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High Efficient Heat Reclaim with CO2

20 June 2010 | Author: Kenneth Bank Madsen, Application Manager, Danfoss A/S
Refrigeration systems with transcritical CO2 has been taking market shares the last years. Since 2007 the market in Denmark has turned from conventional refrigeration systems with HFC or cascade systems with CO2 and HFC towards transcritical CO2 systems. At this moment transcritical systems is everyday business and the technology is mature. The field studies carried out looking at refrigeration only shows that the annual energy consumption is on the same level as HFC DX systems. The article contains a short back ground on the theory behind heat reclaim in transcritical systems, and the efficiency will be compared with the efficiency of HFC systems.
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Chapter 1. High efficient heat reclaim with CO2
Refrigeration systems with transcritical CO2 has been taking market shares the last years. Since 2007 the market in Denmark has turned from conventional refrigeration systems with HFC or cascade systems with CO2 and HFC towards transcritical CO2 systems. At this moment transcritical systems is everyday business and the technology is mature. The field studies carried out looking at refrigeration only shows that the annual energy consumption is on the same level as HFC DX systems. The article contains a short back ground on the theory behind heat reclaim in transcritical systems, and the efficiency will be compared with the efficiency of HFC systems.

Transcritical systems back ground

In normal systems with condensing refrigerants the pressure and temperature are tied together, but on transcritical systems pressure and temperature can be controlled individually. This gives some possibilities regarding heat reclaim.

During normal operation with out heat reclaim the high pressure is kept at a level where the optimum COP is obtained. This is done automatically by an electronic controller. During cold periods the pressure in normally kept at minimum 40 bar ~ 5 ºC or higher. At this pressure there is almost no heat to reclaim. If the pressure is raised the amount of heat that can be reclaimed is increasing.

Example

Water is heated from 15 ºC to 55 ºC. The ambient temperature is -5 ºC and the heat load on the system needs to be reclaimed with the lowest possible energy consumption. The temperature difference of the heat reclaim HX is set to 5 K at in or outlet. The temperature out of the gas cooler is kept at 4 ºC in all cases where the gas cooler is active.

The system used consists of one or more compressors, heat reclaim heat exchanger with pump, two 3-way valves, air cooled gas cooler and a high pressure control valve with electronic controller.





Under these conditions the discharge temperature from the compressors is approx 35 ºC and therefore it is not possible to make 55 ºC hot water. To make the system able to do 55 ºC the discharge needs to be at least 55 ºC and therefore the pressure needs to be pushed upwards.



At 50 bar high pressure the discharge temperature is 55 ºC and therefore it is possible to start reclaiming heat from the system but there is no temperature difference of the heat exchanger. By increasing the pressure further the amount of heat taken out of the system is increasing.



At 80 bar approx 80 % of the heat is reclaimed at a cooling COP of 3,13. To increase the ratio to more than 80 % the pressure can be pushed up and the gas cooler can be by passed. By doing this the ratio will go to 100% because there is no heat lost to the ambient, but all heat is reclaimed. This will put in more compressors to compensate for the lower heat rejection.



Under this conditions all heat is reclaimed and the COP of the system is approx 2,6.

Since the heat output from the system varies with the pressure it is interesting to look at what the heating COP of the system is. The system consumes energy in the condition there it is running with optimised pressure (in this example 40 bar). This means that no mater how much heat we pull out of the system it will consume energy. Therefore the heating COP of the system is calculated at the heating capacity divided with the extra energy consumed by the compressors. This is done because then it is possible to compare the heating COP with alternative heating sources.

P_gc [bar] COP ref [-] Ratio COP Heat [-]
40 8,8 0% -
50     5,7 0% -
60 4,3 25% 2,6
70 3,6 40% 3,1
80 3,1 80% 5,1
80 3,1 100%* 5,1
*By-pass of air cooled gas cooler

The ratio is the ratio between the maximum heat available and the heat used.

The heating COP is varying with the ambient temperature. At high ambient temperatures the compressor work used for refrigeration is higher and therefore the compressor work for heating is less. At lower ambient temperatures the pressure can not be decreased, and therefore this will not effect the heating COP. If the ambient temperature was chosen to be 3 ºC instead of -5 ºC then the result will be a shown in the table below.

P_gc [bar] COP ref [-] Ratio COP Heat [-]
50 5,7 0% -
60 4,3 25% 5,6
70 3,6 40% 5,0
80 3,1 80% 7,3
80 3,1 100%* 7,3
*By-pass of air cooled gas cooler

The results show that the ambient temperature has a significant impact on the heating COP and the heating COP is highest at full load. If the high COP is wanted at part load the system can be build as a CO2 heat pump on top of the refrigeration system.
Chapter 2. Comparing CO2  transcritical with other heat sources
In the section above the heating COP is calculated, but the interesting part is if it is cheaper or more expensive compared to other heat reclaim systems and other energy sources.

Other heat reclaim systems

To be able to compare the COP from CO2 to the COP of other refrigerants it has to be done in a fair way. For the other refrigerants it is chosen to run at -10 °C evaporation and to condense at 55 °C to be able to supply 55 °C hot water. Sub cooling is set to 2K. The minimum condensing temperature is set to 15 °C.



From the chart above it can be seen that the heating COP for CO2 is from approx 25 % to 150 % better that R134A and best at part load witch is the main part of the year.

Heat pump systems

To get around the problem with part load a heat pump can be put on top of the system. This makes the COP of the system as good as possible regardless of the load on the system.

The COP in heating mode has been calculated at 5 °C evaporating (equivalent to the lowest possible condensing for the transcritical CO2 system) , 55 °C condensing and 2 K sub cooling. The calculation has been done for most of the most used refrigerants on the market.

Refrigerant COP heating
R134A 3,7
R290 3,7
R404A 3,3
R410A 3,4
CO2 transcritical heat pump 5,1

The table above shows the COP for different refrigerants. From the data it shows that CO2 has a COP that is from 38 % to 55 % higher that the conventional refrigerants.

Other energy sources

An alternative to a CO2 heat reclaim system could be an oil or gas burner. The question is what is the most economical choice? The COP calculated in this example for a CO2 heat reclaim system is between 2,6 and 7,3. The exact COP is a question of what type of systems it is (Heat pump or heat reclaim), the load profile for the heat reclaim and the ambient temperature. This can be matched with other energy sources with the following equation.



If this ratio is smaller than 1 then the CO2 solution is the most economical solution. In most cases a heat reclaim or heat pump solution is economical attractive. In many cases a heat reclaim solution is attractive if the COP is higher that 2 or 3, but this of cause depends of the energy prices and local taxes.
Chapter 3. Conclusion
The example above shows
  • Heating COP in a transcritical heat reclaim system from 2,6 to 7,3 depending on load and ambient temperature.
  • CO2 is from 25% to 150% better than R134A in a heat reclaim system depending on the load.
  • In a heat pump system CO2 is from 38% to 55% better than the HFC refrigerants compared with.
  • The COP in a heat pump system is higher than a heat reclaim system at part load, but at full load the difference is very little. If it is feasible to install a heat pump system relays on the load profile and the investment costs.
  • Very often CO2 heat pumps or heat reclaim systems are a very attractive alternative to a oil or gas burner

The conclusion is made on the data in the example. If the data are different the conclusion will be different, but there are some guide lines.

  • CO2 is feasible at high temperature lifts. The lower temperature the inlet water or media the better efficiency CO2 will have. The exit temperature is not that important. Up to 80°C is realistic with good efficiency
  • CO2 is not the refrigerant to chose if the outlet media temperature is low and the temperature difference between inlet and outlet is low.

There are systems in operation from 5 kW to 1,5 MW heat reclaim at this moment. There are more than 500 installations world wide with transcritical CO2, not all with heat reclaim. This is not rocket science but everyday business!

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