| HS Code | 623437 |
| Product Name | Radical Photoinitiator Jiuri New Material TPO |
| Chemical Type | Acylphosphine oxide photoinitiator |
| Chemical Name | Diphenyl(2,4,6-trimethylbenzoyl)phosphine oxide |
| Cas Number | 75980-60-8 |
| Molecular Formula | C22H21O2P |
| Molecular Weight | 348.38 g/mol |
| Appearance | Light yellow crystalline powder |
| Melting Point | 88-92 °C |
| Absorption Wavelength Range Nm | 350-420 nm |
| Maximum Absorption Wavelength Nm | 380 nm |
| Solubility | Soluble in acetone, ethyl acetate, and toluene; insoluble in water |
| Purity | ≥99% |
As an accredited Radical Photoinitiator Jiuri New Material TPO factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaged in 20 kg fiber drums with polyethylene inner liners, sealed to protect against moisture and light exposure. |
| Container Loading (20′ FCL) | 20′ FCL loading of Radical Photoinitiator Jiuri New Material TPO: palletized drums, securely stowed, ventilated, protected from heat and moisture. |
| Shipping | Shipped in sealed, light-protective, moisture-resistant packaging to preserve product stability. Classified as a non-dangerous chemical under standard conditions, but safe handling and temperature controls apply. Transport via air, sea, or ground freight with proper chemical documentation, ensuring full compliance with all local and international shipping regulations. |
| Storage | Store in a cool, dry, well-ventilated area away from direct sunlight, heat, and ignition sources. Keep the container tightly sealed to prevent moisture absorption and contamination. Avoid contact with strong oxidizers, acids, and alkalis. Maintain stable temperatures, and follow local regulations for handling and disposal. |
| Shelf Life | Shelf life is 24 months when stored unopened in a cool, dry, dark place away from light and heat. |
On flat-line finishing equipment running white-pigmented acrylic-urethane furniture coats, the replacement of a gallium-doped mercury arc array with a 395 nm LED bank is only viable when TPO is present at a loading that offsets the spectral competition of rutile TiO₂. In a 100% solids oligomer/monomer blend containing 25–30 wt% rutile TiO₂, TPO is typically charged at 0.6–1.4 wt% on total formulation weight, with a surface-cure co-initiator such as 1-hydroxycyclohexyl phenyl ketone at 1.5–2.0 wt%. The production-scale process is a roller-coater or curtain-coater flat line applying 10–30 g/m² wet film, followed by a UV-LED module operating at 395 nm with peak irradiance in the range of 6–12 W/cm² and belt speed between 5–10 m/min. On high-speed lines, the primary failure mode is interfacial under-cure at the substrate-coating boundary when the TiO₂ loading exceeds 30 wt%, producing intercoat adhesion loss that is detected only after 24 h conditioning. Compliance for this segment is anchored to DIN EN 12720:2013-10 for surface resistance to cold liquids, ISO 2409:2013 for cross-cut adhesion classification, ASTM D3359-09e2 for tape adhesion, and EN 71-3:2019+A1:2021 where children's furniture is coated. Terminal articles include flat-pack furniture frontals, engineered wood flooring, interior door skins, and laminate panels for retail display systems.
The limiting variable is not the TPO absorption tail but the optical competition between TPO and rutile TiO₂ in ink films applied at 4–6 µm dry film thickness. In a UV-flexographic white ink containing 12–20 wt% titanium dioxide and 25–35 wt% pigment paste on total ink weight, TPO is incorporated at 0.8–1.2 wt% to shift radical generation into the 385–405 nm window where the pigment opacity is lower. Narrow-web flexo presses with anilox cell volumes of 6–10 cm³/m² and UV-LED arrays at 385 nm can sustain printing speeds of 70–150 m/min, but the process window is constrained by set-off and surface tack when the ink film is cured to less than 60% acrylate conversion. For non-food applications, conformity is demonstrated through EuPIA Good Manufacturing Practice and REACH Regulation (EC) No 1907/2006; for indirect food contact, migration of TPO and its benzaldehyde-related degradation products must be evaluated under EU 10/2011 and Swiss Ordinance SR 817.023.21. Finished product types are industrial pressure-sensitive labels, shrink sleeves for non-food packaging, and single-side coated cartonboard for electronic accessory cartons.
When TPO is dissolved in a methacrylate oligomer blend at 0.5–2.0 wt%, the long-wavelength absorbance near 405 nm decreases after primary radicals are generated, which is the photobleaching effect that permits deep layer cure in DLP, LCD, and SLA systems. The practical consequence is a non-linear relationship between TPO concentration and Jacobs working curve parameters: at 0.3–0.8 wt% in clear resins, the penetration depth Dp remains high but the critical exposure Ec increases, while at 1.5–3.0 wt% in ceramic-filled slurries the initial absorbance suppresses cure depth until bleaching occurs. On a DLP printer operating at 405 nm with an irradiance of 3–10 mW/cm², a 50 µm layer of a clear engineering resin typically requires 0.5–2.0 s exposure when TPO is loaded at 0.5–1.0 wt%. A production-specific defect is lateral overcure in negative features: excessive TPO loading above 2.0 wt% increases radical gradient outside the illuminated pixel boundary, reducing dimensional accuracy according to ISO/ASTM 52921:2013 coordinate artifact testing. Storage at 10–15 °C can precipitate TPO in ethoxylated bisphenol A diacrylate blends above 2.5 wt%, causing print-through variation unless the vat is heated to 20–25 °C. Mechanical validation follows ASTM D638-14 tensile testing, and for medical or dental model applications the final resin must be evaluated under ISO 10993-5:2009; TPO alone does not confer biocompatibility. Terminal products are investment casting patterns, orthodontic study models, jewelry master patterns, rapid tooling inserts, and engineering prototypes requiring translucent or white-pigmented appearance.
A slot-die coating line depositing 50 g/m² of UV-curable acrylic syrup onto release liner does not reach full conversion at the liner interface when TPO is used alone below 0.3 wt%, because the long-wavelength LED dose is attenuated by the adhesive layer before the initiator can generate radicals near the liner. TPO is therefore formulated at 0.3–1.0 wt% in acrylic PSA syrups, often with a thioxanthone derivative at 0.2–0.5 wt% to compensate for oxygen inhibition at the exposed surface. The coating line runs at 10–30 m/min with a 395 nm LED array delivering 1,000–2,000 mJ/cm² UVA dose, and nitrogen inerting is applied to maintain residual O₂ below 500 ppm. Failure to inert the surface produces a tacky, uncured monolayer that transfers to the silicone release liner and reduces peel adhesion. Adhesive performance is assessed by ASTM D3330/D3330M-04(2018) for 180° peel, ASTM D6195-22 for loop tack, and ASTM D4498-07(2015) for shear adhesion failure temperature. Terminal products are double-sided transfer tapes, graphic film laminating adhesives, appliance trim tapes, and window film mounting adhesives.
Selective conformal coating of assembled PCBs uses TPO at 1.0–2.0 wt% in acrylated urethane resins to permit curing with 365 nm and 385 nm LED arrays where the coating is exposed to direct irradiation. The long-wavelength absorption band of TPO reduces uncured residue underneath low-profile QFN and 0201 chip components with stand-off heights of 0.10–0.20 mm, but it does not cure fully shadowed areas. Production lines therefore specify a dual-cure mechanism: radical cure within 1–3 s under LED irradiance of 8–15 W/cm², followed by moisture cure in occluded regions over 24–72 h at 30 °C and 60% relative humidity. The process is run on selective dispense systems with needle-valve or air-assisted spray heads, and the typical dry film thickness is 25–75 µm. Qualification follows IPC-CC-830B for electrical insulating compounds, with humidity insulation resistance measured after 7 days at 85 °C/85% RH, and RoHS Directive 2011/65/EU restricts lead, mercury, cadmium, and other restricted substances in the finished PCBA. Terminal article categories are automotive electronic control units, industrial drives, LED power supplies, and white goods control boards.
UV-curable powder coating systems are compounded in twin-screw extruders with barrel set points no higher than 90 °C, because TPO has a melting point of 91–94 °C and premature softening of the solid initiator before distributive mixing leads to uneven photoresponse and gel specks in the cured film. The formulation window for TPO in UV-curable unsaturated polyester or methacrylate powders is 0.5–1.5 wt%, added downstream of the melt zone through a side feeder or pre-dispersed in a resin masterbatch. Extruded chips are cryogenically ground to a d50 of 30–50 µm, electrostatically sprayed onto MDF panels, melted under IR panels at 90–110 °C for 60–120 s, and then cured with a gallium-doped mercury arc or a high-irradiance 395 nm LED array at 300–600 mW/cm². The critical process boundary is the IR melting step: if the panel surface exceeds 120 °C, the MDF substrate can develop steam blisters and the powder film may gel before UV irradiation. Coating quality is tested according to ISO 1518-1:2019 for scratch resistance and DIN EN 12720:2013-10 for cold-liquid resistance on furniture surfaces. End products include MDF office desktops, kitchen cabinet frontals, and retail display shelves where low solvent emission is required.
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Radical Photoinitiator Jiuri New Material TPO is the commercial designation for the solid acylphosphine oxide photoinitiator (2,4,6-trimethylbenzoyl)diphenylphosphine oxide, identified by CAS 75980-60-8 and molecular formula C22H21O2P. The product is supplied as a light yellow crystalline powder with a molecular weight of 348.37 g/mol and a melting interval of 88 °C to 92 °C. Under UV exposure in the 350 nm to 420 nm region, the molecule undergoes Norrish Type I α-cleavage to generate a 2,4,6-trimethylbenzoyl radical and a diphenylphosphinoyl radical. Unlike benzophenone-amine synergist systems, initiation does not depend on hydrogen abstraction from a co-synergist. That distinction is operationally significant in formulations where amine co-initiators contribute odour, yellowing, or inhibition in acid-functional resins.
Manufacturer release documentation typically reports assay by high-performance liquid chromatography against a TPO reference standard, moisture content by Karl Fischer titration below 0.5%, and a melting interval of 88 °C to 92 °C. Solution colour in a defined acrylate monomer is also reported to detect oxidative impurities. The product is supplied as a dry powder with a density of approximately 1.2 g/cm³ at 20 °C. It is soluble in common acrylate reactive diluents such as 1,6-hexanediol diacrylate and tripropylene glycol diacrylate, but dissolution is faster when the monomer is heated to 40 °C to 50 °C under low-shear mixing. Undissolved crystals can settle and cause filter blockage in roller coating machines equipped with 10 µm to 25 µm bag filters. For UV-LED cure at 365 nm, 385 nm, and 395 nm, TPO is incorporated in concentrations from 0.5 wt% to 3.0 wt% in clear acrylate resins and from 1.0 wt% to 5.0 wt% in titanium dioxide-pigmented systems. Higher loadings can increase surface cure but may raise initial colour and migration potential.
At the air-surface interface, dissolved molecular oxygen competes with acrylate propagation and quenches the excited phosphinoyl species. In a 395 nm LED line source with a peak irradiance of 2 W/cm² to 8 W/cm², a clear acrylate coating containing 1.5 wt% TPO can achieve through-cure at film weights below 10 g/m², but surface tack may persist unless the line speed is reduced to 8 m/min to 15 m/min and the oxygen partial pressure over the coating is minimised by nitrogen inerting. In pigmented white bases at 20 g/m² to 35 g/m², the same lamp array may require a second exposure station because titanium dioxide scatters and absorbs UV while limiting depth of cure. Through-cure is frequently assessed by MEK double rubs to 50 rubs or greater under ASTM D5402; the exact result depends on resin functionality and reactive diluent concentration. A conversion gradient can be monitored by attenuated total reflectance FTIR using the 810 cm⁻¹ acrylate double-bond absorbance against the 1,720 cm⁻¹ carbonyl reference. Excessive TPO loading can reduce depth cure through photon screening at the surface.
In UV-curable inkjet inks for wide-format graphic printers equipped with mercury arc or LED lamp heads, TPO is often combined with a liquid phosphinate such as ethyl (2,4,6-trimethylbenzoyl) phenylphosphinate, commonly identified as TPO-L, to reduce viscosity and prevent nozzle settling. In a production environment where piezo printheads maintain jetting at 35 °C to 45 °C, TPO-L acts as a liquid carrier for the solid TPO and can solvate the crystalline fraction. Inkjet ink viscosity is typically maintained between 8 mPa·s and 25 mPa·s at jetting temperature to avoid missing nozzles. TPO-L has a lower molecular weight of 316.32 g/mol, and its migration propensity through low-density polyethylene packaging films may be higher than that of TPO when assessed by migration testing under Commission Regulation (EU) No 10/2011 for food-contact plastic materials. Published data for this specific configuration is limited; migration trials are required for each printed layer construction and substrate combination.
The substitution of a 120 W/cm mercury arc lamp with a 365 nm LED array changes the spectral overlap of the photoinitiator package. TPO retains usable absorption at 365 nm, 385 nm, and 395 nm, whereas acetophenone-type initiators such as 2-hydroxy-2-methyl-1-phenylpropan-1-one absorb primarily below 330 nm and show lower initiation efficiency under LED heads. On a flatbed line equipped with 365 nm emitters delivering 4 W/cm² peak irradiance at the substrate, a clearcoat containing 2.0 wt% TPO and 2.0 wt% TPO-L can be cured at line speeds of 12 m/min to 18 m/min when the film weight is controlled at 8 g/m² to 12 g/m². A mercury arc lamp may tolerate higher line speed but introduces infrared heating and ozone exhaust handling. LED curing therefore requires reformulation rather than direct substitution of mercury-optimised initiator packages.
In UV-curable clear topcoats for wood and flooring lines, TPO is often combined with a thioxanthone or benzophenone derivative to compensate for the oxygen-rich open-pore surface. A flatline wood coater with a 80 W/cm to 120 W/cm gallium-doped mercury lamp used at 10 m/min to 20 m/min can cure a 20 µm to 40 µm TPO-containing topcoat when the coating is smooth and the wood surface is sealed. Open-grain substrates retain air in the pores, and the resulting oxygen concentration at the pore edges can reduce local cure. Sealer coats are therefore applied before the topcoat, or the line speed is reduced below 8 m/min to increase the dwell time under the lamp.
The selection boundary between TPO, TPO-L, and bis(2,4,6-trimethylbenzoyl)phenylphosphine oxide, commonly designated BAPO, is governed by physical state, molecular weight, absorption, and yellowing. Table 1 summarises the comparison for liquid clearcoat evaluation.
| Parameter | TPO | TPO-L | BAPO |
|---|---|---|---|
| CAS registry number | 75980-60-8 | 84434-11-7 | 162881-26-7 |
| Physical form at 25 °C | Crystalline solid | Liquid | Crystalline solid |
| Molecular weight | 348.37 g/mol | 316.32 g/mol | 418.37 g/mol |
| Melting range | 88–92 °C | Not applicable | 127–135 °C |
| Long-wave UV absorption | 350–420 nm | 360–420 nm | 360–440 nm |
| Typical clearcoat addition | 0.5–3.0 wt% | 0.5–4.0 wt% | 0.2–1.5 wt% |
| Yellowing tendency under high-dose cure | Moderate | Moderate | High |
The comparative data show TPO as the intermediate option between BAPO and TPO-L. BAPO provides greater absorbance beyond 400 nm and higher reactivity in heavily pigmented or UV-A-opaque coatings, but its higher melting range requires heating to 50 °C to 60 °C during dispersion and increases yellowing. TPO-L eliminates recrystallisation in inkjet channels but raises mobility through thin polyolefin films. Comparative evaluations should include ASTM D638 tensile testing of cured free films and pendulum hardness by ISO 1522, because surface tack measurements alone do not indicate through-cure.
In white UV screen ink, titanium dioxide loading above 30 wt% creates a photon-limited cure regime. Formulators use 3 wt% to 5 wt% TPO and may add a BAPO co-initiator at 0.5 wt% to 1.0 wt% to extend absorption to 405 nm. A 395 nm LED source at 4 W/cm² may cure only 10 µm to 20 µm of dry ink per pass when the pigment volume concentration approaches 25% to 30%. Twin-lamp systems or hybrid mercury/LED arrangements are used to extend depth cure. The through-cure result is checked by solvent rub testing under ASTM D5402 and by adhesion cross-cut under ISO 2409.
Moisture and heat accelerate degradation. The powder should be stored below 30 °C in a dry environment; at relative humidity above 60%, pre-drying of the powder or the resin premix is required to avoid water-promoted hydrolysis of the phosphinoyl group. In clear acrylic premixes exposed to ambient light, incomplete dissolved TPO can nucleate recrystallisation over time, forming sediment that changes the effective photoinitiator concentration in the upper layers. Re-dispersal is performed with a rotor-stator high-shear mixer operating at 3,000 rpm to 6,000 rpm, but the batch temperature should be kept below 40 °C because prolonged shear at higher temperatures can initiate thermal polymerisation in low-inhibitor acrylate systems. Viscosity drift greater than 10% after 72 h at 25 °C typically indicates initiator recrystallisation or premature polymerisation and requires corrective reformulation. Avoid combining the premix with strong amines or metal carboxylate catalysts without preliminary storage testing, because premature crosslinking can proceed even in the absence of UV.
During initiation, the TPO absorption maximum near 379 nm decreases as the molecule is consumed, allowing light to penetrate further into the film once surface initiator is depleted. This photobleaching effect is smaller than that of some α-hydroxy ketones but can still influence line-speed optimisation. In a 395 nm LED system operating at 2 W/cm², the first 50 ms to 200 ms of exposure produce the largest change in surface conversion; subsequent exposure through the polymerised surface layer must overcome oxygen that continues to diffuse into the film. The resulting through-cure profile is therefore not linear with irradiance, and doubling the peak irradiance from 2 W/cm² to 4 W/cm² may not double the cure depth. Published data for this specific configuration is limited; dose-response studies should use a radiometer calibrated to the specific LED wavelength and ISO 2409 adhesion testing to confirm intercoat adhesion.
For UV-curing laminating adhesives between flexible films, TPO is used at 1.0 wt% to 2.5 wt% in the adhesive resin. A biaxially oriented polypropylene or polyethylene terephthalate film with transmission above 80% in the 350 nm to 400 nm range allows the LED or gallium-doped lamp to reach the adhesive. If the film contains UV absorber, through-cure fails even at higher photoinitiator loading because the absorbed photons do not reach the bondline. Published data for this specific configuration is limited; adhesion strength should be tested by peel testing under ISO 11339 for flexible-to-flexible constructions and by lap-shear testing for rigid substrates.
From a regulatory standpoint, Jiuri New Material TPO is managed under CLP Regulation (EC) No 1272/2008, with hazard communication based on the harmonised classification for the substance. In the European Union, downstream users are required to include the substance in safety data sheets and consider REACH Regulation (EC) No 1907/2006 restrictions. For application in food-contact printed matter, the final article must comply with Commission Regulation (EU) No 10/2011, which requires migration testing of the printed article rather than reliance on photoinitiator selection alone. Compliance with RoHS Directive 2011/65/EU is typically assessed at the component level; TPO itself does not contain intentionally added lead, mercury, cadmium, hexavalent chromium, PBB, or PBDE.
| Regulatory or test framework | Designation or method | Applicability to TPO-containing materials |
|---|---|---|
| REACH | Regulation (EC) No 1907/2006 | Registration and SDS exposure scenario obligations for EU supply |
| CLP | Regulation (EC) No 1272/2008 | Harmonised classification and labelling requirements for mixtures |
| Food-contact plastics | Commission Regulation (EU) No 10/2011 | Migration testing of final printed article; no direct food-contact approval |
| RoHS | Directive 2011/65/EU | Component-level assessment for restricted heavy metals and brominated flame retardants |
| Adhesion after cure | ISO 2409 | Cross-cut adhesion evaluation of cured films on metal and plastic substrates |
| Solvent resistance | ASTM D5402 | MEK double rub verification of through-cure in production control |
In stereolithography and digital light processing photopolymer resins, TPO is added at 0.5 wt% to 2.0 wt% relative to resin mass. At 405 nm, the absorption tail of TPO is weaker than at 365 nm, so many formulations combine TPO with a bisacylphosphine oxide or a thioxanthone sensitizer to increase cure depth per layer. On a bottom-up DLP printer with a fluorinated ethylene propylene release film, layer separation force is influenced by the degree of conversion at the exposure plane; overcure can increase adhesion to the film. Published data for this specific configuration is limited, but typical exposure energy per layer for a 50 µm slice is in the range of 20 mJ/cm² to 80 mJ/cm² for clear resins containing TPO. The required energy increases when nanofillers or pigments reduce light transmission.