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Title: Final report


1
Final report
  • Department Institute of NEMS
  • Student ID?d9635808
  • Report? Yen - Liang Lin

2
Outline
  • Introduction
  • Design and Fabrication
  • Experimental setup
  • Results and discussion
  • Conclusion
  • Reference

3
Introduction T-junction
The resulting instability that drives droplet
formation is a well-known competition between
surface tension and shear forces
  • Effect of Flow Speed on Droplet Size
  • Effect of Channel Size on Droplet Size
  • Effect of Surfactant on the Stability of Droplets

T. Thorsen et al., Physical Review Letters, 2001.
T. Nisisako et al., Lab. Chip, 2002.
4
Introduction Flow focusing
  • Generation rate104/s for water-in-oil droplets
    and reaching 103/s for oil-in-water droplets
  • The orifice with its cusp-like edge exerts a ring
    of maximized stress around the flow and ensures
    controlled breakup of droplets for a wide range
    of flow rates
  • Focusing the flow into a 3-D profile.
  • Janus particles ?both electrical and color
    anisotropy, for use in electronic paper.
  • To produce bicolored particles, pigments of
    carbon black and titanium oxide are dispersed in
    an acrylic monomer (isobornyl acrylate, IBA)

T. Nisisako et al., Adv. Mater., 2006.
L. Yobas et al., Lab. Chip, 2006.
5
Introduction Solidifying Choppers
  • Solidifying these drops in situ either by
    polymerizing a liquid monomer or by lowering the
    temperature of a liquid that sets thermally.
  • A range of materials can be applied, including
    heterogeneous multiphase liquids and suspensions.
  • A novel combination of hydrodynamic-focusing and
    liquid-chopping techniques.
  • The size of the droplets is tunable using three
    approaches including adjusting the relative
    sheath/sample flow velocity ratios, the applied
    air pressure and the applied chopping frequency.

S. Xu et al., Angew. Chem. Int. Ed., 2005.
G. B. Lee et al., JMEMS, 2006.
6
Design
1. Two immiscible liquids, including a continuous
phase (sample A) with a velocity of V1 and
dispersed phase (sample B) with a velocity of V2
were injected into the T-junction channels to
generate the internal emulsion droplets. 2. The
internal emulsion droplets were hydrodynamically
focused into a narrow stream by the neighboring
sheath flows (Sample C) with a velocity of V3.
3. The pneumatic choppers were used to cut the
pre-focused emulsion flow into double emulsion
microdroplets with well-controlled sizes.
7
Fabrication
  • SU8 master mold
  • Replication process of the PDMS structure

8
Experimental setup
9
Results and discussion
  • The deformation of controllable moving-wall
    structure squeezes the continuous phase flow
    locally and increase the continuous phase flow
    velocity near the intersection of the T-junction
    channels. It therefore increases the shear force
    to form droplets with smaller diameters.
  • The coefficients of variation are 1.28, 2.78,
    1.61, and 3.53

10
Results and discussion
  • V1V2V3 1602000
  • The external droplets size of double emulsion ?
    the applied pressure of pneumatic chopper.
  • The internal droplets size of double emulsion ?
    the applied pressure of controllable moving-wall.

11
Conclusion
  • A new microfluidic chip capable of generating
    uniform double emulsion microdroplets utilizing
    the combination of a controllable moving-wall
    structure at the T-junction microchannels and
    pneumatic choppers was demonstrated.
  • The controllable moving-wall can actively tune
    the size of the emulsion droplets without
    changing the syringe pumps flow rate.
  • The deformation of the controllable moving-wall
    structure can physically change width of the
    microchannel. Therefore the flow velocity can be
    locally changed by applying compressed air
    pressure.
  • The size of the external droplets can be
    fine-tuned by different applied air pressure of
    pneumatic choppers.
  • The developed chip has the potential to be used
    for high-quality emulsification processes,
    including the analysis of pico-liter biochemical
    reactions, drug delivery systems, and cosmetic
    industry.

12
Reference
  • T. Thorsen, R. W. Roberts, F. H. Arnold and S. R.
    Quake, Dynamic pattern formation in a
    vesicle-generating microfluidic device, Physical
    Review Letters, vol. 86, pp. 4163-4166, 2001.
  • T. Nisisako, T. Torii, T. Takahashi, and Y.
    Takizawa, Synthesis of monodisperse bicolored
    janus particles with electrical anisotropy using
    a microfluidic co-flow system, Adv. Mater., vol.
    18, pp. 1152-1156, 2006.
  • T. Nisisako, T. Torii, and T. Higuchi, Droplet
    formation in a microchannel network, Lab. Chip,
    vol. 2, pp. 24-26, 2002.
  • L. Yobas, S. Martens, W. L. Ong, and N.
    Ranganathan, High-performance flow-focusing
    geometry for spontaneous generation of
    monodispersed droplets, Lab. Chip, vol. 6, pp.
    1073-1079, 2006.
  • S. Xu, Z. Nie, M. Seo, P. Lewis, E. Kumacheva, H.
    A. Stone, P. Garstecki, D. B. Weibel, I. Gitlin,
    and G. M. Whitesides, Generation of monodisperse
    particles by using microfluidics control over
    size, shape, and composition, Angew. Chem. Int.
    Ed., vol. 44, pp. 724-728, 2005.
  • C. T. Chen, and G. B. Lee, Formation of
    micro-droplets in liquids utilizing active
    pneumatic choppers on a microfluidic chip,
    Journal of Microelectromechanical System, vol.
    15, pp. 1492-1498, 2006.

13
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