| Surface Heat Transfer area of Square
"CUBE" compared with Round "Tube" ,or "Shell" |
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in Inches and
Inches square |
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Comments |
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"TUBE" or "SHELL" |
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"CUBE" |
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The Same |
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Compare |
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"Tube" "Shell" |
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GAP |
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"CUBE" |
"Cube" Improved |
Cube Area- Tube Area |
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Same |
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Cirumference |
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Same Flow |
Width of Channel |
Heat Transfer Area |
Heat Transfer area |
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| Inner R tube |
Outer R tube |
Flow Area |
Area for flow |
Heat Transfer |
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Hight of |
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Area for "Cube" |
for the same area |
of Square Design |
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Inner Tube |
Outer Tube |
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Area |
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Channel |
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in both fluids |
of flow & same gap |
top+bottom, no sides |
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X |
X |
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XX |
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| ================= |
================================================================================================================================================== |
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1" Gap is just too small to avoid blockage
using Sludge |
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| 1 |
2 |
3.14 |
9.42 |
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6.28 |
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1 |
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3.14 |
3.14 |
6.28 |
0.00 |
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| 2 |
3 |
12.56 |
15.70 |
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12.56 |
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1 |
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12.56 |
12.56 |
25.12 |
12.56 |
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| 3 |
4 |
28.26 |
21.98 |
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18.84 |
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1 |
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28.26 |
28.26 |
56.52 |
37.68 |
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| 4 |
5 |
50.24 |
28.26 |
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25.12 |
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1 |
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50.24 |
50.24 |
100.48 |
75.36 |
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| 5 |
6 |
78.50 |
34.54 |
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31.40 |
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1 |
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78.50 |
78.50 |
157.00 |
125.60 |
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2" Gap
is the Minimum of Minimum to avoid blockage
using Sludge |
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| 2 |
4 |
12.56 |
37.68 |
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12.56 |
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2 |
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12.56 |
6.28 |
12.56 |
0.00 |
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| 3 |
5 |
28.26 |
50.24 |
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18.84 |
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2 |
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28.26 |
14.13 |
28.26 |
9.42 |
most common |
| 4 |
6 |
50.24 |
62.80 |
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25.12 |
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2 |
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50.24 |
25.12 |
50.24 |
25.12 |
most common |
| 5 |
7 |
78.50 |
75.36 |
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31.40 |
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2 |
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78.50 |
39.25 |
78.50 |
47.10 |
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| 6 |
8 |
113.04 |
87.92 |
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37.68 |
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2 |
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113.04 |
56.52 |
113.04 |
75.36 |
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| 7 |
9 |
153.86 |
100.48 |
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43.96 |
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2 |
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153.86 |
76.93 |
153.86 |
109.90 |
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3" gap clearance is good for Non Plug |
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| 3 |
6 |
28.26 |
84.78 |
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18.84 |
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3 |
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28.26 |
9.42 |
18.84 |
0.00 |
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| 4 |
7 |
50.24 |
103.62 |
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25.12 |
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3 |
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50.24 |
16.75 |
33.49 |
8.37 |
most common |
| 5 |
8 |
78.50 |
122.46 |
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31.40 |
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3 |
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78.50 |
26.17 |
52.33 |
20.93 |
most common |
| 6 |
9 |
113.04 |
141.30 |
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37.68 |
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3 |
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113.04 |
37.68 |
75.36 |
37.68 |
most common |
| 7 |
10 |
153.86 |
160.14 |
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43.96 |
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3 |
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153.86 |
51.29 |
102.57 |
58.61 |
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| 8 |
11 |
200.96 |
178.98 |
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50.24 |
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3 |
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200.96 |
66.99 |
133.97 |
83.73 |
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| 4 |
8 |
50.24 |
150.72 |
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25.12 |
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4 |
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50.24 |
12.56 |
25.12 |
0.00 |
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| 5 |
9 |
78.50 |
175.84 |
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31.40 |
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4 |
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78.50 |
19.63 |
39.25 |
7.85 |
most common |
| 6 |
10 |
113.04 |
200.96 |
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37.68 |
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4 |
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113.04 |
28.26 |
56.52 |
18.84 |
most common |
| 7 |
11 |
153.86 |
226.08 |
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43.96 |
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4 |
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153.86 |
38.47 |
76.93 |
32.97 |
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| X |
The "Tube" Heat Exchanger, has as a
rule DIFFERENT Flow Area in the Inner and Outer tubes, It may create too high
or too low velocity in one of the tube, which can reduce the Heat Transfer. |
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| XX |
The "Cube" Heat Exchanger has as a
rule the same Flow Area for Cold and Hot Fluids (optional different sizes),
this as a rule creates better Designed and controlled Heat Transfer. |
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Also the "Tube" or "Shell"
type Heat Exchangers are not as stackable, compact as Flat Heat Exchangers,
therefore usually the "Cube" Heat Exchanger is much smaller . |
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