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| Recommendations for the determination of capillary tube size |
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Table considers condensing temperature Tc = 45 °C. Non adiabatic flow in capillary..
Increase length 2% per each K of increase of condensing temperature..
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| TABLE FOR REFRIGERANT R290 (HMBP) |
| Capillary tube length (m) |
| QASH |
M |
Capillary tube internal diameter (mm) & Evaporating temperature (°C) |
| 0,7 | 0,8 | 0,9 | 1 | 1,2 | 1,5 | 1,7 |
| kcal/h | kg/h | -5 | 7,2 | -5 | 7,2 | -5 | 7,2 | -5 | 7,2 | -5 | 7,2 | -5 | 7,2 | -5 | 7,2 |
| 130 | 1,58 | 5,12 | 4,39 | | | | | | | | | | | | |
| 140 | 1,70 | 4,43 | 4,06 | | | | | | | | | | | | |
| 150 | 1,83 | 3,88 | 3,55 | | | | | | | | | | | | |
| 160 | 1,95 | 0,41 | 3,12 | | | | | | | | | | | | |
| 170 | 2,07 | 3,01 | 2,77 | | | | | | | | | | | | |
| 180 | 2,19 | 2,70 | 2,48 | 5,50 | 5,04 | | | | | | | | | | |
| 190 | 2,31 | 2,43 | 2,23 | 4,95 | 4,54 | | | | | | | | | | |
| 200 | 2,43 | 2,19 | 2,01 | 4,47 | 4,10 | | | | | | | | | | |
| 220 | 2,68 | 1,80 | 1,66 | 3,69 | 3,40 | | | | | | | | | | |
| 240 | 2,92 | 1,51 | 1,40 | 3,12 | 2,86 | 5,84 | 5,35 | | | | | | | | |
| 260 | 3,16 | 1,29 | 1,19 | 2,66 | 2,44 | 4,97 | 4,56 | | | | | | | | |
| 280 | 3,41 | 1,11 | 1,03 | 2,28 | 2,10 | 4,30 | 3,95 | | | | | | | | |
| 300 | 3,65 | | | 1,98 | 1,83 | 3,76 | 3,45 | | | | | | | | |
| 320 | 3,89 | | | 1,75 | 1,62 | 3,30 | 3,04 | | | | | | | | |
| 340 | 4,14 | | | 1,55 | 1,43 | 2,92 | 2,69 | 5,11 | 4,71 | | | | | | |
| 360 | 4,38 | | | 1,38 | 1,27 | 2,60 | 2,39 | 4,60 | 4,22 | | | | | | |
| 380 | 4,62 | | | 1,23 | 1,14 | 2,33 | 2,15 | 4,13 | 3,79 | | | | | | |
| 400 | 4,87 | | | 1,10 | 1,02 | 2,11 | 1,95 | 3,72 | 3,42 | | | | | | |
| 450 | 5,48 | | | | | 1,66 | 1,54 | 2,93 | 2,69 | | | | | | |
| 500 | 6,08 | | | | | 1,33 | 1,24 | 2,38 | 2,19 | | | | | | |
| 550 | 6,69 | | | | | 1,09 | 1,01 | 1,96 | 1,81 | 5,23 | 4,80 | | | | |
| 600 | 7,30 | | | | | | | 1,63 | 1,51 | 4,38 | 4,03 | | | | |
| 650 | 7,91 | | | | | | | 1,38 | 1,28 | 3,72 | 3,42 | | | | |
| 700 | 8,52 | | | | | | | 1,18 | 1,10 | 3,21 | 2,96 | | | | |
| 750 | 9,13 | | | | | | | | | 2,80 | 2,59 | | | | |
| 800 | 9,73 | | | | | | | | | 2,46 | 2,27 | | | | |
| 850 | 10,34 | | | | | | | | | 2,17 | 2,00 | | | | |
| 900 | 10,95 | | | | | | | | | 1,92 | 1,78 | | | | |
| 950 | 11,56 | | | | | | | | | 1,71 | 1,59 | | | | |
| 1000 | 12,17 | | | | | | | | | 1,54 | 1,43 | 5,17 | 4,76 | | |
| 1050 | 12,78 | | | | | | | | | 1,38 | 1,29 | 4,70 | 4,34 | | |
| 1100 | 13,38 | | | | | | | | | 1,25 | 1,17 | 4,30 | 3,96 | | |
| 1150 | 13,99 | | | | | | | | | 1,14 | 1,07 | 3,93 | 3,63 | | |
| 1200 | 14,60 | | | | | | | | | | | 3,60 | 3,33 | | |
| 1250 | 15,21 | | | | | | | | | | | 3,31 | 3,06 | | |
| 1300 | 15,82 | | | | | | | | | | | 3,05 | 2,83 | | |
| 1350 | 16,43 | | | | | | | | | | | 2,82 | 2,61 | | |
| 1400 | 17,03 | | | | | | | | | | | 2,61 | 2,42 | 5,18 | 4,77 |
| 1450 | 17,64 | | | | | | | | | | | 2,43 | 2,25 | 4,82 | 4,45 |
| 1500 | 18,25 | | | | | | | | | | | 2,26 | 2,10 | 4,50 | 4,15 |
| 1550 | 18,86 | | | | | | | | | | | 2,11 | 1,96 | 4,20 | 3,88 |
| 1600 | 19,47 | | | | | | | | | | | 1,97 | 1,84 | 3,94 | 3,64 |
| 1650 | 20,08 | | | | | | | | | | | 1,84 | 1,72 | 3,69 | 3,42 |
| 1700 | 20,68 | | | | | | | | | | | 1,73 | 1,62 | 3,47 | 3,21 |
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QASH is the cooling capacity under ASHRAE (HMBP) condition corresponding to the indicated mass flow rate M (liquid subcooled 9K, return gas superheated up to 35 °C)..
The relationship between length and diameter is, approximately: (L / L0) = (D / D0)5,4..
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