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ID/OD Enhanced Surface for Improved
Boiling Heat Transfer |
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Turbo-BIII is designed for light hydrocarbon boiling. The tube is configured in variations for both high pressure and low pressure refrigerant applications. The integral helical fins on the outside of the tube are modified to enhance the initiation of nucleate boiling sites, thus improving the over all heat transfer coefficient. The inside heat transfer coefficient is improved because of increased some |
surface area and turbulation induced by integral helical ridges on the inside surface. The availability of plain ends and intermediate lands makes Turbo-BIII suitable for shell and tube evaporators. The ID ridges have been modified to improve the overall heat transfer efficiency of Turbo-BIII over Turbo-BII. |
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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) |
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Turbo-BIII High Pressure - UNS 12200 |
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| 75-6050025 | 3/4 (19.05) | 0.025 (0.635) | 0.743 (18.87) | 0.047 (1.18) | 60 | 0.745 (18.92) | 0.022 (0.559) | 0.696 (17.68) |
| 75-6050028 | 3/4 (19.05) | 0.028 (0.711) | 0.743 (18.87) | 0.050 (1.26) | 60 | 0.744 (18.90) | 0.025 (0.635) | 0.696 (17.68) |
| 75-6050035 | 3/4 (19.05) | 0.035 (0.889) | 0.743 (18.87) | 0.056 (1.42) | 60 | 0.744 (18.90) | 0.031 (0.787) | 0.696 (17.68) |
| 75-6078025 | 1 (25.40) | 0.025 (0.635) | 0.995 (25.27) | 0.050 (1.26) | 60 | 0.986 (25.04) | 0.022 (0.559) | 0.937 (23.80) |
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Turbo-BIII Low Pressure - UNS 12200 |
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| 75-6156025 | 3/4 (19.05) | 0.025 (0.635) | 0.743 (18.87) | 0.049 (1.23) | 62 | 0.744 (18.90) | 0.022 (0.559) | 0.697 (17.70) |
| 75-6150028 | 3/4 (19.05) | 0.028 (0.711) | 0.743 (18.87) | 0.050 (1.27) | 62 | 0.741 (18.82) | 0.025 (0.635) | 0.698 (17.73) |
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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 Inside Cross Sect. Area in2 (mm2) |
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Turbo-BIII High Pressure - UNS 12200 |
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| 75-6050025 | 0.371 (0.552) | 0.645 (16.38) | 0.015 (0.381) | 0.169 (0.052) | 0.262 (0.080) | 0.192 (0.059) | 0.315 (203.2) |
| 75-6050028 | 0.422 (0.658) | 0.639 (16.23) | 0.015 (0.381) | 0.167 (0.051) | 0.260 (0.079) | 0.192 (0.059) | 0.309 (199.4) |
| 75-6050035 | 0.448 (0.667) | 0.625 (15.88) | 0.013 (0.330) | 0.164 (0.050) | 0.239 (0.073) | 0.192 (0.059) | 0.297 (191.6) |
| 75-6078025 | 0.505 (0.752) | 0.887 (22.53) | 0.017 (0.432) | 0.232 (0.071) | 0.374 (0.114) | 0.260 (0.079) | 0.374 (241.3) |
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Turbo-BIII Low Pressure - UNS 12200 |
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| 75-6150028 | 0.391 (0.581) | 0.639 (16.23) | 0.015 (0.381) | 0.167 (0.051) | 0.260 (0.079) | 0.192 (0.059) | 0.309 (199.4) |
| 75-6156025 | N/A | 0.647 (16.43) | 0.015 (0.381) | 0.169 (0.052) | 0.256 (0.078) | 0.192 (0.059) | 0.318 (205.2) |
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Engineering Data |
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Catalog Number |
Sieder and Tate2 Constant STCi |
Constants used in Calculating Darcy Friction Factor1 C D |
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Turbo-BIII High Pressure - UNS 12200 |
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| 75-6050025 | 0.073 | 0.686 | 0.250 |
| 75-6050028 | 0.073 | 0.686 | 0.250 |
| 75-6050035 | 0.066 | 0.680 | 0.255 |
| 75-6078025 | 0.076 | 0.644 | 0.240 |
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Turbo-BIII Low Pressure - UNS 12200 |
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| 75-6150028 | 0.073 | 0.759 | 0.254 |
| 75-6156025 | 0.073 | 0.686 | 0.250 |
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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 08/01 |