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REFRIGERATION AND HEAT PUMP
      SYSTEMS WITH CO2
      AS A REFRIGERANT

               S. Girotto
              Enex S.r.l., Italy
        sergio.girotto@enex-ref.com
INDEX
WHY NATURAL REFRIGERANT CO2

ENVIRONMENTAL IMPACT OF CO2 / R404A
EXAMPLE – TYPICAL “COLD CLIMATE”

INVESTMENT & OPERATING COST

EFFICIENCY

FLASH VAPOR RECOMPRESSION

COMMERCIALLY AVAILABLE REFRIGERATION SYSTEMS

HEAT PUMPS FOR HOT WATER
WHY NATURAL REFRIGERANT CO2

Zero ODP / Zero GWP

Non toxic / Non flammable

No further changes of refrigerant in future (with synthetic refrigerants
: R12, R502, R22 -> R404A/R507, R134a + tens of blends ->
HF1234yf -> ?? what comes after?)

CO2 is largely available all over the world as a by-product, low cost

No subject to legislation constraints (F-Gas Directive in EC)
ENVIRONMENTAL IMPACT OF CO2 / R404A
 EXAMPLE – TYPICAL “COLD CLIMATE”
INVESTMENT & OPERATING COST (1)
For a refrigeration system of one supermarket energy cost during lifetime is
85% of the total running cost


Due to above investment running cost must be considered together


Comparison between a DX-CO2 and a conventional HFC system cost splitting
for a reference system 100 kW MT / 30kW LT

                       80000
                       70000
                       60000                        refrigerant
                       50000                        pipi ng/ins.
                      € 40000                       condenser
                       30000
                                                    elec.panel
                       20000
                                                    compr.unit
                       10000
                            0
                                CO2   HFC R404A
INVESTMENT & OPERATING COST (2)

In a proper economical analysis other factors must be considered:
a) cost for refilling of refrigerant during the lifetime of the system
b) cost for inspections due to leak emission control (F-GAS Directive)
c) unforeaseeable cost increase and unavailable of synthetic refrigerant
d) disposal cost
EFFICIENCY (1)

CO2 itself is not “more efficient” or “less efficient” than other fluids.


Efficiency theoretically does not depend on the fluid used (Carnot’s law) but
from the combination of plant design and refrigerant.


Guideline should be: for a given refrigerant (operating fluid) to improve as
much as possible the design of the system so as to obtain maximum
performance.


Compared with other refrigerants CO2 has a lower critical temperature, which
might require a modified cycle for some applications.
EFFICIENCY (2)
A simple comparison with HFC solution cannot enhance differences due to better
heat transfer characteristics or lower influence of pressure drop on efficiency


Efficient CO2 – only systems use one or more of the following:
1) maximum heat recovery
2) extremely low condensing pressure in winter time when no Heat Recovery is
required
3) LPR design – standard solution for some heat pumps and single compressor units
4) recompression of flash vapor in warm ambient conditions
(air cooled systems)


Not – in – kind solutions (like expander, ejector) do exist, but they are still under
evaluation and/or laboratory test
FLASH VAPOR RECOMPRESSION (1)
FLASH VAPOR RECOMPRESSION (2)
                           SIMULATION FOR BARCELLONA CLIMATE

                               Temperature profile July                                              Temperature profile September
                      40                                                                    40
Te m pe rature [°C]




                                                                        Tem perature [°C]
                      30                                                                    30
                                                            average
                      20
                                                                                            20
                                                            max_daily                                                                average
                      10
                                                                                            10
                       0
                                                                                             0
                           0    5     10          15   20
                                                                                                 0        5    10          15   20
                                           hour
                                                                                                                    hour
FLASH VAPOR RECOMPRESSION (3)
      Temperature profile July average
FLASH VAPOR RECOMPRESSION (4)
      Temperature profile July max_daily
FLASH VAPOR RECOMPRESSION (5)
     Temperature profile September average
COMMERCIALLY AVAILABLE REFRIGERATION SYSTEMS - 1
   “New” CO2 systems are on the market since 2006, after a long development
   started in late ‘90s (first CO2 only installation : 1999 – Italy /first CO2–only
   multi-compressor rack : 2001 - Italy)
   Now there are standardized and proven design concepts

   Example : booster system
             for supermarkets




   CO2 as a refrigerant was used in early 20th century (until ’50s) but the
   application was completely different, so a complete re-invention of
   technology was necessary.
COMMERCIALLY AVAILABLE REFRIGERATION SYSTEMS - 2

  Other concepts using only CO2 as a refrigerant are well proven and
  available on the market:

  -Single stage, with a capacity up to 300 kW at -10° eva poration for large
                                                    C
  cold rooms, hypermarkets, water and brine chilling

  -2-stage internal compound up to 100 kW at -35°C evaporation for deep
  freezing (cold rooms, hypermarkets)

  - Cascade for LT (supermarkets, freezing tunnels,…)
COMMERCIALLY AVAILABLE REFRIGERATION SYSTEMS - 3
COMMERCIALLY AVAILABLE REFRIGERATION SYSTEMS - 4
COMMERCIALLY AVAILABLE REFRIGERATION SYSTEMS - 5
HEAT PUMPS FOR HOT WATER
For one specific applications CO2 transcritical concept has no rivals : sanitary
water heat pumps.

The gliding temperature for an isobaric/non-isothermal heat rejection reduces
thermodynamic losses bringing performances at a level that cannot be reached
with any other existing commercial solution :
- Water heating in one pass from 10° up to 90°
                                    C           C
-COP higher than 4,0 for air-source heat pump with air 7°
                                                        C-50% R.H. and water
in-out 10-65°C
HEAT PUMPS – FOR HOT WATER
                     AIR HEAT 25




Best applications:
- Hotels
- Hospitals
- Laundries – Elderly people houses
- Wheneven hot water is needed in large amounts
Many thanks for your attention

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Refrigeration systems & heat pumps with co2

  • 1. REFRIGERATION AND HEAT PUMP SYSTEMS WITH CO2 AS A REFRIGERANT S. Girotto Enex S.r.l., Italy sergio.girotto@enex-ref.com
  • 2. INDEX WHY NATURAL REFRIGERANT CO2 ENVIRONMENTAL IMPACT OF CO2 / R404A EXAMPLE – TYPICAL “COLD CLIMATE” INVESTMENT & OPERATING COST EFFICIENCY FLASH VAPOR RECOMPRESSION COMMERCIALLY AVAILABLE REFRIGERATION SYSTEMS HEAT PUMPS FOR HOT WATER
  • 3. WHY NATURAL REFRIGERANT CO2 Zero ODP / Zero GWP Non toxic / Non flammable No further changes of refrigerant in future (with synthetic refrigerants : R12, R502, R22 -> R404A/R507, R134a + tens of blends -> HF1234yf -> ?? what comes after?) CO2 is largely available all over the world as a by-product, low cost No subject to legislation constraints (F-Gas Directive in EC)
  • 4. ENVIRONMENTAL IMPACT OF CO2 / R404A EXAMPLE – TYPICAL “COLD CLIMATE”
  • 5. INVESTMENT & OPERATING COST (1) For a refrigeration system of one supermarket energy cost during lifetime is 85% of the total running cost Due to above investment running cost must be considered together Comparison between a DX-CO2 and a conventional HFC system cost splitting for a reference system 100 kW MT / 30kW LT 80000 70000 60000 refrigerant 50000 pipi ng/ins. € 40000 condenser 30000 elec.panel 20000 compr.unit 10000 0 CO2 HFC R404A
  • 6. INVESTMENT & OPERATING COST (2) In a proper economical analysis other factors must be considered: a) cost for refilling of refrigerant during the lifetime of the system b) cost for inspections due to leak emission control (F-GAS Directive) c) unforeaseeable cost increase and unavailable of synthetic refrigerant d) disposal cost
  • 7. EFFICIENCY (1) CO2 itself is not “more efficient” or “less efficient” than other fluids. Efficiency theoretically does not depend on the fluid used (Carnot’s law) but from the combination of plant design and refrigerant. Guideline should be: for a given refrigerant (operating fluid) to improve as much as possible the design of the system so as to obtain maximum performance. Compared with other refrigerants CO2 has a lower critical temperature, which might require a modified cycle for some applications.
  • 8. EFFICIENCY (2) A simple comparison with HFC solution cannot enhance differences due to better heat transfer characteristics or lower influence of pressure drop on efficiency Efficient CO2 – only systems use one or more of the following: 1) maximum heat recovery 2) extremely low condensing pressure in winter time when no Heat Recovery is required 3) LPR design – standard solution for some heat pumps and single compressor units 4) recompression of flash vapor in warm ambient conditions (air cooled systems) Not – in – kind solutions (like expander, ejector) do exist, but they are still under evaluation and/or laboratory test
  • 10. FLASH VAPOR RECOMPRESSION (2) SIMULATION FOR BARCELLONA CLIMATE Temperature profile July Temperature profile September 40 40 Te m pe rature [°C] Tem perature [°C] 30 30 average 20 20 max_daily average 10 10 0 0 0 5 10 15 20 0 5 10 15 20 hour hour
  • 11. FLASH VAPOR RECOMPRESSION (3) Temperature profile July average
  • 12. FLASH VAPOR RECOMPRESSION (4) Temperature profile July max_daily
  • 13. FLASH VAPOR RECOMPRESSION (5) Temperature profile September average
  • 14. COMMERCIALLY AVAILABLE REFRIGERATION SYSTEMS - 1 “New” CO2 systems are on the market since 2006, after a long development started in late ‘90s (first CO2 only installation : 1999 – Italy /first CO2–only multi-compressor rack : 2001 - Italy) Now there are standardized and proven design concepts Example : booster system for supermarkets CO2 as a refrigerant was used in early 20th century (until ’50s) but the application was completely different, so a complete re-invention of technology was necessary.
  • 15. COMMERCIALLY AVAILABLE REFRIGERATION SYSTEMS - 2 Other concepts using only CO2 as a refrigerant are well proven and available on the market: -Single stage, with a capacity up to 300 kW at -10° eva poration for large C cold rooms, hypermarkets, water and brine chilling -2-stage internal compound up to 100 kW at -35°C evaporation for deep freezing (cold rooms, hypermarkets) - Cascade for LT (supermarkets, freezing tunnels,…)
  • 19. HEAT PUMPS FOR HOT WATER For one specific applications CO2 transcritical concept has no rivals : sanitary water heat pumps. The gliding temperature for an isobaric/non-isothermal heat rejection reduces thermodynamic losses bringing performances at a level that cannot be reached with any other existing commercial solution : - Water heating in one pass from 10° up to 90° C C -COP higher than 4,0 for air-source heat pump with air 7° C-50% R.H. and water in-out 10-65°C
  • 20. HEAT PUMPS – FOR HOT WATER AIR HEAT 25 Best applications: - Hotels - Hospitals - Laundries – Elderly people houses - Wheneven hot water is needed in large amounts
  • 21. Many thanks for your attention