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Leading Hollow Fiber Membrane Spinning Machine and Spinneret Manufacturer - Trustech

What are the Features and Size Selection of Dual Layer Liquid Spinning Heads?

In NIPS and TIPS ultrafiltration hollow fiber manufacturing, “dual-layer liquid spinning heads” correspond to dual-layer dope spinneret plates. These tools co-extrude two dopes with one bore fluid through concentric, independently metered channels to build composite wall structures (e.g., dense outer skin + porous inner support). Getting features and size selection right determines lumen stability, inter-layer adhesion, OD/ID control, and final pore architecture.

hollow spinneret


Features of Dual Layer Liquid Spinning Heads

  • Three independent channels
    Two dope circuits and one bore circuit remain hydraulically isolated until the outlet, enabling simultaneous co-extrusion. This supports bilayer walls with tailored selectivity and support strength.
  • Precise layer-ratio control
    Each stream is independently metered. Layer thickness ratios are set by calibrated flow rates and maintained via resistance-matched channels and stable temperature control.
  • Synchronized forming at the orifice
    The two dopes converge concentrically around the bore stream at the outlet land. Properly designed tapers and land L/D prevent delamination and ensure continuous, bonded interfaces.
  • Orifice matching logic
    Orifice and annular gaps are sized to the rheology of each dope. Typically, the outer-layer annulus is slightly larger to accommodate higher apparent viscosity or to bias skin formation. Alternative stacks (e.g., one dope + two bore streams) are feasible with the same design logic.
spinning spinneret


Material Composition of Dual Layer Spinning Heads

  • Base materials and coatings
    Spinneret plates and cores use corrosion- and heat-resistant alloys with low-roughness flow paths. Optional surface treatments reduce fouling and shear hotspots, protecting delicate bilayer interfaces.
  • Dimensional stability
    Thermal stability under NIPS/TIPS setpoints prevents drift in annular gaps, land L/D, and concentricity—essential for stable OD/ID and consistent inter-layer bonding.


Design Aspects of Dual Layer Liquid Spinning Heads

  • Distribution and pre-compression
    Balanced manifolds feed each dope circuit with equal hydraulic resistance per hole. Streamlined contractions deliver uniform velocity profiles into the annular land, suppressing vortices and dead zones.
  • Outlet land and shear profile
    Land geometry (gap and L/D) is tuned to flatten shear, minimize Barus swell, and align molecular orientation. Micro-chamfers at the outlet mitigate edge instabilities and surface defects.
  • Concentricity and tolerances
    Maintain tight circumferential gap tolerances to avoid eccentric walls and variable layer thickness around the fiber, which can trigger asymmetric phase inversion.


What are the Features and Size Selection of Dual Layer Liquid Spinning Heads? - Design Aspects of Dual Layer Liquid Spinning Heads


FeatureDescriptionTypical Size GuidanceApplication Notes
Dual-layer channelsTwo dopes + one bore, isolated to the outletOuter annulus gap > inner annulus gap for higher-viscosity skin dopesEnables dense-skin + porous-support structures
Customizable nozzle/landTunable annular gaps and L/DLand L/D selected per rheology to flatten shearReduces swell and stabilizes lumen
Temperature controlIsothermal face and circuit heatingTight control near outlet regionPrevents premature skinning (NIPS) or unintended solidification (TIPS)
Multiple feed portsIndependent metering for each streamCalibrated ΔP–Q per circuitMaintains layer thickness ratios
Automation/monitoringInline ΔP, flow, temp feedbackReal-time ratio hold and drift correctionGuards against viscosity and temperature drift


Size Selection Criteria for Dual Layer Liquid Spinning Heads

  • Match to rheology and throughput
    Higher-viscosity dopes or higher line throughput require wider channels and/or longer pre-compression to maintain uniform velocity without excessive ΔP.
  • Channel thickness and length
    Select annular gaps and land L/D to achieve a uniform shear profile for each dope. Too short amplifies entrance effects; too long increases pressure drop and heat load.
  • Orifice hierarchy
    For most dual-layer, set the outer layer annulus 0.15–0.5 mm larger than the inner layer annulus when outer-viscosity is higher, adjusting per measured rheology and target draw.
  • Equipment compatibility
    Ensure manifold spacing, face dimensions, and core mount geometry align with existing holders, heaters, air-gap or quench layout, and cleaning fixtures.


Impact of Size on Performance in Spinning Applications

  • OD/ID and wall symmetry
    Proper annulus sizing and concentricity stabilize lumen, reduce OD/ID drift, and prevent circumferential thickness bias across holes.
  • Inter-layer bonding and morphology
    Correct land and taper dimensions synchronize layer arrival at the outlet, promoting cohesive bilayer formation and predictable NIPS/TIPS phase inversion.
  • Throughput vs. stability
    Larger gaps support higher flow but can reduce shear control; smaller gaps improve shear control but raise ΔP and fouling risk. Choose a balanced window validated by rheology and bench ΔP–Q tests.


Common Applications of Dual Layer Liquid Spinning Heads

  • UF fibers with engineered skins
    Dense outer selective layers with porous inner supports for low transmembrane pressure and target cut-offs.
  • Functional gradients
    Tailored inner-layer porosity for lumen-side filtration or reinforced support; alternative stacks for specialized phase-inversion paths.


Maintenance and Care for Optimal Performance

  • Fine filtration
    Filter both dopes and bore streams upstream of the spinneret to prevent partial blockages and inter-layer defects.
  • Gentle cleaning and reassembly
    Non-abrasive cleaning, burr-free handling, and torque-controlled reassembly preserve tolerances and surface finish.
  • Calibration and monitoring
    Routine verification of flow meters, ΔP sensors, and thermal controls maintains layer ratios and stable forming.


FAQ

1
How do I choose annular gaps for two dopes with very different viscosities?
Widen and, if needed, shorten the higher-viscosity channel; select a land L/D that flattens shear without excessive ΔP, then verify with bench ΔP–Q and short spinning trials.
2
How can I keep layer thickness ratios stable during viscosity drift?
Independently meter each stream and close the loop with inline flow and ΔP feedback; adjust pump speeds or control valves to re-lock ratios in real time.
3
What outlet features help avoid delamination?
Streamlined pre-compression, matched arrival timing into the land, appropriate land L/D, and micro-chamfers at the exit to minimize edge instabilities.
4
Does NIPS vs. TIPS change size selection?
Yes. NIPS favors tight thermal uniformity and air-gap/bath control to prevent premature skinning; TIPS requires thermal management to avoid early solidification—both influence land L/D and taper sizing.
5
How do I detect resistance mismatch between the two dopes?
Watch for circumferential layer-thickness asymmetry, OD/ID drift, and rising wall RSD. Inline ΔP divergence between circuits and per-hole flow imbalance are early indicators.
6
Can I use two bore streams with one dope?
Yes. The same independent-channel logic applies; ensure concentricity and resistance matching so both bore flows stabilize the lumen and desired internal interface.

Conclusion

Dual-layer spinneret plates for NIPS/TIPS UF fibers rely on three independent, precisely matched channels to co-extrude bilayer walls around a stable lumen. Correct feature design—balanced manifolds, tuned annular gaps, optimized land L/D, and isothermal control—enables synchronized forming and robust inter-layer adhesion. Size selection hinges on dope rheology, throughput, and equipment integration, validated by rheology, ΔP–Q testing, and short-run spinning. With disciplined maintenance and closed-loop metering, dual-layer heads deliver uniform OD/ID, consistent morphology, and reproducible ultrafiltration performance.

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