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Hollow Fiber and Flat Sheet Membrane Spinning System FAQ - 20 Questions
Hollow Fiber Spinneret FAQ - 50 Questions
37
hollow fiber spinneret adaptation for low-temperature vs. high temperature TIPS
● Low-T TIPS (120–160°C): 316 or standard Ni alloys suffice; no complex cooling needed; flow paths optimized to reduce diluent crystallization risk.

● High-T TIPS (200–250°C): Use high temperature alloys (Hastelloy, Ti) to avoid thermal deformation; integrate cooling channels (annular passages) to remove heat and prevent degradation; flow-paths designed to limit thermal aging.

● Practice note: SUS304 and SUS316 have been used long-term for 32-hole TIPS lines without quality issues.

● High-T outlet free span: Extend to 15–20 mm for melt relaxation and to mitigate die swell–induced wall jumps.

● Thermal control: Lower thermal conductivity requires multi-zone heaters to keep axial ΔT < 1.5°C.

38
Do thermal cycles (heat-up/cool-down rates) affect fit clearances?
● Example: 304 CTE ~17×10⁻⁶/°C; from 25→250°C, a φ10 mm inner core expands radially by ~0.038 mm. If outer ring is Inconel (13×10⁻⁶/°C), differential radial expansion ~0.011 mm, potentially narrowing the annular gap → thinner walls.

● Design allowance: Compute ΔD = ΔT × (α₁ − α₂) × D, and pre-clearance (e.g., ~0.02 mm) so that concentricity is optimal at operating temperature.

● Heat-up/cool-down rate: Recommend ≤30°C/h to keep thermal stresses <50 MPa and avoid micro-slip/scratching at seals.

● For same-material assemblies, effects are smaller.

39
Does disassembly frequency affect hollow fiber spinneret life? How does FCT Gen-5 help?
● Seal damage: Each disassembly risks scratching precision sealing faces.

● Needle damage: Traditional designs are hard to disassemble; bore needles are easily damaged and scrapped.

● Precision loss: Concentricity may shift after reassembly, requiring re-calibration.

● FCT Gen-5 advantage: Independent, pinless modular inserts enable quick change without damaging the body; reduces mechanical damage and precision drift, extending service life.

40
Impact of cleaning-media residue on subsequent membrane performance
● Residual cleaners/solvents can alter wall surface energy, causing wetting issues and pore-size drift; reduces permeability or causes local blockage. Rinse with process solvent (e.g., NMP for NIPS) until residue <0.1 mg/cm².

● Phase separation impact: Incompatible residual solvents (e.g., DMF) change coagulation rate—oversized pores or defective skin—lowering flux/selectivity.

● Material contamination: Residual corrosives (strong acids/bases) react with membrane (e.g., PA hydrolysis); metal fines can embed and reduce rejection.

● Biocompatibility: Medical membranes require very low residuals (e.g., ethanol ≤10 ppm) to avoid adverse reactions.

● Corrosion acceleration: Residual Cl⁻ (e.g., from HCl cleaning) induces pitting in stainless steel.

41
Trade-offs between universal vs. dedicated hollow fiber spinnerets for PVDF/PSf/PES/CTA/P
● Universal: Covers multiple materials (PVDF, PSf, PES), but may compromise on precision (orifice tolerance, finish).

● Dedicated: Tailored to a specific material—e.g., solvent-resistant coatings for PVDF; high-strength materials for PA; ceramic coatings for CTA; titanium for PA to prevent hydrolysis. Higher precision/stability but requires frequent changeover in multi-product plants.

● Recommendation: For high-volume, choose universal to reduce cost; for high-precision (e.g., hemodialysis), choose dedicated to ensure performance.

42
Sensitivity of hollow fiber spinnerets to soluble/insoluble additives
● Soluble additives (e.g., PEG, LiCl): Lower sensitivity, but >5% may raise viscosity and extrusion pressure; ensure complete dissolution to avoid local viscosity spikes.

● Rheology impact: Adjust temperature/pressure accordingly.

● Thermal sensitivity: Some additives decompose at high T, forming gels in dead zones—leading to clogs.

● Insoluble additives/nanofillers (TiO₂, CNTs, activated carbon):

● High sensitivity—primary risk is clogging. Particle size ≤1/5 of orifice (e.g., ≤20 μm for 0.1 mm rifice), with excellent dispersion (no agglomeration).

● Abrasion: Hard fillers wear orifices and capillaries, shifting critical dimensions.

● Agglomeration: Accumulates at contractions/orifices, causing blockages.

● Sedimentation: Dense fillers settle in low-shear dead zones.

43
Pressure rating and safety factor for hollow fiber spinnerets
● Base on material yield strength at operating temperature.

● Safety factor:

●  Industry practice: 3–4 for continuous precision chemical equipment.

●  Formula (simplified): Allowable working pressure ≈ yield strength / safety factor.

●  Example: 304 SS yield at temperature ~240 MPa; with SF = 4, allowable ≈ 60 MPa. Actual design set well below for safety margin.

44
Applicability of internal coatings/surface treatments (e.g., DLC, nitriding)
● DLC (diamond-like carbon): Very hard (HV ≥ 2000), hydrophobic, wear-resistant; good for high viscosity dopes (e.g., PVDF melt) or hang-up-prone systems. Limitations: Poor resistance to strong acids/bases; thickness must be 0.5–2 μm—too thick risks spallation and contamination.

● Nitriding (e.g., ion nitriding): Raises surface hardness (HV ≥ 1000) and corrosion resistance; suitable for high temperature TIPS and chlorinated media; good for PSf/PES dopes. Less resistant to fluorinated solvents; hydrophobicity moderate; hang-up reduction less than DLC; may slightly increase roughness.

● General principle: For strong solvents (e.g., DMF), prefer DLC; for high temperature/pressure, prefer nitriding. Always test coating compatibility to avoid chemical failure.

● Material-first: Prefer SUS304/316L; only consider coatings for extreme conditions (high solids/high wear) after long-term validation.

45
Is lower internal surface roughness always better?
● Benefits: Lower roughness reduces friction, residue, and clogging; Ra ≤ 0.8 μm improves diameter uniformity and surface quality—especially for high-precision spinning.

● Not strictly “the lower the better”:

● Diminishing returns below Ra ~0.4 μm with sharply rising cost.

● Exceptions: Ultra-smooth walls can alter wall slip of highly elastic melts; high-solids (>30%) systems may show slip–stick pulsation. Some systems exhibit an optimal roughness window.

● Over-polishing can reduce beneficial lubricating films; in viscose-like charged colloids, adsorption can worsen spinnability.

46
Effect of surface roughness (Ra/Rz) on fouling and hang-up
● Fouling risk: Higher roughness (Ra > 1.6 μm) promotes contaminant adhesion and orifice clogging.

● Hang-up: Rough surfaces increase friction, leaving residual dope that forms gels and contaminates subsequent runs.

● Optimization: Aim for low roughness (Ra ≤ 0.8 μm) via polishing to reduce fouling and hang-up.

47
Effects of scratches/indentations on sealing faces—leakage and eccentricity
● Leakage: Scratches/indentations disrupt flatness and sealing lines; under pressure, dope leaks preferentially at defects.

● Eccentricity: Damage can induce uneven clamping loads, generating small bending moments that distort internal flow alignment and cause eccentric fibers.

48
Do replacement or worn hollow fiber spinnerets affect membrane quality and batch-to-batch repeatability?
● New vs. old: Micron-level orifice differences (±2 μm) shift outer diameter/wall thickness, altering MWCO and flux.

● Wear effects: Orifice enlargement, edge rounding, microcracks cause:

● Higher flow → thinner walls.

● Lower shear → looser skin.

● Higher eccentricity → lower strength.

● Batch variability: Even identical drawings yield micro-variance in orifice/gap, concentricity, and finish—changing spinning dynamics and membrane performance (flux, rejection, strength).

● Quality management: Treat hollow fiber spinnerets as critical assets; log use history against product performance; scrap/refurbish when beyond tolerance.

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