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Fluid Resistance: Micro-channels of the Valve Design

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Presentation on theme: "Fluid Resistance: Micro-channels of the Valve Design"— Presentation transcript:

1 Fluid Resistance: Micro-channels of the Valve Design
Bryan Sadowski Kunal Thaker

2 Outline Description of our current Micro-channel Layout in the Valve Design. Basics of fluid flow in Micro-channels. Calculations of pressure, velocity, flow rate, and resistance for our current design. Effects of the valve on the fluid flow and pressure gradients.

3 Current Micro-channel Design
Dimensions (Rectangular Cross Section) Width: 500 μm Height: ~100 μm Height: ~100 μm Width: 500 μm

4 Fluid Path Down: ~10.4 mm Across: 25.6 mm Up: ~0.2 mm Across: 13.1 mm Up: 10.2 mm Assumed: Pyrex is 10mm wide. PDMS Thin Flex Layer is 50 microns. All other Layers: 100 microns.

5 Basics of Fluid Flow Q= Flow Rate= A*(vbar) A= Cross sectional Area
vbar= Average velocity of the fluid Bernoulli’s Equation (zero viscosity fluids) P1+ (1/2)pv12 + pgy1= P2+ (1/2)pv22 + pgy2 P= Pressure p= Density of Fluid v= Average velocity of the fluid g= gravity Fluid Flow 1 2

6 Basics of Fluid Flow Fluidic Resistance = R= ΔP/Q [(N*s)/m5]
R(circular cross section)= 8μL/(πr4) μ= Fluid Viscosity= 0.01 g/sec*cm L= Length of channel r= Radius of channel R(Rectangular cross section)~ 12μL/(wh3) w= Width of the channel h= Height of the Channel

7 Basics of Fluid Flow Reynolds number= Re= (pvDh)/μ
Dh(Circle)=Diameter Dh(Rectangle)=2wh/(w+h) p(Water)= density=1 g/cm3 Assumed Fluid Flow Rate based on Fluid velocity Based on literature search 1500 cm/minute= 2.5 E5 μm/sec 1.25 E 10 μm3/sec= cm3/sec=12.5uL/sec 1 Torr= Pa

8 Calculations Fluid Down the Reservoir (D=0.4 cm, A=0.126 cm2)
Length= 1.04 cm v~0.1 cm/sec R= g/sec*cm4 Re= 4 ΔP= g/cm*sec2= Pa Fluid Across the Bottom Fluid Layer w= 500 μm, h ~100 μm, A= 5.0 e-4 cm2 Length~2.56 cm v= 25 cm/sec R=6.144 E 6 g/sec*cm4 Re= 41.7 ΔP= g/cm*sec2=7680 Pa

9 Calculations Fluid up the Interconnect
w= 1000 μm, h= 1000 μm, A= 0.01 cm2 Length= 200 μm v= 1.25 cm/sec R= 24 g/sec*cm4 Re= 12.5 ΔP= 3 g/cm*sec2=0.3 Pa Fluid Across the Top Fluid Layer w= 500 μm, h ~100 μm, A= 5.0 e-4 cm2 Length~ 13.0 mm v= 25 cm/sec R= 3.12 E7 g/sec*cm4 Re= 41.7 ΔP= g/cm*sec2=3900 Pa

10 Calculations Fluid Through the Valve Opening
w= 500 μm, h ~20 μm, A= 1.0 e-4 cm2 Length~ 100 μm v= 125 cm/sec R= 3 E6 g/sec*cm4 Re= 48.1 ΔP= g/cm*sec2=3750 Pa Fluid Up the Reservoir (D=0.4 cm, A=0.126 cm2) Length= 1.02 cm v~0.1 cm/sec R= g/sec*cm4 Re= 4 ΔP= g/cm*sec2= Pa

11 Final Results 1.25 E 10 μm3/sec= 0.0125 cm3/sec
Total Pressure Gradient: ~50430Pa~378 Torr Pressure Gradient at the Valve: 3750 Pa~28 Torr Fluid Flow Rate 1.25 E 10 μm3/sec= cm3/sec Total Cycle Time: ~21.2 seconds


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