
| Shell diameter, mm | Pressure, Pó, MPa | Heat-exchange area, m2 w/tubes 025 | L, mm | Í, mm | DN, mm at number of passages per tube: | DN1, mm |
DN2, mm |
L1, mm |
||
| 2 | 4 | 6 | ||||||||
| 630 | 1,0 1,6 2,5 |
105 93 86 |
6900 | 1060 | 200 | 150 | 100 | 300 250 200 |
100 | 700 |
| 800 | 1,0 1,6 2,5 |
191 173 164 |
7080 | 1354 | 250 | 200 | 150 | 400 300 250 |
150 | 650 |
| 1000 | 1,0 1,6 2,5 |
325 300 289 |
7290 | 1558 | 300 | 200 | 150 | 400 300 300 |
200 | 600 |
| 1200 | 1,0 1,6 2,5 |
489 460 442 |
7500 | 1780 | 300 | 250 | 200 | 500 400 350 |
250 | 550 |
| 1400 | 1,0 1,6 2,5 |
675 642 626 |
7750 | 1980 | 350 | 250 | 200 | 500 400 350 |
250 | 470 |
Note: Heat exchanger diameter of 630 mm is considered as outer diameter, the exceeding diameter is specified as internal diameter. Upon the Customer's request, we can produce condensers of special values and dimensions.
Identification Example (for ordering):
Floating-head condenser 1000KP-1,6-1/25-6-2-T as per TU (Spec.) 3612-023-00220302-01, where
1000 – shell diameter, mm;
KP – floating-head condenser;
1,6 – shell pressure, MPa;
Ì1 – material design;
25 – heat-exchanging tubes diameter, mm;
6 – tube length, m;
2 – number of passages per tube;
Ò – w/heat-transfer tubes arranged in sheet in equilateral-triangle way.
Square arrangement of heat-transfer tubes is available on request.




