For circular channelsthe relation is expressed as
R¼ðP 1 P 2 Þ=Q¼ΔP=Q¼ 8 ηl=Πr^4 ð 1 : 51 Þ
The (1.51) can be written as
ΔP¼RQ¼ 8 ηlQ=Πr^4 ¼ 32 ηlU=r^2 ð 1 : 52 Þ
where,ΔP is pressure drop, R is the fluidic resistance, and Q is the volumetric flow
rate through a cross-section area‘A’(Q¼U:A)
For rectangular channelsthe relation in (1.51) is modified to
Rhd¼Cncηl=A^2 ð 1 : 53 Þ
where, Cncis numerical coefficient and is given as
Cnc¼ 8 ðÞAþ 12 =A ð 1 : 54 Þ
where,Ais aspect ratio¼height of the channel (h)/width of the channel (w)
Replacing (1.53) and (1.54)in(1.52)
ΔP¼RhdQ¼CncηlQ=A^2 ¼ 8 ðÞAþ 12 =A
hi
ηlQ=A^2 ð 1 : 55 Þ
Table 1.6 Volumetric flow rates for common geometries
Shape of cross-section Volumetric flow rate (Q) Fabrication approach
Cylindrical Πr^4 ΔP/8ηL Isotropic wet etching, Ball-end milling
Rectangular ΔPw=½ 8 ðAþ 1 Þ^2 =Aη Photolithogrgaphy
Triangular ΔP(3a^4 )1/2/320ηl Anisotropic wet etching
Pressure drop along L = P 2 − P 1
L
P 2
r
R
Flow Resistance
P 1
Fig. 1.8 Illustration of the
pressure drop‘ΔP’along
the channel length‘L’due
to the flow resistance
offered by the fluid to its
motion from point 1 to point
2
22 C.K. Dixit