[Marangoni 재분포 및 비젖음 위험(Dewetting Risk) 한국어 해석 (Korean Engineering Conclusion)]
⚠️ Scientific Model & Engineering Limitation:
Marangoni-induced dewetting is represented as a reduced-order stability screening model.
Actual dewetting depends on wettability, contact angle, surface condition, chemical composition,
film thickness, evaporation, temperature, surface-tension gradients and transient flow.
🎯Nozzle Position Optimizer (V13.3-5)
Engineering Screening | Lightweight Reduced-Order Sweep
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🗺️ Candidate Position Score Map & Top Ranking ComparisonCandidates evaluated: 0
[Top 5 Candidate Position Sweep Results Table]
Rank
X (mm)
Y (mm)
Uniformity (%)
Thickness Range (µm)
Dewetting Risk
Score
Action
Press "Run Nozzle Sweep" to evaluate candidate nozzle positions.
[노즐 위치 최적화 결과 및 공정 제언 (Korean Optimization Conclusion)]
탐색 버튼을 클릭하여 선택한 노즐 위치 범위에 대한 최적 배치 및 액막 품질 평가를 수행하십시오.
⚠️ Model Limitation:
Optimization is based on the current reduced-order model and should be interpreted as engineering screening.
💧Nozzle Flow Balance Optimizer (V13.3-6)
Flow Ratio Distribution Sweep | Constant Total Flow
📊 Flow Rate Ratio vs. Film Uniformity & Optimization Score ChartDistributions tested: 0
[Top Candidate Flow Distribution Results Table]
Rank
Flow Rates (mL/min)
Flow Ratio (%)
Uniformity (%)
Thickness Range (µm)
Dewetting Risk
Score
Action
Press "Run Flow Ratio Sweep" to evaluate candidate flow distributions.
[노즐 유량 분배 최적화 결과 및 공정 제언 (Korean Flow Optimization Conclusion)]
탐색 버튼을 클릭하여 총 유량 조건에 대한 노즐 간 최적 유량 분배 비율을 평가하십시오.
⚠️ Model Limitation:
Flow distribution optimization is based on the current reduced-order film thickness and Marangoni stability screening model.
🔬 SCIENTIFIC MODEL & ENGINEERING LIMITATIONS (CLICK TO TOGGLE)
⚠️ Model Scope & Limitations
• Reduced-Order Model: Uses 2D depth-integrated lubrication approximation (LUB-2D).
• Not 3D CFD / VOF: Does not resolve 3D navier-stokes or explicit phase-volume tracking.
• Representative Properties: Chemical physical constants are reference baseline values.
• Reaction Kinetics: Multi-chemical reaction enthalpy or complex phase changes are not explicitly modeled.
• Equipment Calibration: Actual chamber matching requires empirical process calibration constants.
① Continuous Spin Film Equation
h(r) = [ 3μQ / (2πρω²) ]1/3 · r-2/3
Balance between centrifugal force and viscous shear stress in steady-state spin coating (Emslie, Bonner, Peck 1958).
② Viscosity Temperature Dependency
μ(T) = μ25 · exp( -B · (T - 25) )
Andrade viscosity fitting model for thermal processing effects.