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Leading Hollow Fiber Membrane Spinning Machine and Spinneret Manufacturer - Trustech

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Hollow Fiber and Flat Sheet Membrane Spinning System FAQ - 20 Questions
Hollow Fiber Spinneret FAQ - 50 Questions
1
Designing outlet shear-rate distribution for optimum performance
● Uniform molecular/micellar orientation: Promotes consistent pre-orientation and membrane formation.

● Control extrudate swell (Barus effect): Nonuniform shear causes twist/size instability.

● Adequate L/D: For annular slits, ensure sufficient land length; commonly L/D > 10.

● Pre-compression transition: Use gradual conical convergence into the annular gap to equalize inflow.

● CFD-guided optimization: Iterate geometry until a flat shear-rate profile at the outlet is achieved.

● Converging outlet: Conical/parabolic convergence (5°–15°) to avoid shear shocks.

● Concentric ring-gap uniformity: For bilayer dies, ring-gap tolerance ≤±2 μm around the circumference.

● Edge treatment: Micro-chamfer/radius to reduce edge-induced “sharkskin” instabilities.

● Match to rheology: Highly elastic dopes may need lower shear—use larger orifices or shorter capillaries.

2
How to reduce dead zones and hold-up in distribution manifolds
● Streamline geometry: Large fillets; eliminate sharp corners.

● Avoid section jumps: Use gradual area transitions.

● FIFO principle: Promote forward flow with no recirculation.

● Tapered or coat-hanger manifolds: Ensure uniform widthwise pressure and smooth flow with minimal dead zones.

● Surface finish: Electro/mirror polish to Ra <0.8 μm to reduce adhesion.

● Match flow and volume: Avoid oversized manifolds at low flow; ensure sufficient shear to sweep surfaces.

● Minimize cavity volume: Reduce hold-up to shorten cleaning time.

● Tilt/vent: Prevent air-pocket dead zones with angled install or vents.

● Maintain velocity: Target ≥0.5 m/s via pressure increase or area reduction to prevent stagnation.

3
Diagnosing the impact of bore-fluid composition fluctuations
● Periodic eccentricity or “bamboo nodes”: Bore pump pulsation (e.g., plunger pumps) causes periodic flow changes.

● Unstable lumen size: Bore flow variations directly alter inner diameter.

● Worsening eccentricity: Changes in bore viscosity/density disrupt interfacial tension balance.

● Visual cues: Variable lumen size, pinholes, frequent breaks; too much non-solvent in bore accelerates coagulation; too little delays it.

● Key analytics: Chromatography to quantify solvent/non-solvent ratio (±5% spec); monitor bore viscosity (≤3% variation).

● Process isolation: Hold shell parameters constant, normalize bore composition; if stability returns, root cause confirmed.

● Axial heterogeneity: Pore size/porosity vary along fiber when bore composition swings.

● Event correlation: Match instability to bore system events (tank changeovers, charging).

● Online monitoring: Install inline viscometer/densitometer if feasible.

● Exclusion test: Run with known-good bore while holding others constant to isolate cause.

● Pump health: Check pulsation, seals, trapped air.

4
How external coagulation (non-solvent bath) influences outlet design
● Air-gap length: Strong non-solvents (water) need longer dry zones (5–30 cm); add guides to reduce flutter. Weaker non-solvents allow shorter air gaps; outlet can approach the bath.

● Outlet chamfer: Micro-chamfer (0.1–0.3 mm) or parabolic transition to prevent edge hang-up or tearing.

● Anti-disturbance geometry: Avoid abrupt steps near outlet to reduce bath backflow impact.

● Hole spacing: Increase inter-hole pitch or add shields to avoid sticking at high coagulation rates.

● Corrosion resistance: If bath contains acids/bases (e.g., regenerated cellulose), upgrade outlet materials.

● Wet spinning variants: For rapid coagulation, use minimal or no air gap (in-bath immersion), requiring robust immersion sealing.

● Streamlined outlet profile: Conical/streamlined exterior to reduce turbulence-induced vibration/stretching pre-bath.

● Bath flow direction: Layout multi-orifices with bath flow to avoid upstream boundary-layer effects on downstream holes.

5
How to evaluate and control flow-resistance matching between inner and outer channels
● Theory: Use Hagen–Poiseuille-based calculations with viscosity, flow setpoints, and geometry (length, hydraulic diameter) to estimate pressure drops. Target ΔP ratio ~1:1 ±10%.

● CFD: Simulate velocity/pressure fields and interface behavior to guide design.

● Design compensation: For large viscosity contrasts, shorten/widen high-μ paths to balance resistance.

● Flow-path shape: Use gradually converging or constant-area channels; avoid sudden expansions/contractions.

● Process tuning: Independently adjust metering-pump speeds/pressures to balance ΔP and achieve desired structure.

● Viscosity monitoring: Measure μ (e.g., rotational viscometer) and adjust pumps/valves as μ drifts to maintain balance.

6
How is a hollow fiber spinneret sealed?
● Face seals (most common):

● Lapped metal-to-metal faces clamped by bolts provide primary sealing.

● Add gaskets: Soft metal (copper, soft iron) or high-performance polymers (PTFE, PEEK). Under preload, gaskets plastically conform to micro-roughness.

● Radial seals (O-rings): For secondary joints or quick-disassembly, use chemical/heat-resistant O-rings (FKM/FFKM).

7
Dual-layer dope hollow fiber spinnerets—features and sizing
● Dual, independent flow paths: Two isolated channels co-extrude distinct dopes to form a bilayer (e.g., dense skin + porous support).

● Precise ratio control: Adjustable layer ratio (commonly 1:1 to 1:3) via independent valves/pumps.

● Synchronous formation: Both layers meet and wrap the bore fluid at the outlet to avoid delamination.

● Orifice matching: Outer-ring orifice I.D. 0.05–0.10 mm larger than the inner ring, tuned to layer viscosities (higher μ → slightly larger orifice).

● Channel width: Select per flow (e.g., 2–3 mm for higher flows) to limit pressure drop.

● Overall length: Fit equipment (typ. 50–100 mm); die-to-bath distance 5–10 mm to ensure proper bilayer merging.

8
How to choose hollow fiber spinnerets for hemodialysis membranes
● Extreme precision: Orifice diameter tolerance ≤±0.0003 mm; concentricity ≤0.003 mm to ensure tight pore-size uniformity (10–100 nm) and stable clearance performance.

● Biocompatible materials: Medical-grade stainless or titanium; surface Ra ≤0.5 μm; no metal ion leaching; compliant with ISO 10993.

● Structural reliability: Independent insert designs (e.g., Trustech FCT Gen-5) allow single-orifice replacement without full shutdown; dead-zone-free flow paths reduce residual contamination.

● Low-shear channels: Minimize protein adsorption/denaturation.

9
How to choose a braided-tube coating hollow fiber spinneret
● Guide-tube sizing: The braid passes through a central guide; polymer dope exits an annular slit and coats the braid. Guide I.D. slightly larger than braid O.D.

● Key parameter—die gap: The annular gap determines coating thickness; size/adjust per dope viscosity and desired thickness.

● Flow-path design: Ensure circumferentially uniform pressure to achieve thickness uniformity and avoid eccentric coating.

10
How to choose hollow fiber spinnerets for gas separation membranes
● Ultra-high concentricity and micro-precision: Wall-thickness deviation ≤±2 μm; prevent pinhole defects.

● Dead-zone-free flow paths: Avoid polymer degradation hot spots.

● High viscosity compatibility: Common polymers include PI and PSf; require large channels and strong pressure capability.

● Dry–wet compatibility: Often requires longer air gaps (5–20 cm) to form a dense skin.

● High temperature materials: PI spinning may require >200°C.

11
How does the hollow fiber membrane spinneret affect spinning quality?
● Precision → uniformity: Orifice tolerance and concentricity directly determine diameter variation and eccentricity; high precision can keep fiber diameter variation ≤5%.

● Flow-path structure → formation: Manifold/equalization design governs dope distribution, avoiding “streaky” multi-orifice output.

● Material → stability: Insufficient wear resistance enlarges orifices; poor chemical compatibility causes corrosion—both degrade quality over time.

● Sealing and flow resistance → continuity: Leaks and unequal resistance cause breaks or lumen closure, reducing yield.

● Film-formation dynamics: At the outlet (NIPS/TIPS), extrudate swell and initial bore/shell interface set the stage for phase separation, impacting pore size, distribution, and porosity.

12
Common materials for hollow fiber spinnerets
● Base: 304/316 stainless steels for NIPS at moderate temperatures; resistant to common solvents (ethanol, water).

● high temperature: Nickel alloys, titanium alloys, SUS630 (17-4PH) for TIPS (100–260°C), with higher hot strength and wear resistance.

● Corrosion-resistant: Hastelloy and ceramic-coated materials for aggressive solvents (DMF, DMSO) and strong acids/bases.

● Auxiliary coatings: PTFE or polysiloxane coatings on orifice walls to increase hydrophobicity and reduce deposition.

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