Bolt wrote:If I understand correctly, the water from a well of T ° 12 ° C drops by 5 ° C in the evaporator by supplying it with its calories
ditto for air (from -15 ° C to -10 ° C) (in winter when it is most needed) and therefore the difference in yield depends mainly on the T ° available in the sampling medium
Reversible or non-reversible refrigeration systems use 2 exchangers:
1 "hot" exchanger called condenser which serves to condense the fluid and evacuate the "calories" of condensation of this fluid
1 "cold" exchanger called evaporator which serves to evaporate the fluid and absorb the "calories" of evaporation of this fluid
The compressor and the expansion valve are used to compress and expand the fluid to suitable pressures and temperatures; we chose a refrigerant according to its characteristics
So-called Mollier diagram
See this well done site:
http://www.cooling-masters.com/articles-4-0.htmlhttp://www.univ-nancy2.fr/Amphis/images ... r%20pdf%22for the brave
http://www-ipst.u-strasbg.fr/jld/machth.htmhttp://pastel.paristech.org/bib/archive ... %20R410%22The more the temperature of the medium (air or water) used to capture the "calories" of the evaporation of the fluid is close to the evaporation limits of this fluid at atmospheric pressure, the less the performance is good;
For example the R134 must have an evaporation pressure of -25 ° C at atmospheric pressure, it can be used for cold rooms at T ° 0 ° C, the fluid will work at an evaporation temperature of -10 ° C
Just as the condensation temperatures at the top of the Mollier diagram (sorry, we still cannot insert a file) from 50 to 70 ° C also make the yield drop, because the energy used for compression is greater.
If we take the extremes:
inlet 7 ° C outlet 28 ° C (difference: 21 ° C) = good COP
inlet -15 ° C outlet 50 ° C (difference: 65 ° C) = poor COP (65 ° C is this possible first?)
You understood everything, the relation PxV / T ° being constant, the less there is delta between the temperatures of evaporation and condensation, the less there is effort to provide for the compression of the fluid and the better the yield .
There are so-called high temperature heat pumps, but the efficiency is affected.
The ideal is indeed to use a heat pump on a floor heating at 28 ° C max
with a sun supplement.
But often the COP of PACs with water withdrawal does not take into account the kw which are used to convey water to the PAC
ex: PAC consumes 2 kw, returns 10 kw = COP of 5
if the water pump consumes 1 kW the real result gives:
10 kw divided by (2 + 1) = COP of 3,33
Well yes, the more energy consuming equipment, the lower the efficiency,
a 1KW pump is still tough, unless you pump very deep
Capt_Maloche wrote:at + 7 ° C it is common to find COPs of 5 !! with R410
a little less with R407
What are the differences between R134a; R407 and R410
The T ° of evaporation at atmospheric pressure are different
-25 ° C for 134A
-45 ° C for R407
-52 ° C for R410
With a probe system in a borehole without water withdrawal (advantageous by the compression of the pumping of this water) can have the same problem as a network buried at 0,80 m (freezing a whole mass of underground land to lapse a heat pump) (problem necessarily absent by water withdrawal)
bolt
yes, it all depends on the nature of the earth and the exchange surface
I hope I have informed you
Hello