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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 R134a (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 | 2 |
| 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 | -5 | 7,2 |
| 100 | 2,32 | 4,11 | 3,86 | | | | | | | | | | | | | | |
| 110 | 2,56 | 3,40 | 3,20 | | | | | | | | | | | | | | |
| 120 | 2,79 | 2,88 | 2,71 | | | | | | | | | | | | | | |
| 130 | 3,02 | 2,45 | 2,31 | | | | | | | | | | | | | | |
| 140 | 3,25 | 2,12 | 2,00 | 4,30 | 4,04 | | | | | | | | | | | | |
| 150 | 3,49 | 1,84 | 1,74 | 3,77 | 3,55 | | | | | | | | | | | | |
| 160 | 3,72 | 1,62 | 1,53 | 3,32 | 3,12 | | | | | | | | | | | | |
| 170 | 3,95 | 1,43 | 1,35 | 2,93 | 2,76 | | | | | | | | | | | | |
| 180 | 4,18 | 1,27 | 1,21 | 2,63 | 2,48 | | | | | | | | | | | | |
| 190 | 4,42 | 1,14 | 1,08 | 2,36 | 2,23 | 4,43 | 4,16 | | | | | | | | | | |
| 200 | 4,65 | | | 2,13 | 2,00 | 3,99 | 3,76 | | | | | | | | | | |
| 220 | 5,11 | | | 1,75 | 1,65 | 3,31 | 3,12 | | | | | | | | | | |
| 240 | 5,58 | | | 1,47 | 1,40 | 2,78 | 2,63 | 4,88 | 4,59 | | | | | | | | |
| 260 | 6,04 | | | 1,24 | 1,18 | 2,36 | 2,23 | 4,15 | 3,91 | | | | | | | | |
| 280 | 6,51 | | | 1,06 | 1,02 | 2,04 | 1,93 | 3,60 | 3,40 | | | | | | | | |
| 300 | 6,97 | | | | | 1,77 | 1,68 | 3,13 | 2,96 | | | | | | | | |
| 320 | 7,44 | | | | | 1,55 | 1,47 | 2,75 | 2,60 | | | | | | | | |
| 340 | 7,90 | | | | | 1,36 | 1,30 | 2,42 | 2,29 | | | | | | | | |
| 360 | 8,37 | | | | | 1,21 | 1,15 | 2,17 | 2,06 | | | | | | | | |
| 380 | 8,83 | | | | | 1,08 | 1,03 | 1,94 | 1,84 | 5,19 | 4,89 | | | | | | |
| 400 | 9,30 | | | | | | | 1,74 | 1,66 | 4,67 | 4,42 | | | | | | |
| 450 | 10,46 | | | | | | | 1,36 | 1,30 | 3,69 | 3,48 | | | | | | |
| 500 | 11,62 | | | | | | | 1,09 | 1,05 | 2,99 | 2,83 | | | | | | |
| 550 | 12,78 | | | | | | | | | 2,46 | 2,33 | | | | | | |
| 600 | 13,95 | | | | | | | | | 2,05 | 1,95 | | | | | | |
| 650 | 15,11 | | | | | | | | | 1,73 | 1,65 | 5,83 | 5,50 | | | | |
| 700 | 16,27 | | | | | | | | | 1,47 | 1,42 | 5,00 | 4,73 | | | | |
| 750 | 17,43 | | | | | | | | | 1,28 | 1,23 | 4,38 | 4,15 | | | | |
| 800 | 18,60 | | | | | | | | | 1,11 | 1,08 | 3,84 | 3,64 | | | | |
| 850 | 19,76 | | | | | | | | | | | 3,39 | 3,22 | | | | |
| 900 | 20,92 | | | | | | | | | | | 3,00 | 2,86 | | | | |
| 1000 | 23,25 | | | | | | | | | | | 2,40 | 2,30 | 4,80 | 4,54 | | |
| 1100 | 25,57 | | | | | | | | | | | 1,98 | 1,90 | 3,94 | 3,74 | | |
| 1200 | 27,89 | | | | | | | | | | | 1,64 | 1,58 | 3,28 | 3,12 | | |
| 1300 | 30,22 | | | | | | | | | | | 1,37 | 1,33 | 2,79 | 2,66 | | |
| 1400 | 32,54 | | | | | | | | | | | 1,16 | 1,13 | 2,38 | 2,29 | | |
| 1500 | 34,87 | | | | | | | | | | | | | 2,05 | 1,98 | 5,01 | 4,76 |
| 1600 | 37,19 | | | | | | | | | | | | | 1,78 | 1,72 | 4,42 | 4,21 |
| 1700 | 39,52 | | | | | | | | | | | | | 1,55 | 1,51 | 3,90 | 3,72 |
| 1800 | 41,84 | | | | | | | | | | | | | 1,36 | 1,33 | 3,45 | 3,31 |
| 1900 | 44,17 | | | | | | | | | | | | | 1,20 | 1,18 | 3,08 | 2,95 |
| 2000 | 46,49 | | | | | | | | | | | | | 1,06 | 1,05 | 2,75 | 2,65 |
| 2250 | 52,30 | | | | | | | | | | | | | | | 2,12 | 2,06 |
| 2500 | 58,11 | | | | | | | | | | | | | | | 1,66 | 1,63 |
| 2750 | 63,92 | | | | | | | | | | | | | | | 1,35 | 1,33 |
| 3000 | 69,74 | | | | | | | | | | | | | | | 1,09 | 1,10 |
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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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