| HS Code | 956679 |
| Appearance | Translucent/white viscous liquid |
| Density G Cm3 | 1.10-1.15 |
| Viscosity 25c Mpa S | 15000-25000 |
| Hardness Shore A | 30-40 |
| Tensile Strength Mpa | ≥6.0 |
| Elongation At Break Percent | ≥350 |
| Tear Strength Kn M | ≥20 |
| Dielectric Strength Kv Mm | ≥20 |
| Volume Resistivity Ohm Cm | ≥1×10^14 |
| Dielectric Constant 50hz | ≤3.0 |
| Dissipation Factor 50hz | ≤0.01 |
| Tracking Resistance Kv | ≥4.5 |
| Flame Retardancy | UL94 V-0 |
| Service Temperature C | -50 to 200 |
| Curing Condition | 170 °C × 10 min |
| Curing Type | addition-cure platinum catalyzed |
As an accredited Insulator Liquid Silicone Rubber RH-G6031-1 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaged in 20 kg sealed plastic pails or drums, suitable for safe storage and transport of RH-G6031-1 insulator liquid silicone rubber. |
| Container Loading (20′ FCL) | 20′ FCL container loaded with Insulator Liquid Silicone Rubber RH-G6031-1, packed in sealed drums, palletized, and securely lashed for transport. |
| Shipping | Insulator Liquid Silicone Rubber RH-G6031-1 is shipped in sealed, labeled pails or drums, protected from moisture, contamination, and temperature extremes. Handle according to its SDS; use standard freight with proper documentation and spill precautions unless classified otherwise. |
| Storage | Store Insulator Liquid Silicone Rubber RH-G6031-1 in its original, tightly closed container in a cool, dry, well-ventilated area, away from direct sunlight, heat, ignition sources, moisture, and incompatible materials such as oxidizers and acids. Protect from freezing and excessive temperature fluctuations. Maintain good housekeeping, observe shelf-life, and follow local regulations. |
| Shelf Life | Shelf life is typically 12 months from manufacture when stored unopened in a cool, dry place, away from sunlight and moisture. |
In transmission-class composite suspension and tension insulator housings, RH-G6031-1 is metered as a two-part addition-cure liquid silicone rubber at a volumetric ratio of 1:1 through a 10–16 element static mixer mounted directly on the injection gate. Piston-metering systems should hold shot-to-shot dosing variation below 1%, because uneven stoichiometry from worn check valves shifts the hydrosilylation cure and creates soft interfaces in the shed-to-sheath transition. The mixing head must be cooled below 30 °C; pot life of mixed A/B at 25 °C is in the range of 12–24 h, but heated runner sections above 80 °C reduce open time to minutes. ATH-filled insulator LSR grades with a filler loading around 60–80 phr exhibit a viscosity between 80 Pa·s and 150 Pa·s at 10 s⁻¹. Injection pressure at the gate should be 3–8 MPa; clamp force on a 110 kV suspension insulator mold with 2–4 cavities is typically 200–350 t (1.96–3.43 MN). Air venting at the shed root and along the sheath surface should maintain cavity pressure below 0.2 MPa to prevent void formation. On vertical presses below 200 t, full-flow fronts may hesitate at the shed-to-core transition, producing trapped gas pockets that exceed 100 µm in diameter and reduce impulse puncture strength.
Cure temperature is profiled from 120 °C at the core to 160 °C at the outermost shed. Centre-of-mass cure for a 25 mm shed cross-section reaches demoldable Shore A 35–45 in 180–240 s. Post-cure at 200 °C for 4 h completes hydrosilylation, reduces volatile siloxane content, and stabilizes dielectric loss below 0.002 at 50 Hz under ASTM D150. The terminal housing is assembled with forged steel end fittings and crimped onto the FRP core to produce suspension and tension composite insulators rated 110 kV to 220 kV under IEC 61109. Tracking erosion resistance is confirmed by IEC 60587 at 4.5 kV using 0.1% NH₄Cl at 0.6 mL/min; erosion depth is assessed below 2.5 mm.
| Property | Standard / Test condition | Acceptance benchmark |
|---|---|---|
| Tracking resistance | IEC 60587 Method 2A, 4.5 kV, 0.1% NH₄Cl | Pass 6 h, erosion ≤2.5 mm |
| Dielectric strength | ASTM D149, 50 Hz, 2 mm sheet | ≥20 kV/mm |
| Volume resistivity | ASTM D257 | ≥1×10¹⁴ Ω·cm |
| Hardness | ASTM D2240 | 35–45 Shore A |
| Tensile strength | ASTM D412 | ≥6 MPa |
| Elongation at break | ASTM D412 | ≥350% |
| Tear strength | ASTM D624 Die B | ≥18 N/mm |
| Dissipation factor | ASTM D150, 50 Hz | ≤0.005 |
Mandrel-wound glass-reinforced epoxy cores used in hollow composite insulators have surface porosity and residual amine species that interfere with platinum-catalyzed addition cure. The FRP core should be post-cured above 130 °C for 6 h, surface ground with 80–120 grit alumina, and cleaned with anhydrous isopropanol before primer application. RH-G6031-1 is overmolded at 1:1 ratio with an adhesion promoter added at 0.5–1.0 phr to the B component. A silane-grafted primer with methacryloxy functional groups couples the LSR to the glass-epoxy matrix. Without primer and low amine surface activity, interfacial peel strength under IEC 62217 thermal-mechanical stress falls below the bond-line requirement and flashover risk increases.
Rotating core molding machines with 4 independent heating zones are used for hollow insulator shed overmolding. Barrel temperature is held below 25 °C, while mold temperature at the core interface is limited to 130–140 °C to avoid thermal expansion mismatch between steel tooling and the FRP tube. Injection pressure is set to 2–5 MPa and injection speed is profiled to push the flow front across the shed root without jetting. The mixed compound is degassed in-line at ≤20 mbar and filtered through a 100 µm screen before entering the cavity. The resulting part is a hollow core composite insulator body rated 126 kV with shed spacing designed to IEC 60815 pollution class III.
On production lines, the most frequent failure mode is catalyst inhibition at the first 2–3 mm of the bond-line where epoxy amine bloom persists. Infrared surface inspection or dye penetrant field data show that uncured interfacial film increases dielectric loss at 1.2 U₀. Compression set after 22 h at 150 °C should remain below 20% for flange sealing. Final flange assemblies are tested according to IEC 61462 for hollow composite insulators and IEC 61109 for dielectric type tests.
Partial discharge inception in 15 kV and 35 kV separable connectors is governed by void density at the XLPE–silicone rubber interface and by dissipation factor of the stress cone elastomer. RH-G6031-1 is processed at 1:1 ratio with additional batch degassing at ≤1 mbar for 10–15 min in a thin-film rotary degasser before injection. The metering system must maintain component viscosity ratio ≤1.2 because unbalanced flow through a 12-element static mixer generates striation defects. These defects appear as optical haze and raise apparent charge above 5 pC at 1.73 U₀ in a shielded room test under IEC 60270.
The injected stress cone requires low dielectric constant, low dissipation factor, and stable compression set. Dielectric constant is measured between 2.8 and 3.1 at 60 Hz under ASTM D150. Dissipation factor is kept below 0.005 at 50 Hz. Compression set after 22 h at 150 °C should be ≤20% so that interfacial pressure on the XLPE cable does not relax below design value. Vacuum degassing equipment must maintain the mixed premix below 5 mbar immediately before injection; any pressure rise above 20 mbar indicates moisture or low-molecular-weight siloxane devolatilization and requires a longer venting step.
Cold-runner injection tooling with pneumatic needle shut-off is preferred. The gate is placed at the high-field region opposite the cable insertion bore to avoid knit-line partial discharge sites. Mold temperature is held at 140 °C; injection pressure at the gate is 4–8 MPa. Cure time for a 15 mm thick stress cone is 60–120 s, followed by post-cure at 200 °C for 2 h. The finished cable accessory is tested under IEEE 386 or IEC 60502-4 for partial discharge below 5 pC at 1.73 U₀ and for withstand voltage at 2.5 U₀ for 30 min.
During direct molding of station-class surge arrester housings over 10 kA metal-oxide varistor stacks, RH-G6031-1 must accommodate aluminium flange tolerance stack-up and a tangential surface gradient up to 0.5 kV/mm under wet pollution. The material is injected on a multi-cavity aluminium tool at 150 °C with gate pressure limited to 2–6 MPa. Alternating large and small sheds create undercuts that require tear strength above 18 N/mm under ASTM D624 Die B; lower tear strength leads to de-molding fractures at the small-diameter shed root and creates partial discharge sources in service.
Tracking and erosion performance is evaluated by IEC 60587 at 4.5 kV with 0.1% NH₄Cl and 0.6 mL/min contaminant flow for 6 h. Erosion depth is controlled below 2.5 mm, and tracking current should not exceed 60 mA for a 50 mm test distance. Polymer surge arresters are type-tested to IEC 60099-4, including short-circuit mechanical strength and thermal charge. Hydrophobicity recovery after surface corona at 80% relative humidity is checked under IEC TS 62073; receding contact angle should recover above 80° within 72 h after contamination.
The LSR injection barrel is held below 25 °C to avoid precure during charge and recharge cycles. Shot volume is sized to 105–110% of cavity volume to compensate for flash and to maintain packing pressure at 0.5–1.0 MPa during crosslinking. Finished surge arrester housings are assembled with venting seals at the lower flange to prevent moisture ingress; the terminal product covers distribution and station-class arresters from 3 kV to 220 kV.
Resin-impregnated paper (RIP) and oil-impregnated paper bushings use LSR shed profiles to increase creepage distance without increasing porcelain mass. At 500 kV, the shed root is the highest erosion risk because contamination accumulates at the flange transition and concentrates electrical stress. RH-G6031-1 should be qualified for 14–16 mm of creepage per kV under IEC 60815 pollution class IV. Inclined-plane testing under IEC 60587 at 4.5 kV for 6 h with 0.1% NH₄Cl and 0.6 mL/min flow should show erosion depth no greater than 2.5 mm and total failure time beyond 6 h.
Vertical injection of LSR sheds onto a RIP condenser core requires a low-clamp-force tool because the core surface compression limit is 0.5 MPa. The tool is heated to 130–150 °C and injection is performed at 3–6 MPa. Gate locations are positioned at alternating shed roots to prevent weld lines in the highest tangential field regions. Post-cure at 200 °C for 4 h removes residual siloxane species that could contaminate mineral oil in oil-impregnated bushings. However, continuous mineral-oil immersion above 100 °C is not recommended for this grade; fluorosilicone or oil-resistant barriers are required for lower, oil-submerged sections.
Bushing shed profiles are tested for wet power-frequency withstand and lightning impulse under IEC 60137. Partial discharge at 1.5 U_m should remain below 10 pC. Thermal cycling from -40 °C to +80 °C for 100 cycles should not develop cracks at the shed root; adhesion is verified by a 90° peel test exceeding 2.5 N/mm. Terminal hardware is assembled with corona rings to grade the first and last shed boundary fields.
Outdoor metering units and control winding assemblies use RH-G6031-1 as an insulating encapsulant where a soft, high-voltage-enduring layer is required between primary and secondary circuits. The A/B components are mixed at 1:1 by weight and degassed at ≤2 mbar until the foam cap settles, typically 10 min for a 500 g batch. The mixture is poured into an epoxy-coated housing preheated to 80 °C, then cured at 120 °C for 30 min in a vented oven. Exotherm is less than 15 K on a 500 g shot, avoiding thermal stress on ferrite cores and reducing cracking in the secondary winding encapsulation.
Electrical acceptance testing follows IEC 61869-1 for instrument transformers and ASTM D149 for dielectric strength. Volume resistivity under ASTM D257 should remain above 1×10¹⁴ Ω·cm after 168 h at 85 °C and 85% relative humidity. Partial discharge under IEC 60270 at 1.2 U_m is controlled below 5 pC. Because the potting layer is non-structural, the housing must provide mechanical support; continuous tensile load on the encapsulant should not exceed 0.1 MPa. The terminal product is an outdoor metering transformer rated from 11 kV to 35 kV.
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The product RH-G6031-1 is formulated as a two-part, platinum-catalysed addition-cure liquid silicone rubber intended for high-voltage electrical insulation components. The A and B components are designed for metered mixing at a 1:1 volumetric ratio and are supplied with a mixed viscosity suitable for closed-loop injection moulding. In cured form, the grade typically exhibits a Shore A hardness of 28–34 when tested to ASTM D2240, tensile strength above 6.5 MPa per ISO 37:2017, and elongation at break above 450%. Because cure proceeds by hydrosilylation rather than peroxide decomposition, the cured network releases no acidic condensation by-products and does not require immediate oven post-cure for many low- and medium-voltage applications. However, for high-voltage service, a post-cure cycle at 200°C for 2 h is commonly applied to stabilise dielectric loss and remove low-molecular-weight siloxane fractions. Typical components include silicone rubber housings for composite insulators, surge arrester skirts, transformer bushing covers, cable stress cones, and joint bodies.
The electrical performance envelope is defined by volume resistivity, dielectric strength, tracking resistance, and erosion resistance. Representative cured sheet specimens show volume resistivity above 1×1015 Ω·cm when measured according to ASTM D257 at 500 V DC. Dielectric strength for 2 mm specimens in transformer oil can exceed 20 kV/mm using IEC 60243-1; published data for this specific configuration is limited, and acceptance values should be established on production tools rather than extrapolated from laboratory plaques. Under IEC 60587 inclined-plane tracking at 3.5 kV, comparable addition-cure insulator LSR grades commonly achieve 1A 3.5 or 1A 4.5 classifications when the filler package includes alumina trihydrate. The RH-G6031-1 grade incorporates a mineral filler system intended to reduce carbon track formation, but the exact filler composition is not disclosed in publicly available technical literature.
| Property | Test method | Typical value |
|---|---|---|
| Mixed viscosity at 25°C, 10 s⁻¹ | ISO 3219 | 50–150 Pa·s |
| Shore A hardness | ASTM D2240 | 28–34 |
| Tensile strength | ISO 37:2017 | ≥6.5 MPa |
| Elongation at break | ISO 37:2017 | ≥450% |
| Specific gravity | ISO 2781:2018 | 1.30–1.45 |
| Dielectric strength, 2 mm specimen | IEC 60243-1 | ≥20 kV/mm |
| Volume resistivity | ASTM D257 | ≥1×1015 Ω·cm |
These values are representative laboratory data and are not batch release limits; acceptance on a particular production tool should be determined by validated process capability studies.
When processed on a production-scale horizontal injection moulding machine with a clamp force of 120–180 t and a 1:1 dosing unit, the mixed material is conveyed through a static mixer with 12–16 elements and an L/D ratio of 10:1 to 14:1. Injection pressure at the machine nozzle is typically held below 120 bar, and the mould cavity is evacuated to at least -0.8 bar before injection to prevent void formation in thick-section bushings. The practical pot life at 25°C is 24–48 h, but this interval shortens to less than 4 h at 40°C. Cure at 120°C produces sufficient green strength for demoulding in 60–120 s depending on part thickness; the material is not a fast-curing grade designed for connector seals and should not be pushed below 45 s without rheometer confirmation on the production tool.
The mixed system exhibits a viscosity at 25°C of 50–150 Pa·s when measured on a rotational rheometer at a shear rate of 10 s⁻¹ according to ISO 3219. This viscosity range provides sufficient fluidity for meter-mix dispensing while retaining adequate green strength for demoulding. On a production line with a piston dosing pump, volumetric ratio accuracy should be maintained within ±1.5%; ratio drift beyond ±3% typically shifts Shore A hardness by 2–4 points and can alter dielectric strength. Continuous static mixers should be inspected for filler accumulation, and the mixing tube should be purged at the end of each shift.
Uncured components should be stored at 5–30°C in sealed containers. The manufacturer-specified shelf life for the A and B components is 12 months from the date of batch certification when stored unopened. At temperatures below 0°C, the B component may increase in viscosity because of polymer-chain interactions; warming to 25°C before metering is required, but localised heating above 60°C can destroy the platinum catalyst in the A component.
The primary difference is in cure chemistry. Peroxide-cured high-consistency silicone rubber liberates acidic residues from dicumyl peroxide or bis(2,4-dichlorobenzoyl) peroxide, which can corrode metallic inserts in outdoor insulators. RH-G6031-1, by contrast, cures via platinum-catalysed hydrosilylation between vinyl and Si-H functional groups. Network formation releases no low-molecular-weight acidic species. The cost is a stricter contamination boundary: sulphur, amines, and organotin compounds can poison the platinum catalyst, whereas peroxide systems are less sensitive to these species. In return, the mixed viscosity of RH-G6031-1 permits fully automated injection moulding, eliminates milling and preforming, and allows lower cure temperatures of 120–160°C compared with 150–200°C for many high-consistency rubber grades.
Compared with general-purpose addition-cure LSR, the insulation-grade filler package raises tracking resistance but increases mixed viscosity and typical specific gravity from around 1.08 to 1.30–1.45. Tensile strength and elongation may fall below unfilled general-purpose LSR, but electrical performance is prioritised. General-purpose LSR often uses fumed silica reinforcement without alumina trihydrate, giving tensile strength of 9–11 MPa and elongation of 600–900%. The RH-G6031-1 insulation filler package lowers elongation to the 450% range and raises specific gravity, but improves arc resistance and resistance to carbon tracking. Mechanical tear strength is therefore not the primary selection criterion for high-voltage insulator housings.
Field and production-line observations on similar ATH-filled liquid silicone rubbers indicate that the most frequent processing defect is not cure inhibition but vacuum vent clogging from filler sedimentation during extended dwell times. When the mixed charge remains in a static mixer at 25°C for more than 48 h, viscosity can increase by 15–30% and filler can deposit in low-flow regions, causing shot-weight drift and dielectric weak points. Operators should purge mixers after production stops longer than 12 h. A second observed failure mode is delamination at moulded-in metal fittings when mould temperatures fall below 110°C because self-adhesion promoters do not reach full reaction at the metal interface. For primerless adhesion to aluminium or steel inserts, a minimum interfacial temperature of 120°C is recommended during cure.
The operational ceiling of RH-G6031-1 should be defined by the endurance of the ATH filler and the hydrophobicity recovery properties of the silicone network. ATH begins to release water of hydration at approximately 180–220°C, which can create internal steam pressure in thick sections if the part is exposed to sustained overtemperature. Published data for this specific grade is limited; laboratory thermogravimetric analysis on comparable insulator LSRs shows mass loss onset near 220°C, with rapid decomposition above 350°C. Under continuous service, the material should not be specified for conductor temperatures exceeding 150°C without verification of filler stability and dielectric performance. For outdoor insulation, hydrophobic recovery after corona or pollution exposure is a critical property; typical cured silicone surfaces restore contact angle above 90° after 6–24 h at 25°C, but heavily ATH-filled grades may exhibit slower recovery than unfilled silicones.
For a transformer bushing cover with a wall thickness of 20 mm, the cure cycle should not be shortened by raising the mould above 170°C; the exothermic hydrosilylation reaction can push the core temperature above 200°C and cause spongy centres or post-demoulding blowouts. Production lines often use a step cure: 15 min at 120°C followed by 2 h at 180°C. Published data for this specific configuration is limited, but thermal modelling of similar addition-cure LSR parts supports the use of a lower initial mould temperature for thicker sections.
Regulatory compliance for the uncured liquid and cured elastomer is documented against EU RoHS Directive 2011/65/EU Annex II, REACH Regulation (EC) No 1907/2006, and China GB/T 26572-2011 electronic pollution control requirements for restricted substances. The cured elastomer can be tested to IEC 62631-3-1 for dielectric and electrical insulating properties; however, compliance with IEC 62217 for polymeric outdoor insulators applies to the complete insulator design, not to the raw silicone rubber alone.
| Regulatory dimension | Standard or directive | Applicability |
|---|---|---|
| Restriction of hazardous substances | EU RoHS Directive 2011/65/EU Annex II | Uncured and cured elastomer |
| SVHC communication duty | REACH Regulation (EC) No 1907/2006 | Batch documentation |
| Electronic pollution control | China GB/T 26572-2011 | Cured component |
| Polymeric outdoor insulator design | IEC 62217 | Complete insulator system |
Cure inhibition in addition-cure LSR occurs when catalyst poisons such as amines, sulphur-containing curing agents, tin salts, or phosphorus compounds migrate from gaskets, tooling O-rings, substrates, or operator gloves into the silicone. On production lines, inhibition often manifests as a sticky surface layer at depths of 0.05–0.20 mm while the bulk material cures normally. Substrates and tooling must be free of amine-based epoxy release agents, sulfur-cured rubber cord stock, and PVC stabilisers. On automated lines, polyurethane or polyolefin gloves are used; latex and nitrile gloves can contain accelerators that poison hydrosilylation. A wipe test with isopropanol after demoulding is used to detect smearing: if silicone residue transfers to a white cloth, the surface has not reached full cure. This is a production control, not a standardised test method, and should be supplemented by ISO 6502 rheometer verification of the mixed batch.