| TSL | |||||||||
| 性價比佳。 | |||||||||
| 光管段 | 翅片段 | ||||||||
| 项次 | 外径 mm | 外径 mm | 有效壁厚 mm | 最小壁厚 mm | 内齿高 mm | 名义外表面积 ㎡/m | 实际外表面积 ㎡/m | 名义内表面积 ㎡/m | 实际内表面积 ㎡/m |
| O.D. | O.D. | Wall Thickness | minimum Wall Thickness | Ridge Height | Nominal outside surface area | actualoutside surface area | Nominal inside surface area | Nominal inside surface area | |
| 1 | 15.88 | 15.70 | 0.635 | 0.56 | 0.30 | 0.0499 | 0.1733 | 0.0429 | 0.0625 |
| 2 | 19.05 | 18.85 | 0.635 | 0.56 | 0.35 | 0.0598 | 0.2282 | 0.0529 | 0.0858 |
| 3 | 19.05 | 18.85 | 0.711 | 0.63 | 0.35 | 0.0598 | 0.2387 | 0.0526 | 0.0858 |
| 4 | 19.05 | 18.85 | 0.889 | 0.80 | 0.35 | 0.0598 | 0.2482 | 0.0523 | 0.0852 |
| 5 | 25.40 | 25.15 | 0.635 | 0.56 | 0.40 | 0.0798 | 0.3098 | 0.0725 | 0.1202 |
| 6 | 25.40 | 25.15 | 0.711 | 0.63 | 0.40 | 0.0798 | 0.3229 | 0.0722 | 0.1194 |
| TLC | |||||||||
| 单管性能佳。 | |||||||||
| 光管段 | 翅片段 | ||||||||
| 项次 | 外径 mm | 外径 mm | 有效壁厚 mm | 最小壁厚 mm | 内齿高 mm | 名义外表面积 ㎡/m | 实际外表面积 ㎡/m | 名义内表面积 ㎡/m | 实际内表面积 ㎡/m |
| O.D. | O.D. | Wall Thickness | minimum Wall Thickness | Ridge Height | Nominal outside surface area | actualoutside surface area | Nominal inside surface area | Nominal inside surface area | |
| 1 | 12.7 | 12.65 | 0.600 | 0.50 | 0.20 | 0.0399 | 0.1101 | 0.0348 | 0.0433 |
| 2 | 15.88 | 15.70 | 0.635 | 0.56 | 0.30 | 0.0499 | 0.1733 | 0.0429 | 0.0869 |
| 3 | 19.05 | 18.85 | 0.635 | 0.56 | 0.38 | 0.0598 | 0.2292 | 0.0529 | 0.0901 |
| 4 | 19.05 | 18.85 | 0.711 | 0.63 | 0.38 | 0.0598 | 0.2387 | 0.0529 | 0.0901 |
| 5 | 19.05 | 18.85 | 0.889 | 0.80 | 0.38 | 0.0598 | 0.2482 | 0.0526 | 0.0895 |
| 6 | 25.40 | 25.15 | 0.635 | 0.56 | 0.40 | 0.0798 | 0.3098 | 0.0725 | 0.1202 |
| 7 | 25.40 | 25.15 | 0.711 | 0.63 | 0.40 | 0.0798 | 0.3229 | 0.0722 | 0.1194 |
* Tube fin shape with special design, increase the heat exchange area, thinning of the fin on the film thickness, thus increasing the condensation heat transfer coefficient; while the tube with spiral grooves, enhanced heat transfer tube; both sides of comprehensive effect of heat transfer enhancement can greatly improve the heat transfer coefficient of the total.
* The total heat transfer coefficient is 3-5 times higher than that of the ordinary smooth tube.
* By the condenser condenser tube, because the tube has thermal coefficient and larger heat transfer surface area in the high, thereby reducing the number of use tubes, reduces the condenser volume, reduce copper consumption and manufacturing cost, and reduce energy consumption in operation.
