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Refrigerant quantity vs efficiency etc?

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I have a few questions that I can't quite wrap my head around.

There's been a constant trend to try and minimize the amount of refrigerant in systems.

My understanding is there's several reasons for it, but the main one is apparently for efficiency.

How and why does a large refrigerant charge effect system efficiency? I'm not asking how an undercharged or overcharged system behaves, but why a system designed to use a smaller charge operates more efficiently than one designed around a larger charge? Assuming you've got minimal SH and reasonable SC why does the quantity matter in regards to efficiency?

Also,

Why do some refrigerants require less of a charge I.E. R134A vs R12 in a retrofitted system, or R152A in a R134A system. Why does the system suddenly need less liquid in areas? Does the liquid weigh less, so it's technically the same volume but less weight? Or is there something else going on?

The next question is probably going to be above my head but I'm going to try…..

Why does it seem like some refrigerants, like 410A that run at a much higher pressure actually work more efficiently than others like R22? Or, is that simply because higher pressure means more compressed and the actual pressure difference between high and low is similar? I've never actually checked that……

Single pipe 392sqft system with an EG-40 rated for 325sqft and it's silent and balanced at all times.

Comments

  • mattmia2
    mattmia2 Member Posts: 17,528
    edited 3:34PM

    is the 410a vs 22 efficiency the refrigerant or the system design, was higher efficiency required around the time r22 was phased out? in 2001 when i bought my split system if i recall there was not much in the way of efficiency requirements, you could buy systems with different efficiencies but i don't think it was mandated yet.

    you can find the densities of different refrigerants on wikipedia.

    the evaporator has to remain full of liquid but the amount of liquid and gas in the condenser could vary with different refrigerants.

    if there is less refrigerant you have to pump less stuff but i don't know if that is the efficiency reason. maybe a higher ratio of tube surface to tube volume means the compressor has to move less stuff but that is pure speculation.

  • EdTheHeaterMan
    EdTheHeaterMan Member Posts: 12,517

    A smaller refrigerant charge by itself does not magically improve efficiency. What improves efficiency is the system architecture that allows the machine to operate well with a smaller charge: smaller internal volumes, shorter lines, better coil circuitry, microchannel or optimized tube coils, lower hold-up volume, tighter control, and less “extra” refrigerant sitting in places where it is not doing useful heat transfer. A better question might be: Why can a system designed around a smaller charge often be more efficient than one designed around a larger charge?

    Edward Young Retired

    After you make that expensive repair and you still have the same problem, What will you check next?

    GGrossChrisJ
  • EdTheHeaterMan
    EdTheHeaterMan Member Posts: 12,517

    @ChrisJ asked "Why do some refrigerants require less of a charge I.E. R134A vs R12 in a retrofitted system, or R152A in a R134A system. Why does the system suddenly need less liquid in areas? Does the liquid weigh less, so it's technically the same volume but less weight? Or is there something else going on?"

    Yes the refrigerant is less dense, for example: In many R-12 automotive retrofits, the recommended R-134a charge was often roughly 80–90% of the original R-12 charge by weight.

    A major reason is that R-134a liquid is less dense than R-12 liquid at typical A/C conditions. So if the condenser, liquid line, and evaporator contain roughly the same liquid volume, the R-134a charge will weigh less.

    R-152a is even more dramatic. It has a much lower molecular weight and lower liquid density than R-134a. R-134a has a molar mass of about 102 g/mol, while R-152a is about 66 g/mol. CoolProp’s R-134a data page lists R-134a’s molar mass as 0.102032 kg/mol.

    That does not mean you use exactly 66/102 of the charge, because charge is not based only on molecular weight. But it helps explain why the required weight can drop a lot.

    With R-152a, you may need enough refrigerant volume to wet the evaporator, maintain a liquid seal to the metering device, and establish proper subcooling, but that same volume weighs much less.

    But that is not the only factor…. there is much more going on, however the difference in density is a big reason.

    Edward Young Retired

    After you make that expensive repair and you still have the same problem, What will you check next?

    ChrisJ
  • ChrisJ
    ChrisJ Member Posts: 17,534

    Actually,

    I guess I'm wrong because the biggest way you improve efficiency appears to be larger condensers and evaporators. A larger condenser probably doesn't hold much more, but the evaporator must.

    avpsun.jpg

    Single pipe 392sqft system with an EG-40 rated for 325sqft and it's silent and balanced at all times.

  • mattmia2
    mattmia2 Member Posts: 17,528

    The condenser i have is the most efficient system Lennox had in 2001 without going to 2 stage and it is the size of a small porch. All the parts are scaled up so it doesn't look big but it is huge for a 2.5 ton condenser.

  • ChrisJ
    ChrisJ Member Posts: 17,534

    Single pipe 392sqft system with an EG-40 rated for 325sqft and it's silent and balanced at all times.

  • EBEBRATT-Ed
    EBEBRATT-Ed Member Posts: 20,525

    I don't claim to be smart enough to comment but I will anyhow.

    One reason for limiting the amount of charge in a system (in the old days at least) was to minimize the amount of liquid refrigerant in the system. They talked about this in many of the older books including Copelands

    By limiting the charge it reduced or prevented liquid getting back to the compressor, slugging and liquid migration are reduced preventing compressor damage.

    I too wonder about the pressures required with different refrigerants.

    Some like R-12 run at lower pressures than like 410A whose suction pressure (for AC systems) is probably higher than R-12s discharge pressures.

    Common sense you would think R-12 with lower pressures would require lower HP compressors than a 410A unit but

    That just shows I don't know what I am talking about.

    Line set sizes between refrigerants doesn't seem to change all that much in spite of the higher pressures.

    I always refer to my old Copeland books for stuff like this. The density of the refrigerant as @EdTheHeaterMan mention is part of the discussion and section 1 & 2 in this book go into detail

    ChrisJmattmia2
  • GGross
    GGross Member Posts: 1,982

    I think the larger units we see are mostly due to less than perfect engineering. we had older 18 SEER units that felt like they were twice the size of the current 20 SEER2 units. (not really but they were bigger overall) at our most recent roundtable with a manufacturer they even discussed this directly, that manufacturing the newer A2L units had been progressing and we would see smaller units shipping out at some point. You also have to remember that if you are comparing ratings from today with older units the numbers are not exact, if you see a 13 on todays equipment that means SEER2 which is different from SEER..

    back to the original point, somewhat offtopic but related… Personally I think the most important aspect of lower refrigerant charges in the current age has to do with the rating of the refrigerant. You can build an R290 mono bloc A2WHP with such a tiny amount in it that there is virtually no risk of fire if it leaks. IMO systems like this where you have self contained miniscule refrigerant charges located outside and only hot/chilled water flowing through the house will gain traction over time, or maybe just wishful thinking…

    Here in the US using an A2L if you can keep total system charge below i think 4lbs the RDS that everyone is freaking out about is no longer required.

    ChrisJ
  • ChrisJ
    ChrisJ Member Posts: 17,534

    I think that was very much on topic.

    I know what I asked had a lot of stuff I don't know about, and you made a good point, just like freezers etc using butane.

    For efficiency, I try to look at EER ratings. When I match up a split I usually aim for the highest EER combination and just ignore SEER. That may be a mistake on my part, but I look at it as I want the most effieincy during long run cycles. I think my 2 stage 16 SEER system from 2017 it had an EER of 12, or 12.something in the configuration I did.

    Single pipe 392sqft system with an EG-40 rated for 325sqft and it's silent and balanced at all times.

    GGross
  • Jamie Hall
    Jamie Hall Member Posts: 27,596

    I can't comment on much of this — except the relationship between temperature and pressure. Any mechanical heat transfer system — heat pump, air conditioner, chiller, refrigerator, whatever — works on the same principle. Some refrigerant is evaporated at a low temperature and pressure. This absorbs heat energy from the surroundings. It is then compressed and allowed to condense at some higher temperature. This releases heat to the surroundings.

    Those two pairings of temperature and pressure are controlled by the choice of refrigerant, and different compounds will have different pairings. The amount of power required to raise the pressure is a function only of the pressure differential in question and the volume of gas — choice of refrigerant is relevant only to the extent that it affects the pressure differential required.

    Hope this helps…

    Br. Jamie, osb
    Building superintendent/caretaker, 7200 sq. ft. historic house museum with dependencies in New England
  • mattmia2
    mattmia2 Member Posts: 17,528

    I don't remember, i'd have to look, I think it is somewhere in the ballpark of 10/12.

    remember the compressor is working against the differential, not the gauge pressure although power is a function of volume and pressure so refrigerants with a higher pressure differential are moving less volume at that higher pressure.

  • ChrisJ
    ChrisJ Member Posts: 17,534

    Does anyone know how the Latent Heat of Evaporation of different refrigerants effects things?


    From what I recall, methyl formate and sulfur dioxide seemed to have insanely high amounts of Latent Heat of Evaporation, but it didn't seem like that really related to efficiency, or power of a system. I think ammonia had the highest by far, if I'm remembering right.

    Single pipe 392sqft system with an EG-40 rated for 325sqft and it's silent and balanced at all times.

  • Jamie Hall
    Jamie Hall Member Posts: 27,596

    The latent heat of vapourization does affect things — it determines how much refrigerant you need to compress to transfer a certain amount of heat. Higher values would mean less mass of refrigerant (NOT VOLUME) for a given amount of heat.

    There's another complication, though — the energy put into the fluid by compression also counts, though it's relatively small — except at the extremes of performance. It is one of the factors involved in the lower efficiency of heat pumps at low source temperatures, though.

    Incidentally, water os one of the best refrigerants. Just plain water. Inconveniently, though it freezes at much too high a temperature to be useful in most mechanical applications. It's very high heat of vapourization, though, is what makes steam heat such a wonderful thing…

    Br. Jamie, osb
    Building superintendent/caretaker, 7200 sq. ft. historic house museum with dependencies in New England