410A

    • Non-ozone depleting refrigerant, near-azeotropic blend.
    • Developed for air conditioning as well as some medium temperature refrigeration applications.
    forane-410a
    • Residential and commercial air conditioning systems
    • Small chillers
    • Heat pumps
    • Dehumidifiers
    • Medium temperature commercial refrigeration

    Forane® 410A has a high cooling capacity, thus leading to good performance with low refrigerant charge. Forane® 410A equipments provide the best energy efficiency for air conditioning.

    Polyolester (POE) lubricant must be used with Forane® 410A to ensure complete miscibility between oil and refrigerant. Care must be taken when handling POE lubricants because they are hygroscopic, which means that they can readily absorb moisture from the air. High levels of moisture in the system can lead to oil degradation and system failure.

    Due to the near-azeotropic nature of Forane® 410A, it is better to charge it as liquid to prevent fractionation (changes in the designed refrigerant composition) but it can also be charged as gas. In situations where vapor would normally be charged into a system, a valve should be installed in the charging line to flash liquid from the cylinder into vapor. Forane® 410A requires the use of manifold gauge sets, recovery machines, and cylinders specifically designed and rated for its higher pressures.

    Forane® 410A can be delivered in various packaging:

    • bulk: ISO container (18 tons) or ton-tank (730 kg).
    • pallet of 40 or 100 disposable cylinders (11.3 kg each cylinder). This disposable packaging is commercialized according to local regulations.
    • other packaging available under requests.

    This information is based on values calculated using the NIST REFPROP Database (NIST Standard Reference Database 23, Version 9.0, Lemmon, E. W., Huber, M. L.,and McLinden, M. O., Thermophysical Properties Division, 2010).

    Critical temperature: 71°C

    Saturation points (bubble and dew points at same composition).

    Temperature (°C) Pressure (bar) Liquid

    Phase

    Density

    (kg/m3)

    Vapor

    Phase

    Density

    (kg/m3)

    Liquid

    Phase

    Enthalpy

    (kJ/kg)

    Vapor

    Phase

    Enthalpy

    (kJ/kg)

    Liquid

    Phase

    Entropy

    (kJ/(kg.K))

    Vapor

    Phase

    Entropy

    (kJ/(kg.K))

    -40 1,8 1313 7 142 405 0,77 1,90
    -35 2,2 1297 9 149 407 0,80 1,89
    -30 2,7 1280 11 156 410 0,83 1,88
    -25 3,3 1263 13 163 412 0,86 1,86
    -20 4,0 1245 15 170 414 0,89 1,85
    -15 4,8 1227 18 178 416 0,92 1,84
    -10 5,7 1209 22 185 418 0,94 1,83
    -5 6,8 1190 26 192 420 0,97 1,82
    0 8,0 1170 31 200 421 1,00 1,81
    5 9,4 1150 36 208 423 1,03 1,80
    10 10,9 1129 42 215 424 1,05 1,79
    15 12,6 1106 49 223 425 1,08 1,78
    20 14,5 1083 57 232 426 1,11 1,77
    25 16,6 1059 66 240 426 1,14 1,76
    30 18,9 1033 77 248 426 1,16 1,75
    35 21,4 1006 89 257 426 1,19 1,74
    40 24,3 976 103 266 425 1,22 1,73
    45 27,3 943 120 276 424 1,25 1,72
    50 30,7 907 141 286 422 1,28 1,70
    55 34,4 865 167 297 419 1,31 1,68
    60 38,4 815 201 308 414 1,35 1,66
    65 42,8 748 250 322 406 1,39 1,63

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