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A8_Microfluidics_fundamentals_II

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A8 – Microfluidics II

Microfluidic structures

Integrated Microimmunoassay (INESC MN)

laminar flow

short diffusion times

high hydraulic resistance small volumes

large S/V ratio

surface tension important

A microfluidic chemostat (S. Quake, Caltech)

Integrated components: Actuators valves mixers pumps / Sensors / Systems macromolecular analysis DNA analysis enzyme assays immunoassays cellular analysis cytometry cell-based assays cell biosensors cell culturing

Complete formulation: a system of 5 scalar equations with five unknowns (u, v, w, P, c), two fluid properties (ρ and η), the diffusion constant of the species (D), and

NS two external actions on the fluid (the body force per unit volume F and the concentration source or sink per unit volume S

Usually in microfluidics systems, the flow of the buffer

fluid is permanent (steady state) and only the concentration changes with time. Moreover, we can assume that ρ, η and D are constant and that there are no body forces (gravity

is usually negligible in very small systems)

If the hypothesis of creeping flow is valid, ie, the Stokes approximation is justified (inertial forces much smaller than viscous forces), the system above collapses to

a linear system (under the condition that the function S is well behaved).

Microfluidic systems by soft lithography

UV exposure

Fabrication of a mold using SU-8 photoresist

-typical channel dimensions:

 

 

 

 

 

thickness:

20 µm

 

 

 

 

 

 

 

 

 

 

width:

10-~300 µm

 

 

 

 

 

length:

100’s of µm to cm’s

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

Replication of mold in PDMS

Activate surface of PDMS and substrate

O2 plasma, UV ozone or corona discharge

Seal PDMS microchannel to substrate

Fluidic unit operations

Micromixing within microfluidic devices

Convection/diffusion transport equation for a single species

small molecules (ions, glucose, urea, etc.) have diffusivities ~10-10-10-9 m2/s, proteins have diffusivities of ~10-12-10-11 m2/s

Passive micromixers

- hydrodynamic focusing

flow rate ratios from (a) 0.366, (b) 0.224, (c) 0.208, (d) 0.194

The sheathing streams, which are infused at a higher flow rate than the sample stream, focus or reduce the width of the sample stream

→ reduce the diffusional path length for mixing

Passive micromixers - chaotic advection

In a chaotic flow field, flow elements that are initially close to each other may become widely separated by stretching and folding of material lines even within a laminar flow field

TLCCM: two-layer crossing

channel micromixers

C-shaped serpentine micromixer

Passive micromixers - chaotic advection

Patterned grooves twist incoming flow streamlines, creating vortices and hence chaotic advection within the flow stream

Passive micromixers - chaotic advection

Herringbone shaped grooves embedded into the channel floor, periodically alternating the direction of the herringbone pattern

The fluid experiences a repeated sequence of rotational and extensional local flows

→ a high extent of mixing (>95%) was observed for Re up to 100 and two fluids were able to

fully mix within a 3-cm SHM (staggered herringbone micromixer) even with Pe of the order of 103

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