| HS Code | 732439 |
| Appearance | Translucent amber |
| Density | 1.13 g/cm³ at 25°C |
| Viscosity | 260 cps at 30°C |
| Criticalexposure | 11.8 mJ/cm² |
| Penetrationdepth | 0.14 mm |
| Tensilestrength | 65 MPa |
| Tensilemodulus | 2870 MPa |
| Elongationatbreak | 5% |
| Flexuralstrength | 108 MPa |
| Flexuralmodulus | 2480 MPa |
| Hardness | 87 Shore D |
| Heatdeflectiontemperature | 100°C at 0.46 MPa |
| Waterabsorption | 0.35% |
| Glasstransitiontemperature | 115°C |
| Notchedizodimpact | 25 J/m |
| Postcure | UV |
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DSM Somos ProtoTherm™ 12110 is a liquid photopolymer formulated for laser-based stereolithography and supplied as a water-resistant resin system after ultraviolet postcure. The material is processed on SL platforms operating with 355 nm solid-state lasers and typical layer thicknesses between 0.05 mm and 0.15 mm. The designation belongs to the ProtoTherm family, in which final mechanical and thermal properties are not attained at the end of the laser build; a controlled UV postcure step is required to complete acrylate conversion. Unlike optical-clear water-resistant grades, ProtoTherm 12110 presents a translucent amber to opaque appearance depending on wall thickness and postcure dose. The uncured liquid is a reactive acrylate-containing formulation and is supplied under hazard communication obligations of CLP, Regulation EC 1272/2008. In production environments, the grade is selected for short-run fluid-contact manifolds, inspection gauge bodies, and temperature-resistant tooling inserts where moisture uptake and low-load thermal deflection of conventional stereolithography resins are limiting. The product is characterized by low moisture absorption relative to general-purpose SL resins, but it is not a replacement for true thermoplastic water-resistant polymers in continuous submersion without application-specific validation.
Because stereolithography green-state conversion is incomplete when the platform is lowered, residual unpolymerized acrylate remains within the network. Green parts must be solvent rinsed to remove the liquid resin film, dried, and then subjected to UV postcure. Tensile modulus in the green state is typically 70–80% of the final postcured value; skipping or shortening the postcure cycle lowers heat deflection temperature, raises water absorption, and can produce surface tack. The term water-resistant therefore applies to fully postcured material, not to green or under-cured surfaces. Production experience shows that parts exposed to humid air before postcure may develop surface haze and local plasticization, particularly in high-humidity environments above 60% RH.
Residual acrylate conversion, anisotropic layer consolidation, and irradiance uniformity in the UV chamber determine final part stability. In production-scale stereolithography with 355 nm solid-state lasers, green-state parts of ProtoTherm 12110 are rinsed in 2-propanol; excessive solvent immersion leaches unreacted monomer and promotes surface microvoids. After drying, the UV postcure step increases crosslink density, raises the glass transition temperature, and reduces equilibrium moisture uptake. The rate of conversion is irradiance-dependent. UV chambers delivering 20–30 mW/cm² in the UVA range are commonly used, but shadowed internal channels may receive less than 50% of the nominal surface dose. Under-cured zones therefore retain higher hydrophilicity and lower modulus than the surrounding network. For manifold parts with blind bores, postcure protocols should include internal light guides or a secondary thermal hold to avoid low-conversion regions at thread roots and sealing lands. Published data for specific chamber-to-part thermal loadings in the 12110 formulation is limited; the absolute postcure duration must be established by part mass, wall thickness, and chamber uniformity.
Uncured viscosity at 30 °C is typically within 200–300 mPa·s, measured according to ISO 2884-1, allowing conventional recoater blade passage at standard layer heights. Batch-to-batch viscosity variation can reach approximately ±10%; vat temperature control within ±2 °C compensates for most viscosity drift. Slow vat rotation at 5–10 rpm for approximately 30 min before large-platform builds homogenizes the oligomer blend without inducing bubble formation. Bubbles larger than 0.1 mm in diameter cause print voids and should be allowed to rise for 15–30 min after agitation. The material does not contain heavy ceramic filler, so recirculating vat systems experience lower blade wear and settling than filled high-modulus SL grades.
The table below lists representative postcure values from manufacturer technical literature. Each value should be revalidated against the current product datasheet because laser scan spacing, chamber irradiance, and postcure dose alter final conversion.
| Property | Test Method | Representative Value |
|---|---|---|
| Tensile strength | ASTM D638-14 | 58–63 MPa |
| Tensile modulus | ASTM D638-14 | 2.8–3.0 GPa |
| Elongation at break | ASTM D638-14 | 4–5% |
| Flexural strength | ASTM D790-17 | 95–105 MPa |
| Flexural modulus | ASTM D790-17 | 2.7–3.1 GPa |
| Notched Izod impact | ASTM D256-23 | 18–22 J/m |
| Heat deflection temperature at 0.46 MPa | ASTM D648-18 | 260–268 °C |
| Heat deflection temperature at 1.82 MPa | ASTM D648-18 | 60–65 °C |
| Water absorption, 24 h | ASTM D570-22 | 0.35–0.45% |
| Density | ISO 1183-1:2019 | 1.15–1.17 g/cm³ |
The notched Izod impact range of 18–22 J/m places the postcured polymer in a stiff, moderately brittle regime. Sharp internal corners, thread roots, and snap features require radii greater than 1.0 mm to reduce stress concentration. The large difference between the 0.46 MPa and 1.82 MPa HDT values is significant: the high-temperature utility of ProtoTherm 12110 is strongly load-dependent. Components under continuous mechanical load should not be designed solely against the 0.46 MPa HDT value.
Fully postcured ProtoTherm 12110 exhibits heat deflection temperature under a 0.46 MPa flexural load of approximately 260–268 °C as tested per ASTM D648-18. At the higher 1.82 MPa load, the reported HDT falls to 60–65 °C. The glass transition temperature measured by dynamic mechanical analysis is typically above 120 °C, but exact values depend on postcure dose and laser scan strategy. The 24-hour water absorption in distilled water is typically less than 0.5% by mass under ASTM D570-22. This low hygroscopic uptake supports use in humid or splash-contact environments, but immersion at elevated temperature accelerates diffusion and can promote hydrolytic degradation of ester-containing network segments. There is no published data for continuous immersion beyond 30 days; parts intended for submersible service must be tested under application-specific hydrostatic pressure and temperature cycling.
Dimensional change after 7-day immersion in 23 °C water is generally below standard caliper measurement uncertainty for thin sections, while long-term saturated conditioning may produce slight expansion and reversible weight gain. The material is not suitable for continuous exposure to strong acids, strong bases, or aggressive solvents such as acetone or methylene chloride. Chemical compatibility testing should follow ASTM D543-21 or ISO 175:2010 for candidate process fluids. Isopropyl alcohol used for green-state cleaning causes reversible swelling in uncured or partially cured surfaces but is removed by drying before UV postcure.
Parts intended for dimensional stability over humid cycling should undergo a postcure anneal at 80–100 °C for 2–4 h after UV exposure to relieve internal stresses. Humid cycling between 20% RH and 80% RH at 23 °C can produce reversible length changes on the order of 0.05% for thin sections. For high-precision metrology fixtures, sealing primer or structural tie-coats reduce moisture-driven movement at exposed layer boundaries.
The substitution is justified where complex internal cooling channels, thin-walled manifolds, or conformal tooling inserts are required. Compared with machined acetal copolymer, ProtoTherm 12110 offers higher HDT under low stress but lower tensile elongation and lower notched impact. Machined glass-filled nylon has higher moisture uptake and anisotropic shrinkage; the photopolymer’s lower water absorption and layer-based stress distribution may improve dimensional reproducibility in humid plant air. However, the postcured polymer remains a crosslinked thermoset: it cannot be solvent welded, tapped threads under repeated disassembly may degrade, and adhesive bonding requires surface abrasion with compatible methyl methacrylate or epoxy adhesives. When replacing PEEK or polysulfone in hot-water service, the 1.82 MPa HDT must be compared against actual stress for each flange, boss, or sealing face rather than against the low-load 0.46 MPa value.
On production SL platforms, build chamber temperature is often held at 28–35 °C to stabilize viscosity and recoater shear. The absence of heavy ceramic filler reduces blade wear and settling; homogenization by slow rotation before vat transfer is nonetheless required after storage because oligomer stratification can alter green-state modulus. Laser fill pattern, hatch spacing, and slice thickness alter cure depth and green-state tensile strength. Operator-adjusted parameters must remain within the manufacturer’s validated process window. In high-humidity environments, pre-drying of the platform and part is advised before postcure to prevent surface haze and local plasticization. Use of aggressive solvent degreasing agents containing chlorinated hydrocarbons should be avoided because they induce stress cracking in green or partially cured parts.
Production-scale builds on platforms with build envelopes of 650 mm × 750 mm × 550 mm may show edge-to-center variation in laser irradiance. Part placement near the build perimeter can exhibit 5–10% lower green-state tensile modulus. High-load-bearing components should be staggered toward the center of the platform, and multiple thin walls should not be stacked parallel to the recoat direction without additional support.
Throughput is governed less by laser scan time than by green-state cleaning and UV postcure occupancy. In a typical facility using a 40 W UV chamber with rotating part fixture, a 60–90 min postcure cycle is used for parts up to 10 mm wall thickness. Thicker sections may require stepped irradiance ramps to avoid exothermic surface overheating. The radiated surface temperature can exceed 60 °C if parts are packed too closely, causing local overcure and embrittlement. Cleaning in 2-propanol reduces residual liquid resin but swells the green network; a final rinse in deionized water followed by dry compressed air is common. Work practices should include ventilation and nitrile glove barriers because uncured resin is a skin sensitizer under CLP, Regulation EC 1272/2008.
The relationship between UV dose and tensile modulus is nonlinear. At low doses below 1.0 J/cm² in the UVA range, residual unpolymerized acrylate acts as a plasticizer, lowering modulus and increasing water absorption. At doses above 8–10 J/cm², surface discoloration and embrittlement may occur. Medium-pressure mercury or LED sources emitting at 365–405 nm are both used. LED systems with narrower spectral output produce shallower through-thickness conversion unless cycle time is extended. Rotating fixtures with reflective aluminum chamber walls improve dose uniformity on complex geometries, but shadowed internal channels may receive less than 50% of the nominal surface dose. For manifold parts with blind bores, internal light guides or secondary thermal cure are required to avoid low-conversion zones at thread roots.
In comparison with Somos WaterShed XC 11122, which offers optical clarity and low water absorption for fluid-flow visualization models, ProtoTherm 12110 sacrifices transparency for a higher thermal deflection envelope and reduced long-term moisture uptake at elevated temperature. Against Somos NeXt, the 12110 grade displays higher HDT and lower elongation, making it less suitable for snap-fit covers but more suitable for high-temperature inspection fixtures. Against ceramic-filled Somos PerFORM, ProtoTherm 12110 processes with lower blade wear and produces lower slurry viscosity but also lower modulus in the finished part. The product is therefore positioned for short-run tooling, wind tunnel instrumentation, and fluid manifolds where both water resistance and moderate load-bearing thermal resistance are selection criteria.