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Positive Photoresist Developer Electronic/EL Grade

    • Product Name: Positive Photoresist Developer Electronic/EL Grade
    • 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 764477
    Producttype Positive Photoresist Developer
    Grade Electronic/EL
    Appearance Clear colorless liquid
    Physicalstate Liquid
    Chemicalidentity Tetramethylammonium hydroxide (TMAH) aqueous solution
    Tmahconcentration 2.38%
    Densityat25c 1.00 g/cm3
    Phat25c 13.0
    Refractiveindex 1.335
    Assaytmah 2.38 ± 0.02%
    Sodiumimpurity ≤ 1 ppb
    Potassiumimpurity ≤ 1 ppb
    Ironimpurity ≤ 10 ppb
    Copperimpurity ≤ 1 ppb
    Particulatematter ≤ 10 particles/mL above 0.2 µm
    Nonvolatileresidue ≤ 10 ppm

    As an accredited Positive Photoresist Developer Electronic/EL Grade factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Packaged in a 4 L amber HDPE container with tamper-evident cap, safety labels, and traceability data for Electronic/EL Grade positive photoresist developer.
    Container Loading (20′ FCL) 20′ FCL loading of Positive Photoresist Developer (Electronic/EL Grade) requires secure, labeled, leak-proof packaging with proper segregation for safe transport.
    Shipping Positive Photoresist Developer Electronic/EL Grade is TMAH-based and typically ships as UN 1835, Tetramethylammonium hydroxide solution, Class 8 (Corrosive), Packing Group II. Use UN-approved corrosion-resistant packaging with required hazard labels and documentation. Keep away from acids, prevent leaks, and follow applicable ADR, IATA, and IMDG regulations.
    Storage Store in a tightly sealed, original container in a cool, dry, well-ventilated area away from direct sunlight, heat, and ignition sources. Keep separated from acids, oxidizing agents, and incompatible materials. Avoid contamination and moisture ingress. Maintain consistent temperatures; do not freeze. Follow manufacturer’s shelf-life guidelines and handle with clean, dedicated equipment.
    Shelf Life Shelf life is typically 12 months when stored tightly sealed in original container at controlled room temperature, away from light and heat.
    Application of Positive Photoresist Developer Electronic/EL Grade

    In 300 mm front-end logic and memory wafer fabrication, positive-tone i-line and KrF photoresist development is executed with metal ion-free aqueous TMAH developer delivered through a temperature-controlled point-of-use dispense loop. The product is controlled to ≤0.1 ppb individual cation impurities including Na, K, Fe, Cu, Al, Zn, Ca, Cr, Ni, Mg, Mn, and Pb, with total trace metals ≤0.3 ppb, chloride ≤5 ppm, total organic carbon ≤10 ppm, and particle counts ≤20 particles/mL at 0.2 µm sizing. Monitoring paths follow laser particle counter calibration under ISO 21501-4:2018 and ultrapure water quality per ASTM D5127-13 Type E-1 equivalent. Facility compliance integration includes cleanroom compatibility with ISO 14644-1:2015 Class 1 to 3, dispense pump voltage sag immunity per SEMI F47-0706, and chemical distribution exposure control per SEMI S2-0814. The addition ratio at the point of use is typically 2.38% ± 0.02% by weight TMAH without bulk dilution; low-contrast processes or top-coat-compatible tracks may dilute 1:1 or 1:3 with ultrapure water to produce 1.19% or 0.79% working solutions. The downstream process includes dehydration bake, hexamethyldisilazane priming, spin coating of 90–120 nm i-line photoresist, softbake at 90–110 °C, exposure on immersion lithography scanners, post-exposure bake at 110–130 °C, puddle development using 25–35 mL per 200 mm wafer or 55–75 mL per 300 mm wafer, deionized water rinsing at 0.5–1.0 L per wafer, and spin drying at 1,500–2,500 rpm. Critical dimension stability demands developer temperature control within ±0.3 °C; TMAH-inhibited novolac dissolution exhibits an apparent activation energy near 20–25 kJ/mol, and development rate can shift by 0.5–1.5 nm/s per 0.1% TMAH concentration change. Extended rinse contact with exposed aluminum pads is restricted to ≤60 s because alkaline attack above pH 13 can roughen pad metallization. Terminal products include logic processors, SRAM, DRAM, and 3D NAND devices from 90 nm to sub-5 nm design rules.

    How Does Thick-Resist Patterning Alter Developer Replenishment in Wafer-Level Bumping?

    Wafer-level bumping and fan-out packaging lines that use positive-tone novolac resists coated at 5 µm to 120 µm final thickness after softbake require the same metal ion-free TMAH specification to prevent contamination of Cu/Ni/Sn-Ag electroplating baths. Compliance in this sector is governed by JEDEC JESD22-A104D for thermal cycling, IPC-A-610G for downstream accept/reject decisions, IEC 61340-5-1:2016 for electrostatic discharge control, and RoHS Directive 2011/65/EU for finished bump and package material compatibility. The developer addition strategy for thick-resist processing commonly uses a 1:1 or 1:2 dilution of 2.38% TMAH with ultrapure water for initial breakthrough, followed by undiluted 2.38% TMAH during the main dissolution phase; some high-aspect-ratio copper pillar lines start at 0.79% TMAH to limit surface dark erosion and then switch to 1.19% TMAH after 10–15 s of puddling. The downstream production sequence includes seed layer sputter, dynamic dispense coating at 800–1,200 rpm, hotplate softbake at 100–120 °C, projection or stepper exposure at 1,500–3,500 mJ/cm², and single-wafer spray or puddle development. On production-scale tools, thick-film dissolution generates high resist loading in recirculated developer baths; absorbed CO₂ forms carbonate species and drives pH from 13.2 to 12.6 within one shift unless fresh developer is replenished at 0.15–0.35 L per wafer cassette. The main process conflict is lateral undercut versus vertical dissolution: when TMAH concentration exceeds 1.35% at 23 °C, isotropic undercut on 20 µm lines at 50 µm pitch can reach 1.0–2.5 µm per side and violate bump critical dimension. Endpoint control uses multi-wavelength reflectometry or conductivity-based spiking; a 2.38% working bath is commonly maintained at 45–55 mS/cm, and automatic dosing resets conductivity when alkalinity falls outside the target band. Rinsing after development is limited to ≤30 s because exposed copper seed layers etch in alkaline TMAH above pH 12. Terminal product types include copper pillar solder-capped bumps at 40 µm to 80 µm pitch, redistribution layer traces at 2/2 µm to 10/10 µm line/space, and fan-out wafer-level package dielectrics.

    For semi-additive processing and modified semi-additive processing on flip-chip IC substrates, metal ion-free TMAH developer is specified because high-resolution liquid positive photoresist must be developed on ABF build-up film without attacking electroless copper seed layers. The relevant industry compliance designations are IPC-6012E Class 3 for rigid substrate acceptance, IPC-4101E for laminate and prepreg performance, IPC-TM-650 2.3.25 for ionic contamination, and REACH Regulation (EC) No 1907/2006 for chemical registration. In this application, the developer is diluted from 2.38% to 0.5–1.0% by weight TMAH with ultrapure water in the day tank; lower working concentration reduces lateral undercut on 5/5 µm and 2/2 µm line/space features exposed through semi-transparent copper layers. The downstream process includes laser via formation in 5–15 µm ABF dielectric, desmear, electroless copper flash at 0.5–1.5 µm, photoresist lamination or slot-coating at 3–7 µm dry thickness, direct imaging or mask projection at 355 nm or 405 nm, horizontal conveyorized spray development at 2.0–3.5 kg/cm² spray pressure, cupric chloride or formic acid copper electroplating at 2.0–3.5 A/dm², and alkaline resist stripping. Conveyorized lines maintain TMAH concentration by conductivity dosing between 8 mS/cm and 18 mS/cm depending target working bath. A processing boundary applies: TMAH concentration above 1.2% at bath temperature above 30 °C can roughen ABF surfaces and cause adhesion loss at the plated copper interface, so bath temperature is clamped to 24–26 °C and contact time is limited to 45–90 s. Terminal products are flip-chip chip-scale package substrates, processor package substrates, and high-density memory package substrates with final line/space capability down to 2/2 µm.

    Compliance designations and working concentrations by downstream sector
    Application sectorPrimary compliance designationsTMAH working concentrationRepresentative production equipment
    Front-end semiconductorISO 14644-1:2015 Class 1–3; SEMI F47-0706; SEMI S2-08142.38% undilutedCoater/developer track with puddle dispense
    Advanced wafer-level packagingJEDEC JESD22-A104D; IPC-A-610G; RoHS 2011/65/EU0.79–2.38% stepwise dilutionSingle-wafer spray/puddle tool with conductivity spiking
    IC substrate SAP/mSAPIPC-6012E Class 3; IPC-4101E; IPC-TM-650 2.3.250.5–1.0% dilutedHorizontal conveyorized spray chamber
    LTPS-TFT displayIEC 61747-1-1:2014; IEC 62341-1-2:2014; SEMI S2-08142.38% undilutedLinear coater/developer for Gen 6/8.5 glass
    MEMSIEC 62047-1:2016; SEMI F47-0706; ASTM F24-202.38% undiluted; 1:2 for lift-offWet bench or single-wafer spray with 0.05 µm filtration
    Compound semiconductorRoHS 2011/65/EU; REACH 1907/2006; JEDEC JESD22-A108D2.38% undiluted; 1:1 for thick resistSingle-wafer spray at 500–1000 rpm

    When LTPS-TFT Backplanes Require Channel-Safe Alkaline Development After Dry Etch Patterning

    Low-temperature polycrystalline silicon thin-film transistor backplanes for high-resolution AMOLED and LCD panels use positive-tone photoresist and TMAH developer at gate, source/drain, and pixel define mask steps. Compliance in flat panel display manufacturing is framed by IEC 61747-1-1:2014 for LCD display cells, IEC 62341-1-2:2014 for OLED display modules, ISO 14644-1:2015 Class 5 to 7 cleanrooms for large-substrate handling, and SEMI S2-0814 for coater/developer equipment safety. The developer is used at 2.38% TMAH as supplied in the central chemical dispense system; some Gen 6 and Gen 8.5 lines dilute to 1.19% for lift-off strips, but the critical dimension step retains the 2.38% concentration. The addition ratio is controlled through the developer recirculation tank, with fresh chemical feed at 0.5–1.0 L per display cassette and concentration verification by acid-base titration against 0.1 N hydrochloric acid standard. The downstream production sequence includes slit coating of photoresist on 1,500 mm × 1,850 mm glass substrates, proximity or projection exposure at 365–436 nm, puddle development on linear coater/developer tracks, DI water rinse, and spin dry; subsequent steps include dry etch, ion implantation, and photoresist stripping. The critical process conflict is mobile ion contamination in the thin-film transistor channel. Potassium and sodium in developer must remain below 0.1 ppb, because a single wafer with 1×10¹¹ ions/cm² mobile ion contamination can shift threshold voltage by several hundred millivolts. Fabs therefore deploy online ion chromatography and ICP-MS at day tank recirculation with alarm limits at 0.5 ppb total metals. Terminal products include smartphone and wearable AMOLED displays, high-resolution LTPS LCD panels, and plastic OLED display backplanes.

    Developer Filtration and Defect Density in MEMS Sacrificial Layer Definition

    MEMS devices using surface micromachining and bulk micromachining require positive photoresist development before deep reactive ion etching or release etching. Electronic-grade TMAH developer is selected because it leaves no metallic residue on Al, Ti, SiO₂, or Si₃N₄ surfaces after DI rinse. Compliance includes IEC 62047-1:2016 for MEMS device classifications, SEMI S2-0814 for tool safety, SEMI F47-0706 for dispense system voltage sag immunity, and ASTM F24-20 for airborne particle counting in cleanrooms. The addition ratio in MEMS fabs is typically undiluted 2.38% TMAH for standard mask definition, but for lift-off processes with image reversal resists the developer may be diluted 1:2 with ultrapure water to slow the first dissolution step and preserve undercut profiles. The downstream production process includes wafer cleaning, oxide or nitride deposition, photoresist coating at 1.5–5.0 µm thickness, step-and-repeat exposure, development on a wet bench or single-wafer spray tool, hardbake at 90–130 °C, DRIE at 10–100 µm depth, and release etching. Quality control points include final filtration of developer through 0.05 µm polytetrafluoroethylene or high-density polyethylene filters at the dispense nozzle, and wafer-level defect inspection after development using laser scattering systems calibrated to 0.3 µm equivalent polystyrene latex spheres. The process boundary is that TMAH at 23 °C slowly etches silicon at approximately 0.1–0.3 nm/min, so extended immersion beyond 120 s on bare silicon test pads can alter surface roughness. Terminal products include inertial sensors such as accelerometers and gyroscopes, pressure sensors, microfluidic lab-on-a-chip devices, and digital micromirror arrays.

    In compound semiconductor and optoelectronic wafer fabs processing GaAs, InP, GaN-on-SiC, and sapphire substrates, positive-tone photoresist development for gate, ridge, and via mask openings uses TMAH developer to prevent trace metal contamination of III-V surfaces. Industry compliance designations include RoHS Directive 2011/65/EU, REACH Regulation (EC) No 1907/2006, JEDEC JESD22-A108D for powered device reliability testing, and ISO 14644-1:2015 Class 4 to 6 cleanroom environments. The developer addition ratio is typically 2.38% TMAH undiluted for thin resist layers of 0.5–1.0 µm; for wide-bandgap GaN power amplifiers with 3–6 µm thick resists, a 1:1 dilution with ultrapure water is employed to extend development time and improve line edge roughness. The downstream process includes substrate cleaning, adhesion promoter application, spin coating, contact or projection lithography at 365 nm or electron beam direct write, post-exposure bake, development on single-wafer spray tools at 500–1,000 rpm, rinse, and descum. For lift-off metallization, the TMAH development step is paired with chlorobenzene soak or image reversal bake; undercut is controlled by maintaining TMAH bath temperature at 21–23 °C, with development time between 60 s and 180 s depending resist thickness. Exposed III-V surfaces can undergo native oxide etching in alkaline media; contact time on InP and GaAs is limited to ≤60 s after breakthrough to avoid surface roughening. Terminal products include GaN radio-frequency power amplifiers, edge-emitting laser diodes, vertical-cavity surface-emitting lasers, and micro-LED arrays for pixel-level display modules.

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    Certification & Compliance
    More Introduction

    Positive Photoresist Developer Electronic/EL Grade, designated EL-D238, is an aqueous alkaline developer formulated from tetramethylammonium hydroxide (TMAH; CAS 75-59-2) at a nominal concentration of 2.38 wt% in high-purity water. The Electronic/EL Grade designation refers to the control of trace cation load, anion background, particle count, and nonvolatile residue rather than to a change in active chemistry. The product is intended for metal-sensitive positive-tone photoresist processing in semiconductor, MEMS, and advanced packaging lines.

    At the resist surface, the imagewise development reaction proceeds through the alkaline dissolution of exposed diazonaphthoquinone-novolak photoresist. Exposed diazonaphthoquinone undergoes ketene-mediated conversion to indene carboxylic acid in the presence of water; the acid ionizes in the developer and increases the dissolution rate of the novolak matrix. Unexposed diazonaphthoquinone remains as a dissolution inhibitor. The developer therefore supplies free hydroxide that deprotonates phenolic hydroxyls in exposed novolak. The pH of the solution is maintained between 12.50 and 13.00 at 25 °C. A pH below this range slows clearing, while a pH above this range increases dark erosion of unexposed resist edges.

    Composition and Analytical Release Specifications

    Lot release for EL-D238 is generated by acid-base titration, ion chromatography, collision-cell inductively coupled plasma mass spectrometry, light-obscuration particle counting, and gravimetric nonvolatile residue analysis. The titrant is 0.1 N hydrochloric acid standardized against NIST-traceable sodium carbonate, with potentiometric end-point detection to avoid indicator interference. Density and refractive index are used as rapid binary composition checks after blending. The specification limits shown in Table 1 are representative release criteria for the EL-D238 model when packaged in fluoropolymer or high-density polyethylene containers.

    PropertySpecificationTest method
    TMAH concentration2.38 ± 0.02 wt%Acid-base titration with 0.1 N HCl
    Water contentBalanceASTM E203-16 Karl Fischer titration
    pH at 25 °C12.50–13.00ASTM E70-22
    Density at 25 °C1.022–1.028 g/mLASTM D4052-22
    Refractive index at 25 °C1.367–1.371ASTM D1218-21
    Each metal ion, Na, K, Mg, Ca, Fe, Cu, Zn, Ni, Al, Cr≤ 10 ppbEPA Method 6020B ICP-MS
    Total heavy metals≤ 50 ppbEPA Method 6020B
    Chloride≤ 50 ppbEPA Method 300.1 ion chromatography
    Nitrate≤ 100 ppbEPA Method 300.1
    Sulfate≤ 100 ppbEPA Method 300.1
    Particles ≥ 0.5 µm≤ 25 counts/mLISO 21501-1:2011
    Nonvolatile residue≤ 20 ppmASTM D1353-13(2021)

    Trace-metal data are blank-subtracted and generated with inline internal standards under cleanroom-compatible sampling procedures. In routine production lots, sodium and potassium are typically below 5 ppb, but the release ceiling is held at 10 ppb per element because packaging and sampling can introduce variable cleanroom contributions. The water source used for dilution should meet or exceed 18.2 MΩ·cm resistivity and ≤ 20 ppb total organic carbon before blending. If the water source exceeds these limits, the cation and nonvolatile residue specifications in Table 1 become difficult to maintain.

    What Distinguishes EL Grade from Reagent-Grade or Technical Developers?

    The active alkalinity is not the primary differentiator. A technical-grade TMAH solution at the same 2.38 wt% concentration will clear exposed positive resist, but it can introduce sodium, potassium, calcium, and iron at levels from 0.1 ppm to 10 ppm and may carry uncontrolled particulate debris. Sodium hydroxide or potassium hydroxide developers can provide faster clearing at equivalent normality, but their residual cation burden on silicon surfaces ranges from 1 × 10^12 to 1 × 10^14 atoms/cm² unless unusually aggressive rinsing is used. For gate oxide thicknesses at or below 2 nm, mobile ion contamination above 1 × 10^10 atoms/cm² may shift threshold voltage. Alkali-metal hydroxide developers are therefore restricted to high-voltage or non-electronics applications.

    ParameterEL-D238Technical-grade TMAHNaOH/KOH developer
    Active cationQuarternary ammonium, low metal backgroundQuarternary ammonium plus uncontrolled metal impuritiesSodium or potassium cation
    Alkali metal concentration≤ 10 ppb each Na and K100–10,000 ppb range> 100,000 ppb active alkali cation
    Particle control ≥ 0.5 µm≤ 25 counts/mLNot normally specifiedOften > 500 counts/mL
    Post-bake residue typeVolatile amine decomposition productsVolatile amine plus metallic residueAlkali silicates and carbonates
    Compatibility with metal-sensitive devicesIntended for front-end and bumping linesLimited to non-critical resist strippingNot recommended for MOS gate applications

    The difference is most clearly seen on bare silicon witness wafers analyzed by vapor phase decomposition inductively coupled plasma mass spectrometry. After EL-D238 puddle development and ultrapure water rinse, combined sodium and potassium values are typically below 1 × 10^10 atoms/cm². Technical TMAH can produce values one to three orders of magnitude higher, and sodium hydroxide developers can leave 1 × 10^12–1 × 10^14 atoms/cm² under the same rinse time. The EL-D238 formulation also differs from chromic acid or organic solvent developers because it is water-rinsable and does not introduce heavy-metal oxidants.

    On an automated puddle/spin track, EL-D238 is dispensed through a 0.05 µm polytetrafluoroethylene or high-density polypropylene point-of-use filter. A static puddle of 25–60 s at 21–23 °C is typical for 1.0–2.0 µm i-line positive resist, but thicker films require longer contact. End-point detection by optical reflectance or visual inspection is used to adjust time within the qualified window. Temperature excursions beyond ± 2 °C from the qualified set point should trigger requalification because dissolution rate shifts approximately 0.5–1.5 % per °C for novolak/diazonaphthoquinone systems.

    When Puddle Development Replaces Immersion in High-Density Resist Processing

    Immersion development in a temperature-controlled wet bench is replaced by puddle or spray methods when critical dimension uniformity below 0.05 µm (3σ) is required across a 200 mm or 300 mm substrate. In puddle mode, fresh EL-D238 is dispensed through a point-of-use filter at 1.0–2.0 L/min onto a wafer rotating at 50–200 rpm; rotation is then reduced or stopped to maintain a stable puddle. The main process conflict arises from dissolved resist loading. As exposed novolak/diazonaphthoquinone dissolves into the puddle, organic solids concentration can reach 5–15 g/L, which slows the development rate and can leave residue if the puddle remains beyond the qualified time. Each wafer therefore receives fresh developer rather than a recirculated bath.

    Spray development is preferred for features with aspect ratios above 3:1. A single-wafer spray chamber with nitrogen pressure of 2–4 bar and nozzle oscillation over 20–45 s residence time reduces scumming at the base of via or trench openings. Spray development produces alkaline aerosol; the exhaust system must be compatible with alkaline mist and the bowl must be rinsed to prevent salt accumulation. The developer should not be recirculated across wafers unless filtered through 0.02 µm media and monitored for pH drift greater than 0.1 pH from fresh material. In mixed-track systems, the developer bowl and drain lines must be segregated from acid waste streams to avoid exothermic neutralization and salt precipitation.

    In thick resist processing for electroplating bumps, the standard 2.38 wt% TMAH solution may be diluted gravimetrically with high-purity water to 1.19–1.50 wt% to reduce sidewall attack on positive molds. The final concentration must be confirmed by titration before use. Typical spray development of a 20–30 µm diazonaphthoquinone resist requires 60–120 s in multiple puddle cycles, with an ultrapure water rinse after each cycle. The reduced concentration increases selectivity to the unexposed surface but may lengthen the first clearing time by 30–50 %. For mold applications, nitrogen-blinkered holding tanks are preferred because carbon dioxide pickup in open tanks alters the available hydroxide concentration.

    Carbonate Absorption Remains the Principal Storage Risk

    Atmospheric carbon dioxide converts TMAH into tetramethylammonium carbonate. Carbonate can reduce development contrast and produce residues on aluminum bond pads and copper redistribution layers. Open baths should therefore be avoided. Bulk storage should be in closed, nitrogen-blanketed high-density polyethylene or fluoropolymer containers at 15–25 °C. Point-of-use delivery lines should be constructed from PFA or high-density polypropylene. Polyvinylidene fluoride may be acceptable only after alkaline chemical compatibility qualification because some grades degrade under long-term exposure to quaternary ammonium hydroxide solutions. Filters must be flushed with 10–20 L of developer before product diversion to the process stream. Recirculated developer should be monitored for conductivity and particle count per ISO 21501-1; a conductivity increase of more than 15 % from the qualified baseline indicates carbonate absorption or dilution and requires replacement.

    Shelf life from date of packaging is 12 months at 20 °C in unopened containers. Storage below 5 °C can cause tetramethylammonium carbonate precipitation, and storage above 35 °C can accelerate packaging additive leaching and raise nonvolatile residue. The product is not formulated as a bulk silicon etchant, even though higher-concentration TMAH is used for anisotropic silicon etching, and it is not a solvent developer for negative-tone epoxy resists such as SU-8. It should not be mixed with acid strippers or oxidizers because rapid neutralization and heat release can generate aerosol and damage wet-bench materials.

    For copper and gold bumping lines, residual cation control is verified by vapor phase decomposition inductively coupled plasma mass spectrometry on bare silicon monitors after developer and rinse. The combined sodium and potassium value after EL-D238 puddle development is below 1 × 10^10 atoms/cm² on clean substrates, whereas a conventional sodium hydroxide developer can leave 1 × 10^12–1 × 10^14 atoms/cm² under the same rinse time. This boundary is significant for devices with gate oxide thickness below 2 nm and for through-silicon via sidewalls where later plasma cleaning may not remove alkali metal salts from developed resist openings.

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