| |
 |
|
|
 |
| Recommendations for the determination of capillary tube size |
 |
Table considers condensing temperature Tc = 45 °C and heat exchanger in capillary..
Increase length 2% per each K of increase of condensing temperature..
|
 |
| TABLE FOR REFRIGERANT R134a (LBP) |
| Capillary tube length (m) |
| QASH |
M |
Capillary tube internal diameter (mm) & Evaporating temperature (°C) |
| 0,6 | 0,7 | 0,8 | 0,9 | 1 | 1,2 | 1,5 |
| kcal/h | kg/h | -30 | -23,3 | -30 | -23,3 | -30 | -23,3 | -30 | -23,3 | -30 | -23,3 | -30 | -23,3 | -30 | -23,3 |
| 75 | 1,69 | 2,81 | 2,96 | | | | | | | | | | | | |
| 80 | 1,80 | 2,47 | 2,60 | | | | | | | | | | | | |
| 85 | 1,91 | 2,18 | 2,31 | | | | | | | | | | | | |
| 90 | 2,03 | 1,95 | 2,06 | | | | | | | | | | | | |
| 95 | 2,14 | 1,75 | 1,85 | | | | | | | | | | | | |
| 100 | 2,25 | 1,58 | 1,67 | | | | | | | | | | | | |
| 105 | 2,36 | 1,43 | 1,52 | 3,30 | 3,48 | | | | | | | | | | |
| 110 | 2,48 | 1,30 | 1,38 | 3,00 | 3,17 | | | | | | | | | | |
| 115 | 2,59 | 1,19 | 1,26 | 2,74 | 2,90 | | | | | | | | | | |
| 120 | 2,70 | 1,10 | 1,16 | 2,52 | 2,66 | | | | | | | | | | |
| 125 | 2,82 | 1,01 | 1,07 | 2,32 | 2,45 | | | | | | | | | | |
| 130 | 2,93 | | | 2,14 | 2,26 | | | | | | | | | | |
| 140 | 3,15 | | | 1,85 | 1,95 | 3,82 | 4,04 | | | | | | | | |
| 150 | 3,38 | | | 1,61 | 1,70 | 3,32 | 3,51 | | | | | | | | |
| 160 | 3,60 | | | 1,41 | 1,49 | 2,91 | 3,08 | | | | | | | | |
| 170 | 3,83 | | | 1,25 | 1,32 | 2,58 | 2,72 | | | | | | | | |
| 180 | 4,05 | | | 1,11 | 1,17 | 2,29 | 2,42 | | | | | | | | |
| 190 | 4,28 | | | | | 2,06 | 2,17 | 3,90 | 4,12 | | | | | | |
| 200 | 4,50 | | | | | 1,85 | 1,95 | 3,52 | 3,71 | | | | | | |
| 210 | 4,73 | | | | | 1,68 | 1,77 | 3,18 | 3,36 | | | | | | |
| 220 | 4,95 | | | | | 1,53 | 1,61 | 2,90 | 3,06 | | | | | | |
| 230 | 5,18 | | | | | 1,39 | 1,47 | 2,65 | 2,79 | | | | | | |
| 240 | 5,41 | | | | | 1,28 | 1,35 | 2,43 | 2,56 | 4,29 | 4,56 | | | | |
| 250 | 5,63 | | | | | | 1,24 | 2,23 | 2,36 | 3,94 | 4,19 | | | | |
| 275 | 6,19 | | | | | | | 1,84 | 1,94 | 3,25 | 3,45 | | | | |
| 300 | 6,76 | | | | | | | 1,54 | 1,63 | 2,72 | 2,89 | | | | |
| 325 | 7,32 | | | | | | | | 1,38 | 2,31 | 2,45 | | | | |
| 350 | 7,88 | | | | | | | | 1,19 | 1,98 | 2,10 | | | | |
| 375 | 8,45 | | | | | | | | 1,03 | 1,72 | 1,83 | | | | |
| 400 | 9,01 | | | | | | | | | | 1,60 | 4,11 | 4,34 | | |
| 425 | 9,57 | | | | | | | | | | 1,41 | 3,63 | 3,83 | | |
| 450 | 10,14 | | | | | | | | | | 1,26 | 3,22 | 3,40 | | |
| 475 | 10,70 | | | | | | | | | | 1,13 | 2,88 | 3,04 | | |
| 500 | 11,26 | | | | | | | | | | 1,01 | 2,59 | 2,73 | | |
| 525 | 11,82 | | | | | | | | | | | 2,34 | 2,47 | | |
| 550 | 12,39 | | | | | | | | | | | 2,13 | 2,24 | | |
| 575 | 12,95 | | | | | | | | | | | 1,94 | 2,05 | | |
| 600 | 13,51 | | | | | | | | | | | 1,78 | 1,87 | | |
| 650 | 14,64 | | | | | | | | | | | | 1,59 | | |
| 700 | 15,77 | | | | | | | | | | | | 1,36 | 4,38 | 4,61 |
| 750 | 16,89 | | | | | | | | | | | | 1,18 | 3,79 | 4,00 |
| 800 | 18,02 | | | | | | | | | | | | 1,03 | 3,30 | 3,49 |
| 850 | 19,14 | | | | | | | | | | | | | 2,91 | 3,07 |
| 900 | 20,27 | | | | | | | | | | | | | 2,58 | 2,72 |
| 950 | 21,40 | | | | | | | | | | | | | 2,30 | 2,42 |
| 1000 | 22,52 | | | | | | | | | | | | | 2,06 | 2,18 |
|
 |
QASH is the cooling capacity under ASHRAE (LBP) condition corresponding to the indicated mass flow rate M (liquid subcooled down to 32 °C, return gas superheated up to 32 °C)..
The relationship between length and diameter is, approximately: (L / L0) = (D / D0)5,4..
|
|
| |
| |
|
|