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Specialized in Refrigeration and Air Conditioning |
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Turbo-CDI is designed for light hydrocarbon condensing. The integral helical fins on the outside of the tube are modified to enhance the condensing heat transfer coefficient. The inside heat transfer coefficient is improved because of increased surface area and turbulation induced by integral helical ridges on the inside surface. |
The availability of plain ends and intermediate lands makes Turbo-CDI especially suitable for shell and tube condensers. The increased ID ridge count improves the overall heat transfer efficiency of Turbo-CDI over Turbo-C, while slightly increasing the ID pressure drop. |
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Turbo-CDI - UNS C12200 |
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Standard Sizes |
Plain End Dimensions |
Finned Section Dimensions |
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Catalog Number |
Outside Diameter inch (mm) |
Nominal Wall inch (mm) |
Outside Diameter inch (mm) |
Wall inch (mm) |
Fin Per Inch |
Finished Fin OD inch (mm) |
Min. Wall Under Fins inch (mm) |
Root Diameter inch (mm) |
| 30-4050025 | 3/4 (19.05) | 0.025 (0.635) | 0.743 (18.87) | 0.455 (11.56) | 40 | 0.743 (18.87) | 0.025 (0.635) | 0.668 (16.97) |
| 30-4053528 | 3/4 (19.05) | 0.028 (0.711) | 0.743 (18.87) | 0.049 (1.23) | 40 | 0.743 (18.87) | 0.025 (0.635) | 0.668 (16.97) |
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Turbo-CDI - UNS C12200 |
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Standard Sizes |
Inside Dimensions |
Areas |
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Catalog Number |
Weight Per Unit Length lb/ft (kg/m) |
Nominal Inside Diameter inch (mm) |
Nominal Ridge Height inch (mm) |
Nominal Inside Surface Area ft2/ft (m2/m) |
Actual Inside Surface Area ft2/ft (m2/m) |
Nominal Outside Surface Area ft2/ft (m2/m) |
Actual Outside Surface Area ft2/ft (m2/m) |
| 30-4053528 | 0.360 (0.536) | 0.612 (15.54) | 0.019 (0.483) | 0.160 (0.049) | 0.265 (0.081) | 0.196 (0.060) | 0.711 (0.217) |
| 30-4053528 | 0.360 (0.536) | 0.612 (15.54) | 0.019 (0.483) | 0.160 (0.049) | 0.265 (0.081) | 0.196 (0.060) | 0.711 (0.217) |
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Engineering Data |
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Turbo-CDI - UNS C12200 |
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Catalog Number |
Sieder and Tate2 Constant STCi |
Constants used in Calculating Darcy Friction Factor1 C D |
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| 30-4053528 | 0.069 | 1.107 | 0.289 |
| 30-4053528 | 0.069 | 1.107 | 0.289 |
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1. Constants applicable to Reynolds numbers greater than 20,000. [fDarcy = C(Re)-D] |
| 2. To calculate inside heat transfer coefficient: hi = (k/Di nom.)(STCi)Re0.8Pr1/3[m/mwall)0.14 |
| Rev. draft 07/01 |