data for this specific configuration is limited; laboratory ladder studies using the actual cure schedule and production solvent package remain necessary before scale-up.