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Air handling in combination with evaporative
cooling using water (R718) as a refrigerant is an answer to the F-gas- and
CO2-policy. However, there is a lot of misunderstanding regarding the various
types of evaporative cooling, like Direct or Indirect, Adiabatic or Diabatic, and
Wet bulb or Dew-point cooling. They all discharge only the sensible heat. In
general, evaporative cooling brings down the energy consumption for air
conditioning systems by between 70% and 85%, and COP‘s above 20 are no
exception. Besides the need for a very low energy consumption, there is now an
increasing demand for the system to operate with low water consumption. Legionella
and corrosion must also be points of attention.
·
The
choice: direct/ indirect.
·
Adiabatic
(wet bulb cooling) or diabatic (dew-point cooling).
·
Evaporating
water as refrigerant:
-
(potable) mains water (should be
minimized as much as possible);
-
spring water;
-
salt (sea)water.
·
Water
distribution:
-
gravity without a pump;
-
(re)circulation with a pump;
-
sprinkle (nozzles);
-
absorption.
·
Free
from Legionella, bacteria and algae:
-
with
or without water treatment?
-
descaling
-
demi-water
-
surface tension
·
Materials:
-
not be susceptible to corrosion.
-
preferably the use of synthetic
materials.
Linguistically
the word Adiabatic means Non-Diabatic.
During an
adiabatic process, the heat itself is taken from the air and not supplied or
taken via the cooler surface (in a Mollier diagram this process is drawn with
lines of constant enthalpy = h). Theoretically the lowest temperature that can
be achieved is the wet bulb temperature, hence the use of the term Wet Bulb
Cooling.
During a
diabatic process however, there is an exchange of heat between cooler surface
and air. In this case the lowest temperature theoretically possible is the
dew-point temperature, hence the use of the term Dew-point Cooling. (in Figure
1 (Mollier diagram) this process is drawn with lines of constant
absolute moisture = gr/kg)
Figure 1. Mollier
diagram: wet bulb cooling (adiabatic), compared to dew-point cooling (diabatic).
Example:
Temperature | 28°C |
Absolute humidity | 11.9 g/kg |
RH | 50 % |
Dew-point (blue) | 16.6°C |
Wet bulb temperature (red) | 19.4°C |
Difference | 19.4°C – 16.6°C = 2.8°K |
this will differ from case to case. |
If the
temperature of the sucked-in ambient air is higher, this causes a higher wet
bulb temperature and so a higher outgoing temperature. This is in contrast with
the dew-point temperature, which will not change if the temperature rises.
Minimum
temperature achievable is a few degrees K (Kelvin) above the wet bulb
temperature.
Direct adiabatic
cooling makes use of a wetted absorbent, an air filter and fan. The air to be
cooled is blown through the absorbent, evaporating a part of the water. The
energy needed for evaporation is directly withdrawn from the air by cooling it.
The discharge temperature depends on the temperature and relative humidity of
the air entering the process. These systems mostly use a water circulation pump
and means to prevent legionella and bacteria growth.
·
These
coolers add moisture to the air entering the cooled room, resulting in both a lower room
temperature and also an increasing relative humidity (%RH).
Note the contrasting effect: A lower temperature will be more
comfortable, but a higher RH will be experienced as uncomfortable. The latter is
especially the case when we are dealing with gyms, workshops or other places
where physical exertion is taking place, as it is more difficult to perspire in
a high RH environment.
·
Direct
cooling also might give problems to stored goods and electronics. It is therefore mostly used in dry
(desert) climates or in moderate climates only for industrial purposes.
·
The
minimum discharge temperature of cooled air is a couple of degrees Kelvin above
the wet bulb temperature.
However, if during the daytime the ambient temperatures rises because of the
sun and the absolute humidity (gr/kg) remains the same, the wet bulb
temperature will also rise, resulting in a higher outgoing (cooled) air
temperature.
·
The
vaporized water as a result of the cooling process, will be discharged to the
ambient and will not influence the % RH in the room to be cooled.
·
Indirect
systems are available either as wet bulb cooling or as dew-point cooling each
with its own characteristics.
·
The
minimum discharge temperature is a couple of degrees K above the wet bulb
temperature.
Another outcome, if the ambient temperatures rises during the day, is that the
wet bulb temperature will rise, resulting in a higher outgoing (cooled) air
temperature.
·
The
minimum discharge temperature is a couple of degrees Kelvin above the dew-point
temperature.
·
Comparted
with wet bulb cooling, and depending on the temperature and humidity, both the dew-point temperature and cooled
air temperature will be between 2 K and 4 K lower.
·
If
during the daytime the ambient temperature rises, and at the same time the
absolute humidity (gr/kg) remains the same, the wet bulb temperature will stay
the same and consequently the outgoing (cooled) air temperature will not change.
It will, in fact, stay almost the same for the whole day.
Inert cooling
is a new development based on dew-point cooling, an extreme low energy
consumption, and suitable to operate in an aggressive polluted ambient with
almost any quality of evaporating water. A couple units are now in operation.
This type
of dew-point cooling uses
only one fan for both the primary air and the process air, resulting in a
minimum of moving parts. The outside of the heat exchange plates is covered with
a wetted hygroscopic foil.
At the end
of the heat exchanger, 33% of the cooled air leaving the cooler becomes process
air. This is caused by turning the air 180° and returning it in counter flow
along the outside of the heat exchanger plates by using the available extern
pressure drop (in ducts and grilles of the building to be cooled) as the driving
force. Due to this turning process and a forced air flow (no suction), a
centrifugal force is developed and, as a consequence, dirt particles will not
be taken into the process air stream. As the dirt particles aren’t able to
contaminate the cooler surface, there is no pollution and less maintenance
costs. Cooling is a natural process existing of a water supply by the
combination of falling film, adhesion (foil to plate) and hygroscopic operation
of vapor. The amount of
heat (kJ) taken from the primary air is equal to the amount of kJ necessary for
evaporation of the moisture. The process air discharges the evaporated moisture
towards the open air and cannot enter the conditioned room (Figure 2).
Figure 2. Principle layout of the dew-point
cooler.
It is a commonly
acknowledged that air can be aggressive in combination with moisture in coastal
areas, swimming pools, cattle and poultry, near chemical plants, etc. The use
of demineralised water, with NH4+, or salt can also cause corrosion
problems. This explains why inert cooling systems are entirely made of
synthetic materials.
The use of fresh
water can be a problem in certain areas and has to be limited as far as
possible, but salt (sea)water is always largely available. The system was successful
when tested using sea water for a 6-month period. The use of saltwater is only
possible if the whole unit (housing and cooling surface) is made of synthetic
material. It is possible to prevent salt crystals by using indirect dew-point cooling
with absorption wetting and combined with an overflow of seawater, instead of
with nozzles.
In general,
the water consumption depends first of all on the amount of air to be cooled,
the temperature and humidity of the admitted air. Besides that, also the system
as well as the way of wetting has influence. Based on evaporating, the water
supply temperature has practically zero influence on the cooling capacity.
·
Constant
pump recirculation in combination with a water container
·
Without
a (re)circulation pump, so using the pressure of mains water supply.
·
The
use of nozzles for the water distribution.
Disadvantage: nozzles can -depending on the water quality- clog, so requires
maintenance.
·
The
water supply can be controlled by periodical opening and closing a solenoid
valve in the water supply.
Using Inert
cooling:
·
A
new development water supply is based on absorption, without pump circulation
and without the use of nozzles, using the mains water pressure.
It takes care of a very constant water flow, with little waste of water and
brings down the water surface tension (patent pending).
·
Inert
cooling is also suitable for evaporating salt (sea)water
·
The
cooled air keeps the same absolute humidity during the whole cooling process
without any condensation, so stays dry.
·
The
humidified process air is discharged towards the outside ambient and due to the use of a wetted hygroscopic foil on the
process plate surface, as well as a low process air velocity (< 2 m/s),
no aerosols will be formed.
·
Growth
of algae will not occur, because the cooler operates without re-used water
circulation, has no water collector and the hygroscopic layers are
automatically dried once a day and as soon as the cooling stops.
The test data below was recorded last year
(2015) in a sports hall, situated close in the seacoast and a blast furnace, so
a polluted area, using absorption water supply, so without nozzles.
Air flow | 4 500 m³/h |
Dry bulb | 22.0 °C |
Wet bulb | 16.0 °C |
% Humidity | 54.0 % |
Dew point | 12.3 °C |
Abs. moisture | 8.9 gram/kg |
Air flow | 1 485 m³/h |
V = 33 % process air leaving | 96% to 98% |
Air flow | 3 015 m³/h |
Dew point | 12.3 °C |
Abs. moisture | 8.9 gram/kg |
V cold = cooled air leaving at: | 14.3 °C |
·
According to a simulation program
which is based on using water supply by nozzles, the cooled air should be 16.2 °C, however the
now reached temperature is 14.3°C
·
16.2 – 14.3 = 1.9 K lower than
according to the simulation program (in this case 33% increase and average
25%). Reason: an optimal and constant water distribution compared with the use
of nozzles.
·
In this case: 1.7 K below the wet
bulb temperature (16 – 14.3) and 2 K above dew-point (14.3 – 12.3).
Uges,
P.G.H., 2006; Air
conditioning using R718 (water) as refrigerant, 7th IIR Gustav
Lorentzen Conference on Natural Working Fluids, Trondheim, Norway.
Ree,
prof Ir. H. v.d., 2009; Evaporative cooling of indoor air supply innovated,
RCC-K&L 102 (6) 23-2
Uges, P.G.H., 2010; A closer look at evaporative
adiabatic wet bulb cooling and diabatic dew-point cooling, using water (R718)
as refrigerant. 9th IIR Gustav
Lorentzen Conference on natural refrigerants, Sydney, Australia.
Janssen,
ir M., and Uges P.G.H., 2010; Parameters affecting the performance of a
dew-point cooler, consisting of a counter flow heat exchanger using water as
refrigerant. 9th IIR Gustav Lorentzen Conference on natural refrigerants,
Sydney, Australia.
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