For circular channelsthe relation is expressed asR¼ðP 1 P 2 Þ=Q¼ΔP=Q¼ 8 ηl=Πr^4 ð 1 : 51 ÞThe (1.51) can be written asΔP¼RQ¼ 8 ηlQ=Πr^4 ¼ 32 ηlU=r^2 ð 1 : 52 Þwhere,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 Þwhere, Cncis numerical coefficient and is given as
Cnc¼ 8 ðÞAþ 12 =A ð 1 : 54 Þwhere,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 =Ahi
ηlQ=A^2 ð 1 : 55 ÞTable 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 etchingPressure drop along L = P 2 − P 1LP 2r
RFlow ResistanceP 1Fig. 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
222 C.K. Dixit