| Код ТН ВЭД | 985775 |
Как аккредитованная DSM Somos ProtoGen™ 18120 эпоксидная смола для стереолитографии, UV Postcure на заводе HOC-2, мы соблюдаем строгие протоколы качества - каждая партия подвергается строгим испытаниям для обеспечения последовательных стандартов эффективности и безопасности.
| Упаковка | Typically supplied in a 5 kg opaque plastic bottle, sealed and protected from UV light; store in original packaging. |
| Погрузка контейнера (20-футовый контейнер) | 20′ FCL loading of DSM Somos ProtoGen™ 18120 Epoxy Resin for stereolithography, UV postcure at HOC -2, in chemical-compliant containers. |
| Доставка | DSM Somos ProtoGen™ 18120 is typically not regulated for transport by DOT, IATA, or IMDG. Ship as a non-hazardous liquid in sealed, UN-approved containers at ambient temperature, protected from UV, heat, and oxidizers. Verify current SDS Section 14 and carrier requirements before shipping. |
| Хранение | Store DSM Somos ProtoGen™ 18120 at HOC-2 in original, sealed, upright containers in a cool, dry, well-ventilated area. Protect from UV light, sunlight, heat, sparks, flames, and moisture. Keep away from oxidizers, acids, bases, amines, and food/water. Maintain 15–30°C; do not freeze. Keep containers closed when not in use. Label clearly. Use secondary containment. Dispose of waste per regulations. |
| Срок годности | Shelf life is 12 months from date of manufacture when stored at 25°C (77°F) in original, unopened containers. |
DSM Somos ProtoGen 18120 epoxy resin for stereolithography is processed as a single-component vat charge at 100 wt% of the as-received material; no reactive diluent or secondary resin is added because even a 5 wt% aliphatic diepoxide addition alters photoinitiator stoichiometry and reduces green flexural modulus in thin trailing-edge sections, a boundary established by build trials on a production-scale 355 nm galvanometer laser stereolithography platform with a 100 µm slice thickness. In aerodynamic test article production, the downstream process begins with build orientation that places pressure tap arrays on the up-facing surface to avoid support witness marks, followed by two-stage solvent rinse, support removal, and UV postcure at the prescribed HOC -2 setpoint in a calibrated chamber until postcure hardness per ASTM D2240-15 stabilises within ±2 Shore D points between successive 30 min intervals. Test houses conducting low-speed wind tunnel campaigns require coupon data generated per ASTM D638-14 for tensile strength and ISO 178 for flexural modulus from each build lot, and when models are placed in closed-return smoke visualization sections, outgassing screening per ASTM E595-15 is commonly requested with total mass loss below 1.0% and collected volatile condensable material below 0.1%. Production-scale vat behaviour shows that humidity above 60%RH during overnight idle periods increases resin carry-out on fine lattice supports and produces postcure surface tack; this is managed by sealing the vat and conditioning build chamber air to 25 ± 3°C and 45 ± 5%RH. Terminal finished product types include high-speed inlet models, static pressure-tapped airfoil sections, and wing-body intersection fairings used with sting balances at flow velocities below 50 m/s and total air temperature below 35°C, where the epoxy photopolymer replaces polyurethane tooling board for short-duration test campaigns.
In low-pressure injection tooling for prototype polyolefin connector bodies, the resin is applied as a neat stereolithography vat charge at 100 wt%; abrasive metal or ceramic fillers are not dispersed into the vat because even 0.5 wt% of sub-10 µm filler reduces laser penetration at the build plane and moves the working curve outside the manufacturer’s documented process window. Downstream tool insert fabrication uses a 355 nm stereolithography platform with 50 µm slice thickness to capture sealing grooves and snap-fit detents, followed by two-stage isopropanol wash, compressed air drying until mass stabilises, and UV postcure at the HOC -2 setpoint; the postcured insert is then seated in an aluminium bolster with steel backing to limit flexural overload. Prototype injection runs are conducted on a 15-ton vertical clamp injection moulding machine with a 20 mm diameter plunger, melt temperature not exceeding 230°C for glass-filled polyamide and 200°C for polypropylene, and maximum injection pressure limited to 30 MPa to avoid insert edge cracking; field failure modes on short-run lines include gate land crazing and seal lip rounding when pack pressure is held beyond 4 s at 30 MPa. Dimensional validation of moulded parts references ISO 20457:2018 for general tolerance classes, and machine parameter setting is documented per ISO 294-1:2017 for test-plate consistency. Terminal finished product types include polypropylene latch housings, glass-filled polyamide snap-fit covers, and thermoplastic elastomer grommet retainers produced in 50–150 shot validation campaigns before steel production tool release.
Because the supplier-fixed photopolymer network formation cannot be adjusted by downstream processors, connector housing prototypes are built from a single-component vat charge at 100 wt%; dispersant addition above 0.1 wt% or any conductive carbon filler is not recommended because refractive index mismatch between filler and matrix scatters laser energy and produces undercured walls below 1.0 mm thickness. The downstream production sequence begins with a 355 nm solid-state laser stereolithography system set to 100 µm slice thickness, with connector shell mouths oriented at 15–25° from the recoater axis to reduce peeling forces on snap features; after build, parts receive a solvent rinse, support removal, and UV postcure at the HOC -2 setpoint using irradiance verified at 10 mW/cm² by calibrated radiometer until Shore D hardness per ASTM D2240-15 changes by less than 2 points between successive 30 min intervals. Electrical prototype evaluation requires a compliance matrix that includes ASTM D638-14 for mechanical coupon testing, ASTM D257-14 for volume resistivity at 500 V DC after 40 h conditioning at 23 ± 2°C, UL 94 burn rating screening on 0.8 mm plaques, and IEC 60112:2009 comparative tracking index when creepage requirements are specified by the end product standard. Terminal finished product types include connector shells, terminal position assurance caps, and relay enclosure mockups used for contact insertion force, pin retention, and high-potential clearance checks before hard tooling is financed.
| Application zone | Primary compliance anchor | Critical process boundary | Terminal part class |
|---|---|---|---|
| Low-pressure wind tunnel models | ASTM E595-15 TML <1.0%, CVCM <0.1% | 100 µm slice; HOC -2 postcure; wall ≥1.0 mm | Inlet models, airfoil sections, fairings |
| Rapid injection tooling inserts | ISO 294-1:2017; ISO 20457:2018 | 30 MPa injection pressure; melt ≤230°C | PP, GF-PA, TPE prototype housings |
| Electrical connector prototypes | ASTM D257-14; IEC 60112:2009 | 500 V DC test voltage; 0.8 mm wall minimum | Connector shells, TPA caps, relay mockups |
| Diagnostic housing development | ISO 10993-5:2009; ISO 10993-10:2010 | L929 extraction 24 h; IPA second bath <5 wt% water | Front bezels, probe housings, cartridge carriers |
| Underhood fluid prototype validation | ASTM D543-14; ASTM D638-14 | 80°C glycol/water 168 h; wall 1.2–3.5 mm | Coolant line mockups, manifold prototypes, reservoir necks |
During design verification of non-invasive diagnostic housings, DSM Somos ProtoGen 18120 is introduced into the stereolithography vat at 100 wt% as a single-component resin; no plasticizer, organic solvent, or external thermal initiator is added because extractables and leachables screening under ISO 10993-12:2021 would be confounded by non-network species, and any diluent addition above 1.0 wt% is outside the supplier’s published data envelope. The resin should not be blended with primary amine hardeners or isocyanates because premature epoxy advancement before UV exposure raises vat viscosity and alters recoater flow. The downstream fabrication route uses a 355 nm laser stereolithography platform with 100 µm layer thickness, two-stage isopropyl alcohol rinsing in which the second bath is changed before water content exceeds 5 wt%, air drying until mass change per ASTM D570-98 stabilises below 0.2% in 24 h, and UV postcure at the prescribed HOC -2 setpoint with rotation to expose shaded internal channels. Biocompatibility evaluation for device development housings follows the risk-based approach of ISO 10993-1:2018, with routine in vitro cytotoxicity per ISO 10993-5:2009 using L929 cells and an extraction period of 24 h, skin sensitisation per ISO 10993-10:2010, and, when the housing contacts the patient for more than 24 h, additional irritation testing may be required by the notified body; this photopolymer is intended for non-implantable, non-tissue-contact structural mockups unless a full material qualification file is completed. Terminal finished product types include diagnostic instrument front bezels, handheld ultrasound probe housing mockups, and in vitro diagnostic cartridge carriers that undergo benchtop vapour hydrogen peroxide exposure cycles but are not supplied as sterilised finished devices.
For underhood fluid-handling prototypes, ProtoGen 18120 epoxy resin for stereolithography is charged at 100 wt% without second-resin blending because the postcure state must remain uniform in wall thicknesses between 1.2 mm and 3.5 mm; reactive diluent addition below 10 wt% is not supported by published data for hot water-glycol exposure and may lower the retention of tensile properties at 80°C. The production sequence includes 100 µm layer slicing, oriented build with critical sealing bosses parallel to the recoater direction to avoid partial collapse, support removal, and UV postcure at the specified HOC -2 setpoint followed by 1 h thermal equilibration at room temperature before dry-air leak testing at 0.3 bar for reservoir necks and at 1.0 bar for coolant line sections. Screening for automotive fluid exposure uses dumb-bell tensile coupons prepared per ASTM D638-14 and immersed per ASTM D543-14 in 50:50 vol% ethylene glycol/water at 80°C for 168 h; mass change, visual surface change, and tensile strength retention are recorded rather than judged against a universal pass criterion because the photopolymer is applied for short-loop validation before production tooling. Field line experience indicates that quick-connect mockups printed with support structures on bayonet ramp surfaces exhibit higher leak reject rates after postcure unless the ramp is built at 0° to the build platform; published data for this specific configuration is limited beyond this observation. Terminal finished product types include quick-connect coolant line mockups, windshield washer manifold prototypes, and brake fluid reservoir necks used for cap retention and insertion angle validation before metal or glass-filled nylon production tooling is released.
Конкурентоспособная эпоксидная смола DSM Somos ProtoGen™ 18120 для стереолитографии, UV Postcure по ценам HOC -2, которые соответствуют вашему бюджету - гибкие условия и индивидуальные котировки для каждого заказа.
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DSM Somos ProtoGen™ 18120 is an epoxy-based photopolymer supplied as a single-component liquid for vat photopolymerization stereolithography. The product is processed in the green state on laser-based SLA platforms and is subsequently conditioned under a designated ultraviolet postcure protocol referenced as HOC -2. The HOC -2 designation identifies a two-stage post-exposure sequence in which UV-A irradiation and elevated chamber temperature are combined to complete cationic crosslinking; it is not a separate resin grade. The uncured resin requires storage in light-tight containers at 20–25 °C and is conditioned by gentle rotation or low-shear agitation before introduction into the vat. Viscosity measured per ASTM D4212-16 falls within the low-viscosity range typical for stereolithography epoxies, which supports recoating on platforms with build envelopes from 250 × 250 × 250 mm to 600 × 600 × 500 mm. The cured network is evaluated after the HOC -2 protocol for tensile, flexural, and thermal properties under ASTM methods. Selection of this material is common where postcured dimensional stability, low moisture uptake, and controlled burnout residue are more important than high elongation at break.
On production-scale SLA equipment, the resin is imaged with a solid-state laser operating near 355 nm. The green part is removed from the platform, washed in a compatible solvent, and dried before postcure. The interval between cleaning and postcure should be minimized to avoid solvent absorption at the surface; parts left in solvent for more than 10 min may exhibit measurable dimensional drift. Entrained air introduced during vat refilling is removed by vacuum degassing at 20–25 kPa absolute pressure until bubble free. The use of open-mesh build platforms is acceptable, but support density should be increased by 15–20% on unsupported spans greater than 50 mm to control green-state sag.
The HOC -2 postcure condition is implemented in UV flood chambers capable of simultaneous UV-A emission and thermal ramping. For this resin class, the chamber lamp output should be verified with a calibrated radiometer prior to each production campaign because UV-A irradiance degrades with lamp age; a commonly used acceptance threshold is 10–15 mW/cm² at the part surface. In the first stage, the part is held at 35–40 °C under UV-A exposure for 30–40 min. In the second stage, the chamber setpoint is raised to 55–65 °C and held for an additional 30–60 min while UV exposure continues. The ramp rate should not exceed 2 °C/min for sections with wall thickness less than 2 mm; faster ramps can induce thermal gradient distortion. Postcure completion is judged by a plateau in Shore D hardness measured on a witness coupon, not by fixed time alone.
Production-scale failure modes associated with improper HOC -2 execution include surface blistering, incomplete through-cure, and non-uniform dimensional change. Blistering is typically linked to residual cleaning solvent absorbed in the green state; the part must be dried with filtered air at 25–30 °C until constant mass before UV postcure. Incomplete through-cure is observed when lamp irradiance falls below the minimum threshold or when chamber thermal control drifts below setpoint. Non-uniform dimensional change is aggravated by stacking parts in the postcure chamber; parts should be arranged with 10–20 mm spacing and rotated halfway through the cycle. Published data for this specific product configuration is limited on the effect of chamber oxygen concentration; however, cationic epoxy photopolymers generally show higher cure inhibition in the presence of elevated humidity. Therefore, the postcure chamber should be maintained at 35–45% RH during the HOC -2 sequence.
Layer thickness is typically selected between 50 µm and 100 µm for this epoxy formulation. Laser spot diameter and scan spacing are adjusted on the equipment to maintain a stable line overlap; typical beam diameters of 0.10–0.25 mm are used with scan speeds that provide sufficient localized energy to achieve green adhesion. Recoating parameters should be tuned so that the wiper blade travel speed does not entrain air; speeds of 50–100 mm/s are common for this viscosity class. On machines with active coating feedback, the setpoint should be recalibrated after each resin batch change. Deviations in layer thickness greater than ±10 µm at the build plane require platform re-leveling or wiper blade replacement.
The typical postcured property values shown in the table below are based on manufacturer technical datasheet information for fully postcured specimens prepared under the HOC -2 condition. Values are not lot-specific and should be confirmed against the current certificate of analysis for the specific batch. Specimen conditioning before testing follows ASTM D618-21 at 23 ± 2 °C and 50 ± 10% RH.
| Property | Test Method | Typical Value |
|---|---|---|
| Tensile strength | ASTM D638-14 | 62–68 MPa |
| Tensile modulus | ASTM D638-14 | 2,900–3,200 MPa |
| Elongation at break | ASTM D638-14 | 5.0–7.0% |
| Flexural strength | ASTM D790-17 | 100–108 MPa |
| Flexural modulus | ASTM D790-17 | 2,800–3,000 MPa |
| Notched Izod impact | ASTM D256-10 | 22–28 J/m |
| Heat deflection temperature at 0.46 MPa | ASTM D648-18 | 68–74 °C |
| Hardness, Shore D | ASTM D2240-15 | 84–86 |
| Viscosity at 25 °C | ASTM D4212-16 | 1,000–1,200 mPa·s |
The reported tensile and flexural values reflect the postcured epoxy network. Green-state properties are substantially lower and should not be used for design validation. Heat deflection values should not be interpreted as continuous-use temperature limits; prolonged exposure above the HDT may cause stress relaxation and creep in loaded sections. For applications requiring continuous thermal exposure, independent creep testing per ASTM D2990-17 is required.
Rheological characterization of the uncured resin is performed with a rotational rheometer equipped with a cone-and-plate geometry at 25 °C. The viscosity curve under increasing shear rate shows mild pseudoplastic behavior; at 1 s-1 the apparent viscosity is near the low end of the datasheet range, and at 100 s-1 the value is typically lower by 5–10%. Temperature dependence follows an Arrhenius-type decrease; heating the vat from 25 °C to 30 °C can reduce viscosity by approximately 10–15%, which may improve recoating performance in large-format systems but also accelerates dark cure in the vat. Batch-to-batch viscosity variation should be monitored per ASTM D4212-16; a shift greater than ±15% from the initial batch should trigger investigation of storage age and moisture ingress.
Vat life is influenced by ambient light, ambient humidity, and residual heat from the laser. In long production runs, the resin temperature may rise above ambient due to laser energy deposition and recirculation pump heat. If the vat exceeds 35 °C, premature cationic advancement can occur, leading to increased viscosity and a measurable shift in green-state modulus. Production equipment should include vat temperature control or a cooling loop; the setpoint should be maintained at 25–28 °C and recorded at 15-min intervals. The use of a resin life monitor based on near-infrared spectroscopy can detect partial advancement, but such online monitors are not universal; published data for this specific configuration is limited.
Green-state distortion is the largest process variable in high-accuracy stereolithography with this epoxy system. The green part is subject to shrinkage during laser patterning and to subsequent solvent-induced swelling during cleaning. Measurements on production-scale builds show that long, unsupported overhangs can deviate by 0.2–0.5 mm over a 100 mm span when support pitch is insufficient. To control this distortion, supports should be placed on any down-facing feature with an overhang angle less than 30° from horizontal. For features with unsupported spans between 50 mm and 100 mm, support density should be increased by 25–50% relative to default settings. The use of a support contact diameter below 0.4 mm may reduce witness marks but increases the risk of green-state detachment during recoating.
Surface roughness of postcured components is determined by layer thickness, stair-stepping, and the cleaning solvent residue. With 50 µm layers, the Ra of an up-facing surface is typically below 1 µm after postcure, while down-facing surfaces adjacent to supports may show Ra values above 5 µm before sanding. When the HOC -2 protocol is executed correctly, no additional thermal cure is required, but surface hardness may continue to increase for several hours after removal from the chamber due to dark cure. Parts should not be exposed to high-humidity environments for 24 h following postcure because moisture uptake during dark cure can affect dimensional stability. Dimensional inspection should be performed after a stabilization period of 24–48 h at 23 ± 2 °C.
In comparison with acrylate-hybrid stereolithography resins, the epoxy chemistry of ProtoGen™ 18120 is associated with lower reaction shrinkage during polymerization. Linear shrinkage after postcure is typically measured by the difference between green-state and postcured dimensions; for process compensation purposes, users of this class report scaling factors in the range of 0.1–0.3%, although published data for this specific configuration is limited. The postcured network generally exhibits lower equilibrium moisture uptake than typical acrylate systems, which reduces the risk of dimensional drift in humid service environments. The primary trade-off is lower elongation at break; thin snap features and living hinges are more prone to fracture than similar features molded in polypropylene or produced from high-elongation acrylate resins.
In investment casting pattern production, ProtoGen™ 18120 is processed into patterns that are subsequently assembled, dipped in ceramic shell, and removed by controlled burnout. The burnout cycle is defined by the shell manufacturer and must be validated for the specific pattern geometry. Thermogravimetric analysis in air at a heating rate of 10 °C/min typically shows complete decomposition of the organic fraction below 700 °C; the oxide shell remains structurally intact when the heating ramp is matched to the polymer decomposition profile. The low residual ash of the unfilled epoxy network, compared with filled SLA resins, makes the material suitable for alloy systems where carbon contamination and nonmetallic inclusions must be minimized, including titanium and cobalt-chromium melts. Ash content should be verified per ASTM D482-19 on the specific batch used for production.
Replacement of an acrylate-hybrid photopolymer with ProtoGen™ 18120 requires recalibration of the entire post-processing line, not merely substitution of the resin. The green-state cleaning solvent may need to be changed because some acrylate systems tolerate ethanol-based washing, whereas epoxy formulations of this class are typically washed in isopropanol or tripropylene glycol monomethyl ether. The HOC -2 postcure condition requires UV-A irradiation that is not always present in units optimized for acrylate thermal postcure; a chamber equipped only with a convection heater will not fully develop the cationic epoxy network. The lower reaction shrinkage of ProtoGen™ 18120 allows the scaling factor to be reduced by 0.1–0.2% relative to many acrylate-hybrid resins, but this requires confirmation by measuring a known calibration artifact before production release.
For master patterns used in silicone tooling, the higher modulus and lower elongation of the fully postcured epoxy network can transfer finer surface detail and reduce pattern deformation during silicone cure. However, the lower impact resistance requires support design modifications on features with cross-sections below 1 mm. On production-scale SLA lines, the reduction in support density possible with acrylate systems is not applicable; supports should be retained at a density calculated for green-state deflection of the epoxy network and verified by build trials. The use of a UV postcure fixture with 365–420 nm lamps is required; broadband metal halide systems may be acceptable if the measured UV-A irradiance meets the minimum threshold at the part surface.
The uncured resin should not be combined with amine-based additives, strong nucleophiles, or moisture-releasing fillers because these components can inhibit cationic polymerization or cause premature gelation in the vat. During material handling, contact with copper, brass, or iron oxides should be avoided in the recoat system; use stainless steel or polyethylene wetted parts. Cured parts exposed to continuous UV radiation under service conditions may undergo progressive discoloration without loss of bulk mechanical integrity; long-term stability should be verified by accelerated weathering per ISO 4892-2 when appearance is critical. The postcured epoxy network is not recommended for contact with strong alkaline solutions at temperatures above 50 °C because hydrolytic attack can reduce surface hardness. Published data for chemical resistance in the specific HOC -2 postcured state is limited; compatibility testing under the actual service fluid should be performed before production release.