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Photoresist Thinner

    • Product Name: Photoresist Thinner
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 961247
    Product Name Photoresist Thinner
    Chemical Composition Mixture of organic solvents including propylene glycol monomethyl ether acetate (PGMEA) and ethyl lactate
    Appearance Colorless transparent liquid
    Boiling Point 145-170 °C
    Flash Point 42 °C
    Density At 25 C 0.95-1.00 g/cm³
    Vapor Pressure At 20 C 0.3-0.5 kPa
    Evaporation Rate 0.3-0.5 (n-butyl acetate = 1)
    Solubility In Water Partially miscible
    Purity ≥99.5%
    Water Content ≤0.1%
    Shelf Life 12 months
    Storage Temperature 15-30 °C

    As an accredited Photoresist Thinner factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Packaged in 1-gallon HDPE bottle with secure, leak-proof cap, clear hazard labeling, and safety instructions for chemical handling.
    Container Loading (20′ FCL) Photoresist Thinner loaded in 20′ FCL: hazardous liquid in sealed drums/IBCs, palletized, secured, labeled, with proper ventilation and dangerous goods documentation.
    Shipping Photoresist thinner is a flammable, volatile solvent requiring careful transport. Ship as UN1993, Class 3, packing group II/III, with approved containers and proper hazard labeling. Use grounded, ventilated vehicles; avoid heat and incompatible materials. Follow IATA/IMDG/ADR regulations, with Safety Data Sheet and dangerous goods documentation for all shipments.
    Storage Store Photoresist Thinner in a tightly sealed, approved flammable-liquid cabinet in a cool, dry, well-ventilated area. Keep away from ignition sources, heat, sparks, and direct sunlight. Ensure the storage area is grounded and compatible with local fire codes. Avoid storing near strong oxidizers or acids to prevent hazardous reactions.
    Shelf Life Shelf life of photoresist thinner is typically 1–2 years when stored sealed in its original container under recommended conditions.
    Application of Photoresist Thinner

    In semiconductor wafer fabs running i-line/g-line positive photoresists, the thinner is metered into the resist stream or used as a dedicated edge bead removal solution before dynamic dispense on automated coat/develop tracks. The solvent blend is typically based on propylene glycol monomethyl ether acetate (PGMEA) and ethyl lactate, with minor fractions of n-butyl acetate or cyclohexanone added to tune evaporation rate and leveling on silicon, silicon dioxide, and silicon nitride substrates. Viscosity adjustment is carried out against ASTM D445-21 at 25 °C; production lots are commonly thinned from 18–25 cSt to 10–16 cSt by adding 5–15 wt% of the thinner blend, depending on the target dry film thickness, which for i-line resists ranges from 0.8 µm to 3.0 µm at spin speeds of 1500–5000 rpm. The dispense volume on a 200 mm track is 1.5–2.5 mL per wafer, and the EBR nozzle applies a separate stream at 500–800 rpm to remove resist from the wafer edge and backside, producing a clean exclusion zone of 1.0–3.0 mm. Failure modes observed on Tokyo Electron and SCREEN coat/develop tracks include edge bead re-deposition when the EBR solvent evaporation rate is too high, creating post-develop residues at the wafer apex. The operational window is tight: relative humidity above 60 % increases water uptake in the wet resist film, causing scum formation in unexposed areas after development, and room temperature excursions above 23 °C accelerate PGMEA loss from open thinner reservoirs, shifting viscosity outside the 10–16 cSt control band within one shift in shallow-bath dispense systems. Incompatible materials include strong oxidizing acids, alkali developers, and amine-based additives that can accelerate ester hydrolysis. Compliance documentation for this application references ISO 14644-1:2015 Class 1 for particle control at wafer level, SEMI S2-0718 for equipment safety, REACH Regulation (EC) 1907/2006 for solvent registration, and RoHS Directive 2011/65/EU where applicable to final device homologation. Terminal products include logic, memory, and power management integrated circuits at nodes where 365 nm and 436 nm lithography remains in use for non-critical layers.

    Representative process-control response for a PGMEA/ethyl lactate thinner in a DNQ-novolac i-line resist on 200 mm silicon wafers at 23 °C and 45 % relative humidity; data are control ranges, not universal specifications.
    Thinner additionKinematic viscosity at 25 °CDry film thickness at 3000 rpmProcess observation
    0 wt%18–25 cSt2.4–3.0 µmBaseline edge bead width 3 mm; leveling limited over 0.5 µm steps
    5 wt%14–18 cSt1.8–2.2 µmLeveling improves; edge bead width 2–3 mm
    10 wt%11–14 cSt1.2–1.6 µmTarget window for 1.2 µm logic layer
    15 wt%8–11 cSt0.8–1.0 µmPinholes on step topographies above 0.5 µm
    20 wt%6–9 cSt0.5–0.8 µmPattern collapse risk for 0.5 µm line/space

    When Copper Pillar Plating Requires a Solvent That Does Not Shift the Bath pH

    Thick diazonaphthoquinone/novolak resists used as plating masks for copper pillar, redistribution layer, and solder bump processes are supplied at solids loadings from 35 wt% to 50 wt%, with initial kinematic viscosities often above 500 cSt at 25 °C. The thinner system for this application shifts from pure PGMEA toward a mixture of PGMEA, cyclopentanone, and 2-heptanone; cyclopentanone lowers evaporation rate and improves leveling across 30–100 µm-thick films, while PGMEA maintains coat-develop compatibility with standard 2.38 wt% tetramethylammonium hydroxide developers. On automated wafer processing equipment such as the EV Group EVG 150 and SUSS MicroTec ACS 200 series, addition rates of 5–20 wt% are used to bring the resist to a spin-coating viscosity between 300 cSt and 800 cSt. The process conflict is acute: dilution above 20 wt% commonly produces solvent retention in the lower resist region after post-apply softbake, and the residual solvent shifts the post-exposure bake completion point, leading to undercut sidewall profiles after development and exposing copper seed layer to plating bath attack. Operational boundaries therefore include a maximum thinner addition of 20 wt% for films above 50 µm and a softbake ramp of 2–3 °C/min to avoid skin formation. The softbake itself is typically performed at 90–110 °C on a proximity hotplate, with end-point determined by residual solvent weight loss measured against the same resist lot on a Sartorius moisture analyzer. Because the photoresist pattern must survive acidic copper sulfate electroplating with pH below 1, any thinner imported into the plating bath through carryover must not contain amine or phosphate species; this is controlled by incoming lot metal-ion and cation rejection tests referenced in the supplier certificate of analysis, with detection limits below 10 ppb for sodium, potassium, and calcium. Compliance documentation references SEMI S2-0718, ISO 14644-1:2015 Class 1–5 depending on the packaging step, and REACH Regulation (EC) 1907/2006 Annex XVII restrictions for chlorinated solvents. Terminal products include copper pillar interconnects, solder bumps for wafer-level chip-scale packages, and redistribution layer structures.

    How Is Slit Coating Meniscus Stability Maintained for Color Filter Resists?

    On Gen 6 to Gen 8.5 flat-panel coating lines, color filter, black matrix, and photo-spacer resists are coated on glass substrates by slot die or slit coater; the coating uniformity target is typically below 3 % total thickness variation across the plate. The thinner composition for this application is formulated with PGMEA and 3-methoxy-3-methyl-1-butanol or similar high-boiling glycol ether esters to reduce viscosity without collapsing the wet film edge. Process data from coating lines indicate that the resist solution is prepared at a solids content of 18–25 wt% and then thinned to 14–17 wt%, corresponding to a kinematic viscosity of 2–4 mm²/s at 25 °C when measured by ISO 3219 rotational viscometry. The slot die gap is held between 50 µm and 150 µm, the coating speed ranges from 20 mm/s to 100 mm/s, and the wet film is dried under a sequential hotplate or air-float oven. Adding thinner below 10 wt% does not eliminate transverse ribbing; addition above 25 wt% drops the black matrix optical density below 3.0 per the panel maker's incoming inspection and causes pinhole defects in the 1.5–2.5 µm final film. Meniscus stability is also sensitive to the vapor pressure balance: a thinner with excessive high-volatility content raises the local viscosity at the meniscus, creating streak defects parallel to the coating direction. Humidity above 60 % relative to 23 °C is known to produce mura after development because water ingress into the film before pre-bake inhibits acid-catalyzed crosslinking of the negative-tone acrylic matrix. Equipment includes flat-panel coater tools from SCREEN and Toray, with exhaust velocity controlled at the die lip to 0.2–0.5 m/s to avoid solvent flash. Compliance follows ISO 14644-1:2015 Class 5 for panel fab cleanroom operation, SEMI S2-0718 for coater safety, and IEC 62321-3-1:2013 for restricted substance test methods in final display modules. Terminal products include active-matrix LCD televisions, OLED smartphone displays, and in-cell touch panels.

    Compliance and test method matrix for photoresist thinner use by downstream segment.
    Downstream segmentStandard or regulationTest method or clauseControlled parameter
    Semiconductor i-line/g-line spin coatingASTM D445-21Kinematic viscosity at 25 °CResist thinning ratio
    Semiconductor wafer track EBRISO 14644-1:2015 Class 1Airborne particle monitoringWafer-level particle contamination
    Thick resist for copper pillar platingREACH (EC) 1907/2006 Annex XVIISupplier CoA, ICP-MSNa, K, Ca below 10 ppb
    Flat-panel slit coatingISO 3219Rotational viscosity at 25 °CMeniscus stability, film thickness
    PCB liquid photoimageable solder maskIPC-SM-840E / ASTM D1200-10Efflux viscositySpray viscosity window
    Photomask blank rinse and EBRASTM D1078-11 / ASTM E203-16Distillation range and water contentSolvent purity, low moisture
    MEMS spray coatingISO 14644-1:2015 Class 5 / SEMI S2-0718Particle count, equipment safetyCleanroom and tool safety

    For high-density interconnect PCB spray lines, liquid photoimageable solder mask and primary resist formulations are adjusted with a thinner blend based on dipropylene glycol monomethyl ether acetate and ethyl 3-ethoxypropionate; the addition of 3–8 wt% reduces efflux viscosity measured by ASTM D1200-10 to the 100–200 s range required for HDI spray equipment, and the cured film must meet IPC-SM-840E class T for solder mask adhesion, hardeners, and dielectric withstand.

    Photomask Blank Rinse and EBR Metal-Ion Budget Under Class 1 Airflow

    Photomask and reticle blank processing uses photoresist thinner not only for dilution but also as a dedicated edge bead removal and backside rinse solvent on 6025 quartz and 6-inch blank formats. The material must meet low-metal-ion specifications because reticle-level contamination transfers to the wafer during exposure; supplier certificates of analysis commonly report sodium, potassium, and calcium below 10 ppb, although published data for a unified public specification is limited. On HamaTech MaskTrack and SUSS MicroTec mask processing systems, the EBR solvent is dispensed during slow spinning at 300–700 rpm after resist coating, removing the edge bead from the blank perimeter and preventing flake generation in the exposure tool vacuum chuck. The thinner composition is typically high-purity PGMEA with a distillation range between 145–146 °C according to ASTM D1078-11, and water content is held below 0.05 wt% by Karl Fischer titration per ASTM E203-16. Because photomask resists are often electron-beam or 193 nm-laser resists with different polymer solubility parameters, the thinner is not interchangeable with standard i-line EBR solvents unless the solubility match is verified by contrast curve and dark erosion testing. Operational boundaries include a particle cleanliness level below 10 particles/mL at 0.2 µm as measured by an in-line particle counter, and the exclusion of plasticizer-containing tubing that can leach phthalates into the solvent stream. The application is governed by ISO 14644-1:2015 Class 1 for mask blank handling and SEMI S2-0718 for equipment safety. Terminal products include binary and phase-shift photomasks for 248 nm and 193 nm lithography.

    Spray-Coated MEMS Resists Demand Thinning Profiles That Preserve Sidewall Coverage

    In microelectromechanical systems with cavity depths from 100 µm to 500 µm, spray-coated photoresist layers must cover vertical sidewalls without bridging at the cavity opening. The thinner for this application is enriched in cyclopentanone and 2-heptanone, with a lower evaporation rate than PGMEA-only blends, because an atomized droplet must remain liquid long enough to coalesce on silicon or glass sidewalls after leaving a 40–60 kHz ultrasonic nozzle. Typical addition levels in a DNQ-novolac or thick epoxy resist are 10–30 wt%, bringing the kinematic viscosity measured by ASTM D445-21 from 800–2000 cSt to 100–300 cSt for spray deposition. Process limits are observed on EVG and SUSS spray coat modules: thinning above 35 wt% causes pinholes at the bottom of high-aspect-ratio cavities because the low-viscosity film drains before softbake, and thinning below 10 wt% produces dry-spray roughening with a measured surface roughness above 80 nm root mean square on 200 mm wafers. An HMDS vapor prime at 130–150 °C for 60–120 s is applied before resist coating; excessive thinner flash-off at the nozzle can remove this adhesion layer at the cavity rim, leading to localized delamination after development. Softbake is carried out at 95–115 °C on a ramped hotplate for 10–20 min, with exhaust airflow limited to 0.1–0.2 m/s to avoid forming a skin that traps solvent in the thickest cavity regions. Published data for thinner-induced sidewall thickness uniformity on arbitrary MEMS topographies is limited; therefore, process engineers use cross-section SEM on a per-lot basis with a fixed panel of cavity aspect ratios, a practice referenced in internal process qualification documents. Compliance documentation includes ISO 14644-1:2015 Class 5 for MEMS wafer processing, SEMI S2-0718 for equipment safety, and REACH Regulation (EC) 1907/2006 for solvent registration. Terminal products include inertial measurement units, pressure sensors, microfluidic devices, and uncooled infrared microbolometers.

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    Certification & Compliance
    More Introduction

    Photoresist Thinner PRT-2300

    Photoresist Thinner PRT-2300 is a semiconductor lithography solvent blend supplied in 1 L, 4 L, and 20 L fluoropolymer or glass containers. The product is a filtered mixture of propylene glycol monomethyl ether acetate and propylene glycol monomethyl ether, with a target mass ratio of 80:20. It is used as a viscosity adjustment diluent for positive-tone novolac/diazonaphthoquinone resists and selected chemically amplified resists, and as a cup solvent for edge bead removal, backside rinse, and nozzle cleaning. The thinner contains no photoactive compound, no acid generator, and no surfactant. Its primary function is to reduce resist viscosity while preserving dissolution selectivity and photospeed.

    Specification for Photoresist Thinner PRT-2300
    PropertySpecificationMethod
    AppearanceClear, colorless liquid free of suspended matterASTM D4176
    Density0.970–0.985 g/cm³ at 20 °CASTM D4052
    Kinematic viscosity1.20–1.40 mm²/s at 25 °CASTM D445
    Water≤0.050 wt%ASTM D5127
    Acidity as acetic acid≤0.010 wt%ASTM D1613
    Color≤10 Pt-CoASTM D1209
    Refractive index1.402–1.406 at 20 °CASTM D1218
    Distillation rangeInitial boiling point ≥138 °C; dry point ≤150 °CASTM D1078
    Trace metals by ICP-MSEach cation ≤20 ppb; total ≤100 ppbClosed-vessel digestion with ICP-MS
    Particle count≥0.3 µm particles ≤200/mL; ≥0.5 µm particles ≤50/mLLiquid particle counter
    Fill filtration0.05 µm PTFE membraneCleanroom fill

    What Process Window Does PRT-2300 Maintain in Spin-Coating and Edge Bead Removal?

    On 200 mm and 300 mm coater/developer tracks, PRT-2300 is dispensed through point-of-use filters with pore size 0.05 µm or 0.1 µm. Open-bowl exhaust must maintain solvent vapor concentration below 25% of lower explosive limit; track interlocks typically require exhaust face velocity of 0.8–1.2 m/s. For thickness adjustment, dilution addition rates from 2 wt% to 10 wt% are used depending on resist solids and target film thickness. A 5 wt% addition to a 10 cP resist can reduce coated thickness by 8–15% at constant spin speed, based on spin-curve runs on 200 mm tracks with open-bowl spinner configurations. The exact thickness shift requires on-site spin-curve generation because film thickness depends on resist batch, substrate topography, and exhaust conditions. The processing window narrows at high addition levels: above 10 wt%, some novolac resists show edge profile rounding and increased film thickness non-uniformity above 3% across the wafer. Published data for this specific configuration is limited.

    For edge bead removal, precision nozzles deliver 1.0–2.5 mL per backside rinse and edge cut on 300 mm tracks. Bowl rinse lines should be constructed of PTFE, HDPE, or stainless steel because PGMEA/PGME blends can swell polypropylene fittings after extended contact. At relative humidity above 60%, an open reservoir can absorb more than 0.1 wt% water within a 12 h shift; water uptake in chemically amplified resists may alter photospeed and cause surface defects. A nitrogen blanket on the reservoir is recommended when track humidity cannot be maintained below 45% RH. Softbake conditions must remain within ±2 °C of the process recipe when PRT-2300 is used as a diluent, because residual PGME can shift the evaporation tail and influence the post-exposure bake response in deep ultraviolet resists.

    Material Differences Between PRT-2300 and Acetone, PGMEA, Ethyl Lactate, and Methyl Ethyl Ketone

    PRT-2300 is not interchangeable with common ketone or alcohol diluents in lithography tracks. Acetone and methyl ethyl ketone have higher vapor pressure and lower flash point, which increase evaporative cooling and can reduce wafer surface temperature below the dew point. Water condensation on the resist film produces haze, dewetting, and photospeed drift. Ethyl lactate has higher viscosity and slower evaporation, which may improve leveling in some thick resists but can leave higher residual solvent after softbake. PGMEA-only diluents provide a narrower polarity range; the addition of PGME in PRT-2300 modifies surface wetting and reduces tailing during edge bead removal without dropping the closed-cup flash point to the level of methyl ethyl ketone.

    Representative Physical and Safety Comparisons
    SolventDensity at 20 °CKinematic viscosity at 25 °CBoiling point or rangeClosed-cup flash point
    PRT-23000.970–0.985 g/cm³1.20–1.40 mm²/s138–150 °C38–42 °C
    PGMEA0.966 g/cm³1.1–1.2 mm²/s146 °C42 °C
    Acetone0.791 g/cm³0.32 mm²/s56 °C-17 °C
    Methyl ethyl ketone0.805 g/cm³0.43 mm²/s79.6 °C-9 °C
    Ethyl lactate1.03 g/cm³2.6 mm²/s154 °C46 °C

    The closed-cup flash point of PRT-2300 keeps the material in the combustible liquid classification rather than the flammable liquid range occupied by acetone and methyl ethyl ketone. This distinction affects storage, exhaust, and spill-control requirements on manufacturing lines. However, PRT-2300 should still be stored away from oxidizers and ignition sources because the vapor can accumulate in poorly ventilated cup enclosures. Replacing PRT-2300 with acetone in an edge bead removal loop may extract residual resist components and leave a faster-drying film, but the lower flash point and higher evaporation rate create a narrower safe operating window in enclosed track plumbing.

    Filtration, Trace Metal, and Packaging Controls

    PRT-2300 is filled in an ISO Class 5 cleanroom using stainless steel lines with PTFE and perfluoroelastomer seals. The product is filtered through a 0.05 µm PTFE membrane at fill, and each lot is released after particle counting, water analysis, and trace metal analysis. Long-term storage in high-density polyethylene is not recommended because solvent permeation can allow airborne contamination to enter the container. Fluoropolymer and glass containers are preferred for preserving low-metal specifications. The product should be kept in original sealed containers at 15–25 °C and protected from direct sunlight. Open-reservoir use beyond 8 h without nitrogen blanketing may increase water content above the specification limit; the material should be re-tested before use if the reservoir has been exposed to atmospheric moisture for longer than one shift.

    The product is labeled in accordance with Regulation (EC) No 1272/2008. The safety data sheet lists the closed-cup flash point, distillation range, and storage conditions in Section 9. The product does not contain substances of very high concern above 0.1 wt% according to the REACH Candidate List. RoHS Directive 2011/65/EU Annex II substances are not present above 0.1 wt% in the homogeneous material as supplied. The product is not intended for direct food-contact use and is not an FDA-regulated food adjunct. Industrial hygiene controls should follow the occupational exposure limits in the safety data sheet.

    When Backside Rinse and Nozzle Clean Demand a Low-Metal, Low-Water Solvent

    For backside rinse on copper or tungsten interconnects, the low-metal grade PRT-2300-LM is specified with each cation ≤10 ppb and total metals ≤50 ppb. The low-metal grade is used after lift-off resists and for nozzle clean sequences where residual metal ions can contaminate exposed metal surfaces. Nozzle materials should be PTFE or stainless steel 316L; polypropylene fittings may stress-crack after 6–12 months of PGMEA exposure and are not recommended for permanent solvent lines. A nitrogen dry step at 2–3 L/min per nozzle after solvent flush prevents liquid holdup in dead-legs and reduces the risk of downstream particle shedding. The solvent flush cycle should be interlocked with the track exhaust sensor so that cup ventilation remains above 25% LEL before dispense. Published data for this specific configuration is limited.

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