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Online proceedings - EDA Publishing Association

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11-13 <br />

May 2011, Aix-en-Provence, France<br />

<br />

**<br />

⎡ − εε ⎤<br />

mp<br />

f = ⎢ ⎥<br />

(2)<br />

CM<br />

**<br />

⎢⎣<br />

+ 2εε<br />

mp<br />

⎥⎦<br />

*<br />

*<br />

where ε and<br />

p<br />

ε are the complex permittivity of the<br />

m<br />

particle and the medium, respectively. The complex<br />

permittivity is related to the conductivity σ and angular<br />

frequency ω, which relates to ω = 2πf<br />

, through the<br />

formula:<br />

σ<br />

* εε j−≡<br />

ω<br />

(3)<br />

where j equals − 1 . Therefore, the DEP force is<br />

dependent mainly on difference between the dielectric<br />

properties of particles and the suspending medium solution.<br />

It can be either a positive DEP, which pulls the particle<br />

toward the location of the high-electric field gradient, or a<br />

negative DEP, that repels the particle away from the region<br />

of high-electric-field gradient.<br />

The schematic diagram of the cDEP microfluidic chip is<br />

depicted in Fig. 1. Four insulating structures which formed<br />

an X-pattern in the microchannel, as shown, were employed<br />

to squeeze the electric field in a conducting solution, thereby<br />

generating the regions high-electric-field gradient. The inlet<br />

flow field and the electric field were applied vertically. The<br />

negative-dielectrophoretic particles were repelled from the<br />

high- electric-field region, moving to the center of the<br />

microchannel where the flow velocity was higher. The<br />

insulator was designed 60 μm in width and 200 μm in length.<br />

The distance of the insulators along the direction of flow, as<br />

well as along the direction of the electric field, was 120 μm.<br />

The inclined angle of the insulator was 45 degrees. The<br />

particles were introduced into the microchannel and<br />

pre-confined hydrodynamically by the funnel-shaped<br />

insulating structures close to the inlet. The particles with a<br />

negative dielectrophoretic response were repelled toward the<br />

center of the constricting region. The electric field in the<br />

main microchannel was generated by using electrodes<br />

inserted into two conductive micro-reservoirs, which were<br />

separated from the main microchannel by thin insulating<br />

barriers made of 20 μm-width of PDMS [7].<br />

III.<br />

EXPERIMENTAL SECTION<br />

A. Chip Fabrication<br />

A biocompatible material of polydimethylsiloxane<br />

(PDMS) was adopted for cDEP microfluidic chip. The mold<br />

master was fabricated by using the inductively coupled<br />

plasma (ICP) dry etching technique on the silicon wafer<br />

(around 100 μm in height) to define the micropatterns, as<br />

showed in Fig. 2a. The PDMS prepolymer mixture was<br />

poured and cured on the mold master to replicate the<br />

structures (Fig. 2b). After the PDMS replica had been peeled<br />

off, the replica was bonded with the glass substrate after<br />

treatment of the oxygen plasma in the O 2 plasma cleaner<br />

(Model PDC-32G, Harrick Plasma Corp. Ithaca, NY, USA).<br />

The image of the fabricated microchip for particle focusing<br />

taken by the optical microscope was revealed in Fig. 2c.<br />

B. Apparatus and Materials<br />

A function/arbitrary waveform generator (Agilent<br />

33220A, Agilent Technology, Palo Alto, CA, USA) was<br />

employed as the AC signal source and connected to an RF<br />

amplifier (HSA-4011, NF corporation, Japan) to apply<br />

electric fields required for dielectrophoretic manipulation in<br />

the microchannel. Polystyrene particles, 10 mm in diameter,<br />

(G1000, Thermo Scientific Inc., USA) were used to<br />

investigate the efficiency of focusing. A sample of<br />

polystyrene particles with a concentration of 10 6<br />

particles/mL was injected using a syringe pump (Model KDS<br />

101, KD Scientific Inc., Holliston, MA, USA). The<br />

dielectric permittivity and conductivity of polystyrene<br />

particles at the frequency of 1 MHz are about ε r =2.6; σ=10 -16<br />

S/m, respectively [9]. The particles are suspended in a<br />

sucrose solution with an 8.62 wt% and 2.74×10 -2 wt% of<br />

K 2 HPO 4 (ε r =78; σ=4.50×10 -2 S/m). The dielectrophoretic<br />

focusing of particles was observed and recorded by an<br />

inverted fluorescence microscope (model CKX41, Olympus,<br />

Tokyo, Japan) mounting a CCD camera (DP71, Olympus,<br />

Tokyo, Japan) and a computer with Olympus DP controller<br />

image software.<br />

IV. RESULTS AND DISCUSSION<br />

To investigate the capacitive behavior of the PDMS barrier,<br />

the Wayne Kerr precision impedance analyzer 6420 was<br />

used to measure the impedance of the PDMS in DMEM<br />

medium (Gibco, Grand Island, NY, USA), which was<br />

commonly used in cell culture. The micro-reservoirs were<br />

filled with DMEM medium with an electric conductivity of<br />

0.8 S/m; besides, this medium in light red color could be used<br />

for confirm that there was no leakage from insulating barriers.<br />

The experimental set up was depicted in Fig. 3. The<br />

measured impedance of the PDMS barrier under different<br />

frequencies and the fitting curve to experimental data using<br />

the least-squares method were depicted in Fig. 4. The results<br />

revealed the capacitive behavior of the PDMS barrier. The<br />

impedance decreased with the frequency. The relative<br />

dielectric permittivity and conductivity of PDMS at a<br />

frequency of 1 MHz were 10.46 and 7.6×10 -4 S/m,<br />

respectively. The numerical simulations of the electric and<br />

flow fields, as well as the particle trajectory, were performed<br />

using the commercial software CFDRC-ACE + (ESI Group,<br />

France). Fig. 5 showed the transient simulation of the tracks<br />

of latex particles (ε r =2.6; σ=10 -16 S/m) [9] under varying<br />

electric field strengths and inlet velocity. The increase in the<br />

applied electric field significantly enhances the performance<br />

of focusing. Furthermore, decreasing inlet velocity increases<br />

the efficiency of focusing because the higher velocity results<br />

in more lateral expansion. Experimental results of focusing<br />

of fluorescent latex particles at different inlet flow rates and<br />

under varying electric field strengths of a frequency of 1<br />

MHz were demonstrated the performance of focusing, as<br />

showed in Fig. 6. The latex particles of 10 μm in diameter<br />

suspended in the sucrose medium with 8.62 wt% and<br />

2.74×10 -2 wt% of K 2 HPO 4 (ε r =78; σ=4.50×10 -2 S/m) were<br />

used to investigate the efficiency of focusing. The sample of<br />

latex particles was injected using a syringe pump. The<br />

experimental results showed that the performance of<br />

363

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