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| HS Code | 388262 |
| Material | Silicone (polysiloxane) |
| Chemical Structure | Alternating silicon-oxygen backbone with organic groups (typically methyl) attached to silicon |
| Physical State At Room Temperature | Solid, rubbery, gel, or liquid depending on molecular weight and crosslinking |
| Appearance | Transparent to translucent or white; optically clear in some forms |
| Density | Approximately 1.0 to 1.3 g/cm³ |
| Operating Temperature Range | -60°C to +230°C continuously (up to 300°C short-term for some grades) |
| Thermal Conductivity | Low, typically 0.1 to 0.2 W/(m·K) |
| Electrical Property | Excellent electrical insulator with high dielectric strength |
| Water Repellency | Highly hydrophobic; low surface energy repels water |
| Chemical Resistance | Resistant to water, oxygen, ozone, and many chemicals; can swell in some solvents |
| Mechanical Elasticity | Highly flexible with low modulus and good rebound elasticity |
| Gas Permeability | Permeable to gases and moisture vapor |
| Biocompatibility | Generally inert, non-toxic, and used in medical and food contact applications |
| Uv And Weathering Resistance | Excellent resistance to ultraviolet radiation and outdoor weathering |
As an accredited Silicone factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Silicone is packaged in sealed 25 kg pails or 200 kg drums, with sturdy lids and clear hazard labeling. |
| Container Loading (20′ FCL) | Loading silicone into a 20′ FCL involves securing drums or cartons with dunnage, protecting from moisture, and ensuring safe, stable stowage. |
| Shipping | Silicone is typically shipped as non-hazardous cargo in sealed drums, pails, or totes. Protect containers from punctures and extreme heat. Keep away from moisture and incompatible materials. Use proper labeling and secure loading to prevent shifting. No UN dangerous goods classification applies unless formulated with additives, so verify Safety Data Sheet before transport. |
| Storage | Store silicone products in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and strong oxidizing agents. Keep containers tightly sealed to prevent contamination or moisture uptake. Avoid extreme temperatures; ideal range is typically 15–30°C. Follow specific manufacturer guidance, as uncured sealants may require low humidity and proper ventilation. |
| Shelf Life | Silicone’s shelf life is typically 6–24 months unopened if stored cool, dry, and away from sunlight and moisture. |
On 230 kV composite insulator lines, hydrophobic recovery after pollution is a measurable maintenance interval driver. The coating is a one-part room-temperature vulcanizing polydimethylsiloxane dispersion filled with fumed silica at 3 wt% to 8 wt% and alumina trihydrate at 30 phr to 60 phr. The mix is applied by airless spray at 0.6 MPa to 0.8 MPa output pressure over a silane-primed porcelain or glass substrate. Wet film thickness is controlled to 300 µm to 500 µm. Dry films below 200 µm show early erosion under inclined-plane tracking. The low molecular weight siloxane fraction migrates through the pollution layer and restores hydrophobic class HC1 within 24 h to 48 h of wetting, as measured per IEC TS 62073. Tracking and erosion resistance is tested per IEC 62217. Volume resistivity is measured to 1 × 10^15 Ω·cm per ASTM D257. Full cure proceeds by atmospheric moisture diffusion. At 23 °C and 50 % RH, skin-over time is 10 min to 20 min, and a 2 mm section requires 7 days to reach terminal Shore A hardness. Below 5 °C moisture uptake slows enough to delay the same section beyond 14 days. At RH < 30 %, cure remains incomplete even after 14 days. Acetoxy cure systems release acetic acid during condensation and are avoided in confined metal-clad switchgear. Oxime cure systems are selected for those enclosures because the released ketoxime by-product is less corrosive. The end product is a pollution-rated insulator or surge arrester housing used on transmission lines and 25 kV railway catenary systems. RoHS recast 2011/65/EU restrictions do not govern the cured RTV silicone itself, but solvent-carried formulations must meet local volatile organic compound limits in the application plant.
A polyimide masking tape exposed to 288 °C reflow does not fail by silicone adhesive depolymerization alone. The adhesive is a condensation-cured polydimethylsiloxane gum and MQ silicate resin blend at a resin-to-gum ratio from 60:40 to 80:20. Higher MQ content raises the 180° peel value on stainless steel from 4 N/25 mm to 9 N/25 mm but lowers loop tack and increases transfer residue after 350 °C excursions. The adhesive is coated at 25 µm to 50 µm dry thickness on 25 µm polyimide backing and cured in a forced-air oven at 150 °C for 3 min. Residual benzoyl peroxide catalyst above 0.5 wt% of adhesive solids produces radical scission during reflow and causes peel loss. Peel adhesion is measured per ASTM D3330/D3330M after lamination to a stainless steel panel and after 24 h dwell at 23 °C. A formulation with an 80:20 resin-to-gum ratio retains 60 % to 70 % of initial 180° peel after the 288 °C solder float. A 60:40 ratio may retain 40 % to 50 %. Thermal oxidative degradation follows first-order kinetics after 20 min at 316 °C. Published data for retention beyond 350 °C is limited. The tape is used for wave solder masking on printed circuit boards where the silicone adhesive must survive solder float at 288 °C for 10 s to 15 s. The backing is tested for tensile strength and elongation per ASTM D3759. Sulfur- or amine-containing primers are incompatible because base species inhibit condensation cure and reduce cohesive strength.
Flexible slabstock foam with a water content of 3.0 pphp reaches a viscosity inversion point during rise. The polydimethylsiloxane-polyoxyalkylene copolymer is dosed at 0.8 pphp to 1.5 pphp based on polyol mass. In a continuous slabstock line with a mixing head pressure of 150 bar to 200 bar and throughput above 300 kg/min, the surfactant lowers surface tension from 32 mN/m to 22 mN/m in less than 1 s. The cell walls are stabilized until the polyol-isocyanate gel reaction reaches a complex viscosity above 1 × 10^4 Pa·s. If the surfactant is under-dosed below 0.5 pphp, cell coalescence produces coarse cells and partial collapse before gelation. If the dose exceeds 2.0 pphp, foam stabilizes too strongly, air flow falls below 1.5 ft³/min on ASTM D3574 test G, and shrinkage occurs during cooling because closed cells account for more than 20 % of total cell population. The finished polyurethane foam is tested for indentation force deflection per ISO 3386-1 and density per ISO 845. The silicone polyether branch ratio determines whether the foam cell size distribution is narrow or bimodal. For automotive seating foam with a density of 24 kg/m³ to 32 kg/m³, the surfactant is selected for high hydrogen-bond acceptance to avoid tin catalyst deactivation. In slabstock, the addition point is before the mixing chamber, not as a post-injection stream, because local surfactant concentration above 5 pphp creates soft spots.
| Loading (pphp) | Foam condition | Air flow per ASTM D3574 | Density per ISO 845 |
|---|---|---|---|
| 0.4 | Coarse cells, partial collapse | 6.5 ft³/min | 22 kg/m³ |
| 1.0 | Uniform cell structure | 3.2 ft³/min | 24 kg/m³ |
| 2.0 | Closed cells, shrinkage | 1.2 ft³/min | 27 kg/m³ |
Peristaltic pump tubing is often extruded from addition-cure high-consistency silicone rubber because tensile set after autoclave aging is predictable. The base is a dimethyl silicone elastomer with a platinum catalyst at 10 ppm to 20 ppm metal content and an inhibitor at 0.01 wt% to 0.05 wt%. A two-stage extruder with an L/D ratio of 25:1 is fed at 15 °C to 25 °C to prevent scorch before the die. The die temperature is 120 °C to 160 °C, and line speed is 10 m/min to 30 m/min for 6.4 mm outside diameter tubing. Post-cure at 200 °C for 4 h removes volatile siloxanes and completes addition crosslinking. The extrusion grade has a minimum tensile strength of 8 MPa and elongation at break of 600 % per ASTM D412, with tear strength from 30 kN/m to 45 kN/m per ASTM D624 Die B. Compression set after 22 h at 175 °C must remain below 15 % for pump tubing that is resterilized. The product is tested for cytotoxicity per ISO 10993-5, irritation per ISO 10993-10, and systemic toxicity per USP Class VI. Food-contact approval is limited to FDA 21 CFR 177.2600 and selected EU 10/2011 conditions. The extruder cannot run with nitrile or latex contact surfaces. Sulfur-bearing shop air above 0.1 ppm inhibits platinum cure. The extruded tubing becomes a critical element in peristaltic pumps for cell culture media and blood contact, where spallation and leachables are monitored by HPLC after 70 °C water extraction. Published data for exact spallation particle counts at high line speeds is limited. Wound drainage catheters and enteral feeding sets use the same extrusion grade when the final tube must survive repeated steam autoclave cycles at 121 °C.
Turbocharger intercooler sealing in 2.0 L to 3.0 L diesel platforms places an LSR molding window between 150 °C and 190 °C. The material is a two-part addition-cure liquid silicone rubber with a 1:1 volumetric mix ratio and a platinum complex catalyst. The injection molding machine is equipped with a closed-loop metering pump, an all-electric clamp of 200 t to 500 t, and a cold runner block held below 25 °C. The barrel is maintained at 18 °C to 25 °C, not heated. The mold cavity is heated to 160 °C for a 1.5 mm cross-section. That condition produces a cure time of 30 s to 45 s. If the mold temperature drops below 145 °C, compression set after 22 h at 175 °C rises above 35 % because surface crosslink density is insufficient. At 190 °C to 200 °C, cure time falls to 15 s to 20 s, but flash adhesion in the parting line increases and demolding force becomes unstable. The seal is tested for heat aging per ISO 188 at 175 °C for 1000 h, compression set per ASTM D395 Method B, and hardness per ASTM D2240 at Shore A 40 to 70. Typical tensile strength for a 50 Shore A LSR is 7 MPa to 10 MPa with elongation at break of 400 % to 600 % per ASTM D412. The LSR seal replaces acrylic rubber in charge-air cooler end tanks because the hot-side tank temperature exceeds 180 °C for short transients. Acetal cold runner components are incompatible because formaldehyde released from acetal inhibits platinum cure.
| Mold temperature | Compression set per ASTM D395 Method B | Tensile retention per ASTM D412 |
|---|---|---|
| 135 °C | 38 % | 82 % |
| 160 °C | 18 % | 94 % |
| 190 °C | 12 % | 97 % |
Torsional vibration damper silicone fluid is characterized by high shear stability and a viscosity-temperature coefficient lower than mineral oil. The fluid is a linear polydimethylsiloxane with a kinematic viscosity of 10 000 cSt to 60 000 cSt at 25 °C measured per DIN 51562-1. For a crankshaft damper on a 13 L heavy-duty diesel engine, the fluid is filled under vacuum below -0.095 MPa into a sealed housing and then closed with a rolling elastomeric seal. The fill mass tolerance is ±1.5 wt% of the specified charge. The assembly is tested for sub-synchronous vibration on a dynamometer. The service temperature in the damper cavity reaches 140 °C to 160 °C. The pour point of the silicone fluid remains below -60 °C per ISO 3016. The viscosity index of high-molecular-weight polydimethylsiloxane is typically 250 to 300, compared with 90 to 100 for a mineral damper fluid. Volatility after 24 h at 150 °C must remain below 0.5 % because vapor loss changes damper inertia. Published data for exact evaporation loss at 160 °C in heavy-duty engine service is limited. The fluid is incompatible with hydrocarbon oils and some EPDM seals because linear siloxane swells the elastomer. Fluorosilicone or fluorocarbon seals are used at the damper closure. The end product is a tuned torsional vibration damper that shifts the crankshaft resonant frequency below the engine operating range.
Water-based flexographic inks on corrugated board develop macrofoam in the return line when air entrainment exceeds 3 % by volume. The defoamer is a polydimethylsiloxane with hydrophobized silica particles of 10 µm to 30 µm median size. It is added at the letdown stage, not during pigment dispersion, because a Cowles blade above 1500 rpm strips the silica from the silicone droplet and collapses the defoamer to an inactive oil film. The dosage is 0.1 wt% to 0.5 wt% of the total liquid ink. A dose below 0.05 wt% leaves macrofoam in the ink pan. A dose above 0.6 wt% causes cratering on low-energy coated board and fish eyes in the printed solid. Foam reduction is evaluated per ASTM E2407 at 25 °C. The foam height after 60 s must be reduced by 80 % to 95 %. The ink is used for food-contact packaging only when the specific defoamer is listed under FDA 21 CFR 176.170 or Swiss Ordinance 817.023.21. Not all silicone defoamers carry this clearance. In the printing unit, the defoamer particle size must remain below the anilox cell depth of 80 µm to avoid cell plugging. The addition is made under low shear at 500 rpm to 1000 rpm, and the batch is checked after 15 min for optical density uniformity. Silicone defoamers with a high content of free polydimethylsiloxane above 5 wt% of the defoamer concentrate are avoided in inkjet-grade inks because they migrate to the printhead nozzle plate.
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Polydimethylsiloxane (PDMS)-based silicone elastomers are supplied as moisture-cure one-part RTV-1 sealants, two-part platinum-catalysed RTV-2 encapsulants, peroxide-catalysed high-consistency rubber (HCR), and liquid silicone rubber (LSR). The product is identified by grade family rather than a single model number because cure chemistry, mixed viscosity, and post-cure performance define processing and end-use selection. RTV-2 products are commonly mixed at 10:1 or 1:1 volume ratios with viscosities from 3 to 60 Pa·s; LSR grades are shipped as paired A/B components with mixed viscosity from 200 to 800 Pa·s for injection molding. Across commercial grades, Shore A hardness spans 5 to 80 under ASTM D2240, specific gravity spans 1.05 to 1.55 under ASTM D792, tensile strength ranges from 3.5 to 11 MPa, and elongation at break ranges from 100 to 700 percent under ASTM D412. The siloxane backbone gives a glass transition near −125 °C, but the low intermolecular forces reduce tear resistance relative to polyurethane and nitrile elastomers. Silicone also differs from organic rubbers in its high gas permeability, excellent ozone resistance, and retention of flexibility over a wider temperature interval.
Platinum-catalysed LSR is processed on injection molding machines with heated platens at 110–180 °C; for wall sections between 2 and 5 mm, cure cycle times are typically 30–90 s. The principal production risk is cure inhibition. Sulfur-containing gloves, amine-based mold releases, natural rubber residues, certain PVC plasticizers, and contact with tin-catalysed condensation silicone can poison the hydrosilylation catalyst and leave a tacky, uncured surface even when the interior is crosslinked. Metering is performed by positive-displacement pumps through a static mixer; on a 100-tonne clamp machine, LSR cavity pressure remains lower than 35 MPa because the material flows in thin sections without the packing force required by thermoplastic melts. Mixed A/B work life at 25 °C is commonly 24–72 h, but at 40 °C the same material can gel within 4–8 h. Cold-runner blocks are therefore maintained below 60 °C upstream of the gate, while the mold surface is kept above 110 °C to initiate cure. When mold gaps exceed 0.02 mm, LSR flash can generate parted-line contamination that must be removed before the next cycle.
Process audits on liquid silicone molding lines identify three recurring causes of batch-to-batch variance: A/B mixing ratio drift from worn pump seals, moisture uptake in the filler resin, and storage of mixed material in warm plant environments. Mixing ratio drift of more than 2 percent often shifts tensile strength by 5–10 percent and changes cured hardness by 2–4 Shore A points. Because LSR has no solvent carrier, shrinkage during cure is low, but differential shrinkage between thin and thick sections can still produce internal stress if the cavity is packed too early. De-molding is normally performed at 60–80 °C part surface temperature to avoid reversion in confined sections above 200 °C.
Peroxide-cured high-consistency rubber is delivered as milled slab stock with Mooney viscosity ML 1+4 at 100 °C between 20 and 80 MU. It is mixed on two-roll mills at 20–30 °C to disperse fumed silica and to re-soften filler network after storage; storage beyond 6 months typically requires re-milling because stiffening changes flow into compression and transfer molds. Press cure is conventionally 170–180 °C for 5–10 min, followed by air post-cure at 200 °C for 4 h to remove volatile peroxide decomposition residues and to complete crosslinking. HCR is specified for seals that operate above 125 °C in dry air but should not be used in submerged hydrocarbon or ketone service until immersion testing under ASTM D471 confirms acceptable volume swell and property retention. Compared with addition-cure LSR, HCR has higher green strength and can be compression molded as thick blocks; the trade-off is longer cycle time and greater sensitivity to storage-induced hardening.
Compression set measured by ASTM D395 Method B after 22 h at 177 °C is typically 15–40 percent for heat-stabilized silicones, while general-purpose EPDM grades often exceed 50 percent. This difference determines gasket performance in enclosures cycling between −40 °C and 150 °C. The low glass transition prevents low-temperature stiffening, and the siloxane network resists permanent deformation at high temperature. The design constraint is low tear strength. Sharp metal edges, installation radii below 0.5 mm, and flange gaps above 1 mm can initiate cuts because hot tear strength of silicone is lower than that of FKM or HNBR. Durometer is matched to flange flatness: 30–40 Shore A for rough castings and 60–70 Shore A for precision-machined faces. For applications with a processing window narrower than ±5 °C, such as cure reversion in confined sections above 200 °C, published data for long-term seal stability is limited and component-level validation is required.
Silicone is specified as a gasket material when compression set and broad temperature range matter more than tensile strength. Compared with PTFE, silicone is conformable and resilient at low torque, but it cannot match chemical inertness or low friction; PTFE exhibits service temperatures from −200 °C to 260 °C and tensile strength above 20 MPa, but its cold flow requires higher flange loads. Compared with EPDM, silicone has better high-temperature and ozone stability but lower tear resistance and higher gas permeability. Compared with polyurethane, silicone has better UV and ozone resistance but poorer abrasion resistance; polyurethane tensile strength can exceed 40 MPa, while general-purpose silicone typically remains below 11 MPa.
Typical comparative property ranges for elastomer families used in gaskets and seals are provided below. Values are obtained from published supplier data sheets using the listed methods.
| Test method | Heat-stabilized silicone | EPDM | FKM | NBR |
|---|---|---|---|---|
| ASTM D2240 hardness | 20–80 Shore A | 30–90 Shore A | 40–95 Shore A | 30–95 Shore A |
| ASTM D412 tensile strength (MPa) | 5–10 | 7–21 | 6–14 | 7–20 |
| ASTM D412 elongation at break (%) | 100–700 | 100–600 | 100–350 | 200–600 |
| ASTM D624 die B tear strength (kN/m) | 15–45 | 25–50 | 15–40 | 25–60 |
| ASTM D395 compression set after 22 h at 100 °C (%) | 10–30 | 25–40 | 20–35 | 25–45 |
Long-term hot-air aging of silicone rubber at 150 °C for 1000 h generally retains more than 70 percent of initial tensile strength and elongation when measured to ASTM D573. At 200 °C, retention depends on the stabilizer package and filler type; some iron oxide and cerium oxide stabilized compounds show acceptable elongation retention, while unstabilized grades may harden and lose flexibility within 500 h. The brittle point under ASTM D2137 remains below −60 °C for general-purpose grades, but phenyl-modified silicones extend low-temperature flexibility to −100 °C and below at the expense of higher viscosity and narrower processing windows.
Addition-cure RTV-2 silicones are used as potting and conformal coatings where bond-line temperatures exceed 125 °C. Typical dielectric strength is 20–25 kV/mm under IEC 60243-1, volume resistivity is 1×10¹⁴ to 1×10¹⁶ Ω·cm under ASTM D257, and dissipation factor at 50 Hz is below 0.001. Compared with rigid polyurethane potting resins, silicones generate lower cure exotherm and lower stress on solder joints during thermal cycles between −40 °C and 125 °C. Lap shear strength of unfilled grades is generally below 2 MPa; structural bonding requires a silane primer or plasma treatment. Dispensing through 18–25 gauge needles at 2–6 bar is standard, but mixed pot life must be re-verified when ambient relative humidity exceeds 60 percent because moisture can destabilize the platinum catalyst. The product also has lower thermal conductivity than epoxy alternatives, typically 0.2–0.3 W/m·K, so high-power modules may require filled thermal grades or a thinner bond line.
Medical and food-contact silicone parts are specified as platinum-catalysed, post-cured grades to avoid peroxide residuals and condensation-cure by-products. Cytotoxicity is screened under ISO 10993-5, sensitization under ISO 10993-10, and systemic biocompatibility under USP <88> Class VI. Food-contact grades are tested under FDA 21 CFR 177.2600 or BfR Recommendation XV. Tubing formulated to 50–70 Shore A with tear strength above 30 kN/m under ASTM D624 is used in peristaltic pumps because the material recovers from repetitive compression. Silicone is not appropriate for continuous transfer of nonpolar solvents or silicone-swelling fluids unless immersion testing to ASTM D471 at the service temperature produces acceptable volume swell and property retention data.
Typical compliance matrix for silicone grades used in regulated applications includes the following test designations.
| Application | Standard or regulation | Typical grade condition |
|---|---|---|
| Food-contact articles | FDA 21 CFR 177.2600 | Post-cured addition-cure or peroxide-cured |
| Medical device components | ISO 10993-5, USP <88> Class VI | Platinum-cured, post-cured LSR or HCR |
| Electrical insulation | IEC 60243-1, ASTM D257 | Dielectric strength ≥20 kV/mm, volume resistivity ≥1×10¹⁴ Ω·cm |
| Flame-retarded enclosure seals | UL 94 V-0 | Halogen-free silicone with mineral fillers |
Unfilled silicone surfaces have low surface free energy, typically 22–24 mN/m, which limits direct adhesion to metals, glass, and engineering thermoplastics. Bonding processes use plasma, corona discharge, or organosilane primers applied at a dry film thickness below 5 µm before molding or bonding. In lap shear coupons prepared from 2 mm slabs adhered to aluminum with a silane primer, cohesive failure at 1–2 MPa under ASTM D1002 is typical, while untreated surfaces may fail adhesively below 0.1 MPa. The specific primer selection depends on substrate chemistry: methacryloxy and glycidoxy silanes are used on glass and metal, and amino silanes are used on some filled polyamides. Each additional primer in a medical device is assessed under ISO 10993-1 because the extractable profile changes after surface treatment. Manufacturers must also control humidity during primer application; moist conditions above 60 percent RH promote condensation of silanol groups and reduce bond reproducibility.
Extruded and injection-molded LSR tubing is produced with wall-thickness tolerances near ±0.15 mm for diameters up to 12 mm and ±0.25 mm for larger sizes, measured according to ISO 3302-1. Pump trials on peristaltic platforms at 10–20 percent occlusion show that silicone tubing often maintains flow stability over 500 h continuous running, but performance depends on pump geometry, roller speed, and fluid backpressure. Compared with PVC, silicone contains no phthalate plasticizers and offers higher temperature tolerance; compared with thermoplastic elastomer tubing, silicone exhibits broader low-temperature flexibility but lower tensile strength and higher gas permeability. Oxygen and carbon dioxide permeation through silicone can be 10–20 times higher than through butyl rubber, which makes silicone appropriate for respiration circuits but unsuitable for long-term beverage gas-barrier lines.
Chemical resistance boundaries are determined by solubility parameter mismatch. General-purpose PDMS swells in nonpolar aliphatic and aromatic hydrocarbons, ketones, chlorinated solvents, and some ester-based hydraulic fluids; volume swell in mineral oil at 100 °C typically exceeds 20 percent. Silicone is resistant to hot water, steam, dilute alkali, salt solutions, and many polar organic compounds. For aggressive fluid seals, fluorosilicone or FKM should be evaluated rather than general-purpose PDMS. When condensation-cure RTV-1 is specified for electrical enclosures, acetic acid-releasing grades should not be used on copper traces or brass fittings; neutral oxime or alcohol-cure RTV-1 grades are selected for those substrates.