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perry s chemical engineers phần 5 pot
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Mô tả chi tiết
pressure drop with laminar flow (Rev < 100) of liquids across banks of
plain tubes with pitch ratios P/Dt of 1.25 and 1.50:
∆p = 1.6 m
(6-164)
m = (6-165)
where Rev = DvVmaxρ/µb; Dv = volumetric hydraulic diameter [(4 ×
free-bundle volume)/(exposed surface area of tubes)]; P = pitch (= a
for in-line arrangements, = a or c [whichever is smaller] for staggered
0.57
(Rev)
0.25
ρV2
max
2
µs µb
Dt P
280Nr
Rev
arrangements), and other quantities are as defined following Eq.
(6-163). Bergelin, et al. (ibid.) show that pressure drop per row is
independent of the number of rows in the bank with laminar flow. The
pressure drop is predicted within about 25 percent.
6-38 FLUID AND PARTICLE DYNAMICS
FIG. 6-43 Friction factors for in-line tube banks. (From Grimison, Trans. ASME, 59, 583 [1937].)
FIG. 6-44 Friction factors vs. transverse spacing for single row of tubes. (From
Boucher and Lapple, Chem. Eng. Prog., 44, 117 [1948].)
FIG. 6-45 Friction factors for transition region flow across tube banks. (Pitch
is the minimum center-to-center tube spacing.) (From Bergelin, Brown, and
Doberstein, Trans. ASME, 74, 953 [1952].)