You have been asked to design a heat exchanger to pasturize milk by raising it from 4°C to 72°C. The milk will be run through the heat exchanger at a flow rate of 15 liters/second. To create the heat exchanger, milk will flow through tubes with a 1.2 cm diameter. The tubes will be kept at a constant surface temperature through exposure to condensing steam at 100°C. You have been asked to calculate the following: • A single tube design – You must specify: ∗ The length of the tube ∗ Average milk velocity ∗ The pressure drop required to operate the exchanger ∗ Give at least two reasons why a single tube heat exchanger is not feasible

Elements Of Electromagnetics
7th Edition
ISBN:9780190698614
Author:Sadiku, Matthew N. O.
Publisher:Sadiku, Matthew N. O.
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I have the following problem, and my solution is shown in the image, is it correct? Please verify the calculations

You have been asked to design a heat exchanger to pasturize milk by raising it from 4°C to 72°C. The milk will be run through the heat exchanger at a flow rate of 15 liters/second. To create the heat exchanger, milk will flow through tubes with a 1.2 cm diameter. The tubes will be kept at a constant surface temperature through exposure to condensing steam at 100°C.

You have been asked to calculate the following:

• A single tube design

– You must specify:
∗ The length of the tube

∗ Average milk velocity
∗ The pressure drop required to operate the exchanger
∗ Give at least two reasons why a single tube heat exchanger is not feasible

Irichon tacby- F 0-316
= 06105
Pressuri toss due to f
un duct
Jx Vm Y L
0•o105x (132-62}*x&402
hL =
O'012 x 24 9:44
hi= 6642-35m
DP = hL Pmxga
6592-35 × ' 1030x4.44
DP =
6-615X16 Pascd
Concluion
The single tube is not. eompensiate the
large amount of Pessux toss .
velociny .
and uoy high,
Transcribed Image Text:Irichon tacby- F 0-316 = 06105 Pressuri toss due to f un duct Jx Vm Y L 0•o105x (132-62}*x&402 hL = O'012 x 24 9:44 hi= 6642-35m DP = hL Pmxga 6592-35 × ' 1030x4.44 DP = 6-615X16 Pascd Concluion The single tube is not. eompensiate the large amount of Pessux toss . velociny . and uoy high,
Om =154s 215 xlo3mls
%3D
Im : 163okg Im3
D=1-20m
Tmin yo
7i: Tmo
0'002 Pass
L= S:402m
Ts = lo0°C
O - Heat han ster Rale toom conkinsing syskm seam
O = mm•lpm ( mo-Tmi =
ms xh tys
- ms 21bo
mis = l4269 hgls,
%3D
vdlocty th vougn milk
Om = AxVm =
ISX16-3
Vm =
132-63mls
Reynoia numbir =
V Sm D
b'002
Re = S1964 7.96
- How w tuablent
Nuo =
= D'013 19 647.96)"x
lo0213930
Nuo = 4,073•6
hm =
NuD xk
hm
135786.67 W/mt k
O = hm TCDL C Tums -Tmi)
13378.67 X TLX O012 *96
G.402m
Transcribed Image Text:Om =154s 215 xlo3mls %3D Im : 163okg Im3 D=1-20m Tmin yo 7i: Tmo 0'002 Pass L= S:402m Ts = lo0°C O - Heat han ster Rale toom conkinsing syskm seam O = mm•lpm ( mo-Tmi = ms xh tys - ms 21bo mis = l4269 hgls, %3D vdlocty th vougn milk Om = AxVm = ISX16-3 Vm = 132-63mls Reynoia numbir = V Sm D b'002 Re = S1964 7.96 - How w tuablent Nuo = = D'013 19 647.96)"x lo0213930 Nuo = 4,073•6 hm = NuD xk hm 135786.67 W/mt k O = hm TCDL C Tums -Tmi) 13378.67 X TLX O012 *96 G.402m
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