| HS Code | 602358 |
| Product Type | Methyl terminated hydrogen branched silicone oil |
| Chemical Structure | Methyl-terminated branched poly(methylhydrogensiloxane) |
| Appearance | Colorless to light yellow transparent liquid |
| Viscosity At 25 C | 50–200 mPa·s |
| Hydrogen Content | 0.45–0.60% |
| Density At 25 C | 0.95–0.98 g/cm³ |
| Refractive Index At 25 C | 1.400–1.410 |
| Flash Point | ≥100°C |
| Volatile Matter At 150 C For 3 H | ≤2.0% |
| Surface Tension | 20–25 mN/m |
| Ph | 6–7 |
| Active Content | ≥99% |
| Ionicity | Nonionic |
| Solubility | Insoluble in water; soluble in toluene, xylene, and other organic solvents |
| Storage Temperature | 5–35°C |
| Shelf Life | 12 months in unopened container |
As an accredited Methyl Terminated Hydrogen Branched Silicone Oil RH-H502 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | RH-H502 is supplied in 200 kg sealed steel drums, clearly labeled and stored in a cool, dry, well-ventilated area. |
| Container Loading (20′ FCL) | Methyl Terminated Hydrogen Branched Silicone Oil RH-H502 is loaded in clean, dry 20′ FCL containers with proper sealing and labeling. |
| Shipping | RH-H502 is typically shipped in sealed steel drums or IBC totes under ambient conditions. Keep containers tightly closed and protect from moisture, heat, and contamination. Transport according to the SDS and local regulations; use appropriate PPE and avoid contact. |
| Storage | Store Methyl Terminated Hydrogen Branched Silicone Oil RH-H502 in a cool, dry, well-ventilated area away from heat, sparks, open flames, and direct sunlight. Keep containers tightly closed, correctly labeled, and protected from moisture, acids, bases, and oxidizing materials. Avoid freezing and excessive temperatures; maintain recommended ambient conditions. Use secondary containment, inspect regularly for leaks or damage, and follow local regulations. |
| Shelf Life | Shelf life is 12 months from date of manufacture when stored in the original, sealed container under cool, dry conditions. |
Table 1. Addition-cure LSR formulation response envelope at constant vinyl polymer and fumed silica loading.
| SiH/SiVi molar ratio | Shore A hardness | Tensile strength | Elongation at break | Tear strength | Compression set |
|---|---|---|---|---|---|
| 1.0:1 | 34 | 5.2 MPa | 620% | 13 kN/m | 26% |
| 1.2:1 | 42 | 6.8 MPa | 580% | 18 kN/m | 17% |
| 1.4:1 | 47 | 7.4 MPa | 510% | 21 kN/m | 12% |
| 1.6:1 | 53 | 6.9 MPa | 420% | 23 kN/m | 9% |
| 1.8:1 | 56 | 5.6 MPa | 330% | 20 kN/m | 8% |
In solventless addition-cure release coatings, RH-H502 is blended with vinyl-functional polydimethylsiloxane and a platinum-divinyltetramethyldisiloxane complex at a platinum concentration of 80 ppm to 120 ppm. The target SiH/SiVi molar ratio is lower than in molded rubber, typically 1.1:1 to 1.3:1, because any unreacted hydride in the cured film migrates into the pressure-sensitive adhesive and raises release force drift during roll aging. Coat weight on 23 µm biaxially oriented polypropylene is maintained at 0.9 g/m² to 1.2 g/m² using a slot-die coater with a lip gap of 50 µm and a line speed between 300 m/min and 600 m/min. Oven temperature is set at 135 °C to 155 °C with residence time of 8 s to 12 s; platinum inhibition by humidity is minimized when coating room relative humidity is held below 55%. Release force is measured after lamination with TESA 7475 tape under FINAT FTM-3 and after 24 h at 23 °C and 50% RH; target values below 15 cN/25 mm are obtainable, while subsequent adhesion is checked under FINAT FTM-4. The branched hydride architecture lowers volatile content and reduces misting at high coating speeds compared with linear methyl hydrogen silicone oil because the higher molecular weight raises the boiling range and lowers the fraction of low-molecular-weight cyclic siloxanes. A production-scale limitation is that the cured film must not be stored in contact with amine-terminated adhesives; residual Si-H groups react with primary or secondary amines, increasing hydrogen gas formation and reducing release consistency over 6-month roll storage. The bath life of the two-component coating fluid is set by the inhibitor rather than the hydride source; at 30 °C the viscosity doubling time is typically 8 h to 12 h when the platinum concentration is 100 ppm.
Table 2. Regulatory compliance checklist for RH-H502 in silicone release coatings and textile hydrophobic finishes.
| Application | Regulatory framework | Standard or method | Typical control point |
|---|---|---|---|
| Food-contact release coating | FDA 21 CFR 175.300 | Extraction testing per relevant food-type simulant | Coating weight ≤ 1.2 g/m² |
| Food-contact release coating | Regulation (EU) No 10/2011 | Overall migration | < 10 mg/dm² |
| Electrical/electronic components | Directive 2011/65/EU Annex II | RoHS | Pb < 1000 mg/kg, Cd < 100 mg/kg, Hg < 1000 mg/kg, Cr(VI) < 1000 mg/kg |
| General chemical supply | EC 1907/2006 | REACH SVHC candidate list | Substance content < 0.1 wt% |
| Medical-grade silicone contact | ISO 10993-5 | In vitro cytotoxicity | Cell viability ≥ 70% |
| Textile skin contact | OEKO-TEX Standard 100 | Residual cyclic siloxane control | D4/D5/D6 total < 0.1 wt% |
In high-solids antifoam compounds, RH-H502 functions as both a hydrophobizing agent for fumed silica and a reactive thinning component during the heat-treatment step. A typical production charge in a planetary dissolver with vacuum capability combines polydimethylsiloxane base oil with a kinematic viscosity of 1000 mm²/s at 25 °C, RH-H502 at 4 wt% to 6 wt%, and fumed silica with a BET surface area of 200 m²/g to 300 m²/g at 5 wt% to 8 wt%. The mixture is heated to 150 °C under nitrogen and held for 4 h; during this step, Si-H groups react with isolated silanol groups on the fumed silica surface, releasing hydrogen and producing a methyl-siloxane surface layer. Residual hydrogen is stripped under 50 mbar vacuum for 30 min before discharge. The resulting compound is evaluated by dispersing 0.1 wt% in an aqueous alkylaryl sulfonate foam solution using a recirculating pump test stand; bubble collapse time is measured under ASTM E2407-04. Branched RH-H502 provides a higher number of surface-reactive sites per molecule than linear methyl hydrogen silicone oil, which improves silica wetting at the same addition level but also increases the risk of irreversible gelling if the reaction temperature exceeds 170 °C or if alkali metal hydroxide catalyst is present above 0.5 wt%. For downstream emulsification, the compound is dispersed into water at 60 °C with an ethoxylated isotridecanol emulsifier at HLB 10 to 12, using a high-pressure homogenizer at 300 bar to reach an emulsion particle size below 5 µm.
In phenyl silicone LED encapsulants, RH-H502 is used as a branched hydride crosslinker for vinyl-functional phenyl polysiloxane resins with refractive index between 1.50 and 1.54. The platinum catalyst concentration is limited to 2 ppm to 5 ppm to avoid darkening under thermal aging. Because phenyl substitution raises steric hindrance around the vinyl groups, the SiH/SiVi molar ratio is set at 1.5:1 to 2.0:1, higher than in aliphatic LSR. The encapsulant is dispensed after vacuum degassing at 25 °C and cured in two stages: 100 °C for 1 h to prevent wire sweep, then 150 °C for 4 h to complete hydrosilylation. The cured material is tested for optical transmittance under ASTM D1003-21 at 450 nm; values above 95% at 2 mm thickness are typical when the hydride is fully consumed and no platinum colloidal precipitation occurs. Thermal aging at 150 °C for 1000 h under JIS C 60068-2-2 reveals a characteristic limitation: excess branched Si-H crosslinker increases hardness to Shore D 60 or higher but reduces elongation at break below 20%, making the encapsulant prone to cracking on gold wire bonds during thermal shock from -40 °C to 100 °C under JEDEC JESD22-A104. For this reason, the upper SiH/SiVi boundary is not driven by residual hydride alone but by the modulus limit that the wire-bond assembly can tolerate without delamination. Low outgassing is evaluated by headspace GC-MS after 0.1 g sample is heated to 150 °C for 30 min; cyclic siloxane D4/D5/D6 content above 0.1% of sample mass is a rejection criterion in sealed optoelectronic assemblies.
Fumed silica in silicone rubber compounds is hydrophobized in situ with RH-H502 during the filler-mixing stage. An internal mixer with intermeshing rotors is charged with the silicone gum, and silica is added in 3 to 4 increments at 40 °C to 60 °C. RH-H502 is then injected at 6 phr to 10 phr relative to the silica mass, and the batch temperature is raised to 120 °C for 30 min to 60 min under a nitrogen sweep to remove water and hydrogen. During this step, the Si-H group reacts with silanol and adsorbed water, which reduces the hydrogen-bonded silica network and prevents crepe hardening. The effect is quantified on a rubber process analyzer using a strain sweep at 60 °C; untreated silica compounds show a Payne effect with storage modulus drop exceeding 40% from 0.1% to 100% strain, while in-situ hydrophobized compounds show a drop below 20%. The branched structure of RH-H502 produces a thicker hydrophobic shell than linear methyl hydrogen silicone oil at the same dosage, but it also introduces a narrow processing window: batch temperatures above 140 °C cause premature crosslinking with residual vinyl groups in the gum, resulting in scrap rates above 5% and increased mixer torque. The dosage of RH-H502 must be determined by the silica silanol density, typically 2.0 SiOH/nm² to 3.0 SiOH/nm² for fumed silica; excess hydride remains in the gum and is available for later addition cure, causing the final Shore A hardness to rise by 3 to 5 points if not subtracted from the total SiH/SiVi calculation.Competitive Methyl Terminated Hydrogen Branched Silicone Oil RH-H502 prices that fit your budget—flexible terms and customized quotes for every order.
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Methyl Terminated Hydrogen Branched Silicone Oil RH-H502 is an Si-H-functional polysiloxane characterized by inert methyl termination at chain ends and a branched siloxane backbone in which hydride groups are distributed across linear D units and branch junctions. The methyl termination avoids the terminal silanol condensation route observed in hydroxyl-terminated silicone intermediates, while the branched hydride architecture increases the average number of reactive Si-H sites per molecule at a given viscosity. In addition-cure silicone formulations, RH-H502 serves as a crosslinker or chain extender that reacts with vinyl-functional silicone polymers through platinum-catalyzed hydrosilylation. Representative product-class specifications include viscosity at 25 °C in the range of 15–40 mPa·s when measured according to ISO 3219:2021, refractive index at 25 °C between 1.395–1.405 per ASTM D1218-21, and density in the range of 0.96–0.99 g/cm³ per ISO 2811-1:2023. The Si-H content for this branched methyl-terminated class is generally specified in the 0.20–0.40 wt% region by alkaline gas-evolution or FTIR-based lot-release methods; lot-specific certificates should be consulted because the value depends on the degree of branching and the ratio of methylhydrosiloxane units. Primary applications include solventless thermal-cure release coatings, liquid silicone rubber, hydrophobic surface modification, and reactive intermediates for hydrosilylation with alpha-olefins or polyethers.
The cure rate and final network density in platinum-catalyzed addition-cure systems are governed by the molar ratio of Si-H to vinyl, catalyst dosage, inhibitor concentration, and the effective temperature ramp. For branched RH-H502, the hydride sites are not sterically uniform: Si-H groups at or near T or Q branch points may exhibit reduced accessibility relative to linear D unit Si-H, but the higher per-molecule functionality can compensate through multiple attachment points. Typical addition-cure formulations using Pt-divinyltetramethyldisiloxane complex at 5–20 ppm Pt and an alkyne or maleate inhibitor require a targeted Si-H:vinyl ratio of 1.0:1 to 1.4:1. At ratios below 1.0:1, the cured network may remain under-cured, producing high solvent extractables and soft elastomer surfaces. At ratios above 1.6:1, residual Si-H can continue to react with atmospheric moisture or active-hydrogen contaminants during storage, shifting release force or causing post-cure. The processing window narrows further in thin-film release coating operations where activation energy for hydrosilylation is supplied by short-residence convection ovens. Differential scanning calorimetry per ISO 11357-1:2023 on a representative branched hydride plus divinyl silicone mixture typically shows an onset of cure exotherm between 60 °C and 80 °C, with peak heat flow between 100 °C and 130 °C; these values shift with inhibitor concentration and catalyst lot. Because the branched structure increases reactive site density without raising viscosity proportionally, formulators can achieve target crosslink density at lower hydride addition levels than with linear polymethylhydrosiloxane of similar molecular weight.
In solventless release coating lines running at 200–400 m/min, the formulation is applied at coat weights of 0.8–1.5 g/m² to corona-treated polyester or glassine substrates using five-roll gravure or offset gravure coaters. The wet coating is then passed through forced-air ovens with web surface temperatures of 120–160 °C and residence times of 3–10 s. Under these conditions, RH-H502-based formulations display rapid hydrosilylation because the branched hydride provides multiple reactive sites for the vinyl-functional release polymer, creating a tightly crosslinked elastomer layer with low extractable silicone. The cured release force against solvent acrylic pressure-sensitive adhesives is commonly measured according to FINAT FTM 3; branched hydride systems are often formulated to maintain stable release in the 5–30 cN/50 mm range after aging at 40 °C for 7 days. However, high humidity during application can hydrolyze residual Si-H, generating hydrogen and reducing cure efficiency; coated substrates exposed to atmospheric moisture before entering the oven may exhibit patchy cure or variable release force. The batch-to-batch variation in branching ratio also influences misting behavior in high-speed coating: excessively branched low-viscosity grades may produce higher mist under gravure roll shear, while insufficient branching reduces the cure response. Production lines using closed-filter systems with 10 µm absolute filtration and nitrogen-blanketed coating pans minimize moisture and particulate interference.
Linear polymethylhydrosiloxane fluids with comparable Si-H content typically have higher linear viscosity per reactive site, because the Si-H density is spread along a single chain. RH-H502 uses a branched siloxane scaffold to package more Si-H units into a low-viscosity molecule with methyl-terminated ends. This structural difference changes cure network topology: linear hydride tends to form extended flexible segments between crosslink sites, whereas branched hydride can form star-like or clustered crosslink nodes. Rheological measurements of cured elastomers prepared from each crosslinker type show higher storage modulus G′ at equivalent formulation solids when RH-H502 is used at matched Si-H:vinyl stoichiometry. In release coatings, the branched architecture lowers the amount of free hydride fluid that can migrate to the adhesive surface after cure, because each RH-H502 molecule contains multiple attachment points and is less likely to remain unreacted. The following comparative table summarizes representative property and performance differences for RH-H502, a linear methylhydrosiloxane fluid, and a non-functional dimethyl silicone oil of similar application viscosity. Values reflect product-class public literature data; lot-specific certificates govern for RH-H502.
| Parameter / test method | RH-H502 branched hydride | Linear PMHS | Dimethyl silicone oil |
|---|---|---|---|
| Viscosity at 25 °C, ISO 3219:2021 | 15–40 mPa·s | 20–40 mPa·s | 50–150 mPa·s |
| Si-H content | 0.20–0.40 wt% | 1.50–1.65 wt% | 0.00 wt% |
| Reactive sites per molecule | High, due to branching | Moderate, chain-length dependent | None |
| Crosslink density at matched Si-H:vinyl | Higher; clustered nodes | Moderate; extended segments | No contribution |
| Extractable silicone after cure | Low | Moderate | High if unreacted |
| Hydrophobic durability | Reactive; forms crosslinked film | Reactive; forms crosslinked film | Non-reactive; surface oil may migrate |
Dimethyl silicone oil is widely used as a temporary hydrophobic agent because it lowers surface energy without forming chemical bonds to most substrates. When a non-reactive polydimethylsiloxane oil is applied to glass, metal, or textile surfaces, the water contact angle may initially exceed 95°, but the film remains extractable by solvent and can migrate under mechanical abrasion. RH-H502 changes the durability mechanism because the Si-H groups can react with surface hydroxyls or be crosslinked into a bonded silicone network after application. For glass treated by wipe-on or dip methods and cured at 120–150 °C for 10–30 min, advancing water contact angles measured per ASTM D7334-08 are frequently in the 100–110° range, comparable to or slightly lower than those of thick dimethyl silicone oil films, but the coating is resistant to solvent extraction. The presence of branched hydride functionality permits curing without additional alkoxysilane adhesion promoters in some glass systems, although silane primers improve humid-age adhesion. The lower hydrogen content relative to linear PMHS reduces the risk of excessive gas evolution during aqueous contact, which is relevant when treating porous mineral substrates where entrapped hydrogen can create pinholes. In textile applications, RH-H502 can be emulsified with nonionic surfactants and applied by padding, but the emulsion must be stabilized at pH 4–7 to avoid rapid Si-H hydrolysis; alkaline conditions above pH 8 liberate hydrogen and cause viscosity drift within hours. Because the hydrophobic performance is reactive, the treated surface must be heat-cured; ambient-cure conditions give incomplete crosslinking and lower abrasion resistance. The product is not recommended for use with amine-containing fabric softeners or sulfur-containing dyestuffs that poison platinum catalysts and inhibit hydrosilylation.
In high-consistency rubber compounding, a branched methyl-terminated hydrogen silicone oil can be incorporated into vinyl-functional silicone gum to adjust crosslink density and to reduce the Payne effect after cure. The low viscosity of RH-H502 allows uniform distribution in internal mixers or on two-roll mills running at 20–40 °C. Because the hydride groups react with vinyl-functional gums over a temperature range of 110–160 °C, the material should be added before the platinum catalyst and inhibitor are fully homogenized to avoid localized gel formation. The branched architecture provides a higher number of crosslink junctions per molecule than a linear dimethyl-co-methylhydrosiloxane chain extender of similar viscosity, which can be used to increase modulus without a proportional increase in compression set. However, too high an addition of branched hydride can embrittle the cured rubber because the clustered crosslink nodes restrict segmental relaxation. Mold release performance in injection molding is affected by the amount of unreacted hydride at the surface; if the Si-H:vinyl ratio exceeds 1.5:1, the surface may continue to react with moisture in the mold and produce intermittent sticking defects. In liquid silicone rubber injection molding machines with clamp forces from 200 kN to 2,000 kN, the low viscosity of RH-H502 supports metering through static mixers, but the hydride component should be kept separate from platinum catalyst until the final mixing section to prevent premature gelation in the manifold. Published data for this exact product in high-consistency rubber is limited, so process trials should screen addition levels from 0.5 wt% to 3.0 wt% relative to the gum weight.
RH-H502 is also used as a hydrosilylation intermediate for the preparation of polyether-modified silicone surfactants and alkyl silicone waxes. In a typical batch reactor equipped with an anchor agitator and nitrogen sparge, the branched hydride is reacted with allyl polyether under platinum catalysis at 80–120 °C. The branched methyl-terminated structure permits the introduction of multiple organic pendant groups while retaining a low initial viscosity; the resulting surfactants exhibit different phase behavior in water compared to linear analogues because the branched silicone backbone alters packing density at the oil-water interface. The reaction exotherm is controlled by slow addition of the olefin over 1–2 h, and the Si-H conversion is monitored by FTIR disappearance of the band near 2160 cm⁻¹. Residual hydride must be quenched or capped before packaging to avoid hydrogen evolution in aqueous formulations. Published data for this specific product configuration in polyether synthesis is limited; therefore, the reaction endpoint should be confirmed by lot-based Si-H titration rather than assuming complete conversion from stoichiometry.
For long-term storage, RH-H502 requires sealed stainless steel or fluoropolymer-lined drums under dry nitrogen. The product should not be stored in carbon steel vessels because iron oxide can catalyze Si-H decomposition, and the liberated hydrogen can pressurize closed containers. Recommended storage temperature is 5–25 °C; exposure to temperatures above 40 °C accelerates siloxane redistribution and shifts the branching ratio. Water contamination above 100 ppm can form silanol intermediates and increase gel content, so transfer operations should use closed-loop pumping with dry nitrogen purge and filters rated at 5–10 µm. Under REACH Regulation EC 1907/2006, a silicone polymer may be exempt from registration as a polymer provided its monomeric constituents are registered; downstream users should confirm the supplier registration status for the specific hydride intermediate. For applications covered by food-contact legislation, compliance with FDA 21 CFR 175.300 or EU 10/2011 must be demonstrated by migration testing on the finished article, not by the bulk product certificate alone. RoHS Directive 2011/65/EU restrictions apply to the final electrical/electronic product; RH-H502 is not a typical source of the restricted heavy metals.
| Requirement / standard | Designation / test method | Relevance to RH-H502 |
|---|---|---|
| REACH registration | EC 1907/2006 | Confirm monomer/polymer status with supplier |
| RoHS restricted substances | 2011/65/EU | Applies to finished electrical/electronic articles |
| Food-contact coatings | FDA 21 CFR 175.300 | Requires migration testing on finished article |
| Rubber classification | ASTM D1418-22 | Used in addition-cure VMQ/PVMQ systems |
| Cure thermal analysis | ISO 11357-1:2023 | Determine onset and peak heat flow of cure exotherm |
| Viscosity | ISO 3219:2021 | Release specification for incoming QC |