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ROUNDTABLE ON CLIMATE & OZONE-FRIENDLY TECHNOLOGIES          Belgrade, May 10, 2011




                                    Franc Kosi, P.E.

                 The Society for Air-Conditioning, Heating and
                              Refrigeration (KGH)
                               Belgrade, Serbia



                                    CASE STUDY:

                     A NEW REFRIGERATION PLANT
                       BASED ON AMMONIA WITH
                      SECONDARY FLUIDS LOOPS



                                                                                      1
ROUNDTABLE ON CLIMATE & OZONE-FRIENDLY TECHNOLOGIES                     Belgrade, May 10, 2011




    DESCRIPTION OF ASSIGNMENT

    To design refrigeration system for an meat industry factory , capacity of about
    7.000 chicken per hour (or 105.000 a day).

    The product are frozen meat pieces, boiled and dried sausages and ham
    product.

    The total refrigerated area (two levels) is approximately of 21.250 m2; it
    comprises 49 cold rooms and production spaces, a quick freezing tunnel, four
    freezing plate heat exchagers and tunnel for precooling of chicken meat before
    processing.




                                                                                                 2
ROUNDTABLE ON CLIMATE & OZONE-FRIENDLY TECHNOLOGIES              Belgrade, May 10, 2011




        SITE INFORMATION


        The factory is situated about 60 km to the south from
        Belgrade.

        The design ouside dry and wet bulb air temperature are
        +35°C and +24°C, respectively.




                                                                                          3
ROUNDTABLE ON CLIMATE & OZONE-FRIENDLY TECHNOLOGIES                    Belgrade, May 10, 2011




 THE SYSTEM:

 The refrigeration system includes central refrigeration unit based on ammonia, and seven
 sub-systems with water solution of propylene-glycol as a secondary refrigerant.

 All of the ammonia evaporators: liquid overfeed, circulation numbers 3 to 6

        high system efficiency and reduced operating expenses;

        the evaporator surface is used efficiently and the compressors are
        protected;

        central unit (CP, PV, CP) are located in the machinery room; thus, they
        are under operator surveillance or computer monitoring.




                                                                                                4
ROUNDTABLE ON CLIMATE & OZONE-FRIENDLY TECHNOLOGIES                   Belgrade, May 10, 2011




  AMMONIA AS A REFRIGERANT

    Ammonia has greatest application as a refrigerant in industrial settings, primarily in the
    food processing and food distribution sectors (also in the petrochemical and even
    pharmaceutical sectors).
    Ammonia has superior thermodynamic properties and ammonia refrigeration systems
    are more efficient (3-10%) than most traditional and newer refrigerants in a wide
    range of evaporating and condensing temperatures (+10 to –45°    C);
    Generally speaking, ammonia refrigeration systems cost 10-20% less to install than
    systems using alternative industrial refrigerants.

    zero ODP, zero GWP, low TEWI;
    no cumulative effects on the environment;
    very limited (a few days) atmospheric lifetime (it is considered to be “biodegradable.”)


    self-alarming pungent odor! even the slightest traces of ammonia in the air can be
    easy detected.




                                                                                               5
ROUNDTABLE ON CLIMATE & OZONE-FRIENDLY TECHNOLOGIES                  Belgrade, May 10, 2011



FLAMMABILITY of AMMONIA


Ammonia is difficult to ignite and exhibits a narrow range of flammability (it is
flammable only at high concentrations and under extremely limited conditions).

Because ammonia will not sustain a flame on its own, ignition of ammonia vapor
requires an uninterrupted external flame source.

Ammonia's burning velocity, at a maximum of 8 cm/s, is substantially lower than other
flammable refrigerants, and is not high enough to create an explosion. For these
reasons, ammonia explosions are rare.

Properly designed ammonia refrigeration systems that are well ventilated and free of
open flames or ignition sources mitigate against potential explosion.




                                                                                              6
ROUNDTABLE ON CLIMATE & OZONE-FRIENDLY TECHNOLOGIES                       Belgrade, May 10, 2011



   WHY PROPYLEN GLYCOL (as a secondary fluid)?

   Cost of maintaining: low;

   Bio degradability in water: good, fluid is completely water soluble;

   Toxicity: medium (based on mono propylene glycol and corrosion inhibitors);

   Flash point: 420°
                   C;

   Operational temperature: –30°to 50°
                                     C;

   Fluid is suitable for mixed metal systems;


   Thermophysical properties: poor!




                                                                                                   7
ROUNDTABLE ON CLIMATE & OZONE-FRIENDLY TECHNOLOGIES                                              Belgrade, May 10, 2011




                                    REFRIGERATION LOAD


                                       Evaporator
                                                         Temperature of    Refrigeration
    Nr.         Refrigerant         Temperature of the                                           Consumer
                                                         Secondary Fluid    Capacity
                                     Primary System
     /               /                     °C                  °C              kW                       /
                                                                                            freezing tunnel, plate
    1.    ammonia                          -42                  -             682.0
                                                                                               heat exchangers
    2.    ammonia                          -33                  -             204.2          frozen food storage
    3.    ammonia                          -10                  -             847.0        technology equipment
                                                                                           cooling chambers (25)
    4.    propylene-glycol, 40%            -16               -12/-8           1361.8
                                                                                                 at -5 to +0°C
                                                                                           cooling chambers (24)
    5.    propylene-glycol, 25%            -10                -5/-1           1496.2
                                                                                                at +2 to +8°C
    6.    propylene-glycol, 25%            -10               +7/12            451.7          air handling units

          propylene-glycol, 25% -
                                                             -12/-8
    7.    “ice water” (tertiary            -16                                 34.3        technology equipment
                                                            +0.5/+5.5
          refrigerant )




                                                                                                                          8
ROUNDTABLE ON CLIMATE & OZONE-FRIENDLY TECHNOLOGIES
                                                      Belgrade, May 10, 2011




                                                                               9
ROUNDTABLE ON CLIMATE & OZONE-FRIENDLY TECHNOLOGIES   Belgrade, May 10, 2011




                                                                           10
ROUNDTABLE ON CLIMATE & OZONE-FRIENDLY TECHNOLOGIES                            Belgrade, May 10, 2011




                              SCREW COMPRESSOR UNITS


                                                                                   Installed
                 Working       Swept volume                   Refrigeration
        Nr.                                    Swept volume                         electric
                condititons     (calculated)                    capacity
                                                                                    power
         /       tO/ tC, °C        m3/h            m3/h           kW                  kW

      CP-1                                        2300,0         379,3               132
                 -42/-10           4157
      CP-2                                        2300,0         379,3               132

      CP-3       -33/-10           786            846,5          231,2                55

      CP-4                                        1486,0         830,3               315
                 -16/+35           2391
      CP-5                                        1126,1         613,6               250

      CP-6                                        2311,6         1481,8              450

      CP-7       -10/+35           6697           2311,6         1481,8              450

      CP-8                                        2311,6         1481,8              450

                                                                          Total:    2.234




                                                                                                    11
ROUNDTABLE ON CLIMATE & OZONE-FRIENDLY TECHNOLOGIES                          Belgrade, May 10, 2011




                      TABLE T-4. EVAPORATIVE CONDENSERS



                 Working condititons
                                                      Number of     Make-up      Installed electric
          Nr.                              Capacity
                                                      condensers   Water Flow         power
                      TDB/TWB


           /                                 kW           /           m3/h              kW

          1.          +35/+24               1.500         5        2.62x5=13.1     5x42.0=210

          2.          +35/+24               2.000         1            3.6             51.0

                                  Total:    9.500         /           16.9            261.0




                                                                                                      12
ROUNDTABLE ON CLIMATE & OZONE-FRIENDLY TECHNOLOGIES                                      Belgrade, May 10, 2011




                                     PRESSURE VESSELS
                                          Temperature of                   Volume of      Mass of
      Nr.         Type of Vessel                            Dimensions
                                            Ammonia                         Amonia        Amonia
                         -                     °C              mm             m3            kg
              Low-Pressure Suction
      1.                                       -42         Φ1300x5000        1.66          1.150
                  Accumulator
              Low-Pressure Suction
      2.                                       -33          Φ800x2600        0.33           225
                  Accumulator
              High-Pressure Suction
      3.                                       -16         Φ1200x4000        1.15           605
                  Accumulator
              High-Pressure Suction
      4.                                       -10         Φ1200x3250        0.92           600
                  Accumulator
              High-Pressure Suction
      5.    Accumulator/Intercooler and        -10         Φ1400x5000        1.95           1260
                    Subcooler
              High-Pressure Suction
      6.                                       -10          Φ800x2500        0.32           205
                  Accumulator

      7.    Thermosiphon Accumulator           +35         0.2604x20.000     0.53           310

      8.      High-Pressure Receiver           +35         Φ1000x3500        1.37           805
                                                                                Total:     5.160




                                                                                                              13
ROUNDTABLE ON CLIMATE & OZONE-FRIENDLY TECHNOLOGIES                   Belgrade, May 10, 2011



                                      BENEFITS:
 The amount of ammonia used in the system is relatively high. One of the reason is two-
 stage compression.
 However, ammonia system components are located just close to the compressor room;
 thus there is not ammonia in the production and storage units;

 The refrigeration system inludes the subsystem for using the waste heat (i.e. heat
 extracted through compressor oil cooling); heat of cooling is used for sanitary water
 heating;
   The working fluid is an 40% water solution of propylene-glycol;
   The total heat power of heating is as 802.9 kW ;

 Energy efficiency of the refrigeration plant could be additionaly increassed by using a
 certain part of condenastion heat for water heating purposses.




                                                                                           14
ROUNDTABLE ON CLIMATE & OZONE-FRIENDLY TECHNOLOGIES            Belgrade, May 10, 2011




     Ammonia refrigeration safety features address minimizing the
     refrigerant charge, suitable ventilation, ammonia absorbing systems,
     restricting the use of ammonia in public locations, and promoting
     indirect cooling systems

      With regulations properly tailored to ammonia refrigeration systems,
      the application of ammonia refrigeration systems will probably
      become more widespread.




                                                                                    15
ROUNDTABLE ON CLIMATE & OZONE-FRIENDLY TECHNOLOGIES   Belgrade, May 10, 2011




                                   THANK YOU!




                                                                           16

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New ammonia refrigeration plant

  • 1. ROUNDTABLE ON CLIMATE & OZONE-FRIENDLY TECHNOLOGIES Belgrade, May 10, 2011 Franc Kosi, P.E. The Society for Air-Conditioning, Heating and Refrigeration (KGH) Belgrade, Serbia CASE STUDY: A NEW REFRIGERATION PLANT BASED ON AMMONIA WITH SECONDARY FLUIDS LOOPS 1
  • 2. ROUNDTABLE ON CLIMATE & OZONE-FRIENDLY TECHNOLOGIES Belgrade, May 10, 2011 DESCRIPTION OF ASSIGNMENT To design refrigeration system for an meat industry factory , capacity of about 7.000 chicken per hour (or 105.000 a day). The product are frozen meat pieces, boiled and dried sausages and ham product. The total refrigerated area (two levels) is approximately of 21.250 m2; it comprises 49 cold rooms and production spaces, a quick freezing tunnel, four freezing plate heat exchagers and tunnel for precooling of chicken meat before processing. 2
  • 3. ROUNDTABLE ON CLIMATE & OZONE-FRIENDLY TECHNOLOGIES Belgrade, May 10, 2011 SITE INFORMATION The factory is situated about 60 km to the south from Belgrade. The design ouside dry and wet bulb air temperature are +35°C and +24°C, respectively. 3
  • 4. ROUNDTABLE ON CLIMATE & OZONE-FRIENDLY TECHNOLOGIES Belgrade, May 10, 2011 THE SYSTEM: The refrigeration system includes central refrigeration unit based on ammonia, and seven sub-systems with water solution of propylene-glycol as a secondary refrigerant. All of the ammonia evaporators: liquid overfeed, circulation numbers 3 to 6 high system efficiency and reduced operating expenses; the evaporator surface is used efficiently and the compressors are protected; central unit (CP, PV, CP) are located in the machinery room; thus, they are under operator surveillance or computer monitoring. 4
  • 5. ROUNDTABLE ON CLIMATE & OZONE-FRIENDLY TECHNOLOGIES Belgrade, May 10, 2011 AMMONIA AS A REFRIGERANT Ammonia has greatest application as a refrigerant in industrial settings, primarily in the food processing and food distribution sectors (also in the petrochemical and even pharmaceutical sectors). Ammonia has superior thermodynamic properties and ammonia refrigeration systems are more efficient (3-10%) than most traditional and newer refrigerants in a wide range of evaporating and condensing temperatures (+10 to –45° C); Generally speaking, ammonia refrigeration systems cost 10-20% less to install than systems using alternative industrial refrigerants. zero ODP, zero GWP, low TEWI; no cumulative effects on the environment; very limited (a few days) atmospheric lifetime (it is considered to be “biodegradable.”) self-alarming pungent odor! even the slightest traces of ammonia in the air can be easy detected. 5
  • 6. ROUNDTABLE ON CLIMATE & OZONE-FRIENDLY TECHNOLOGIES Belgrade, May 10, 2011 FLAMMABILITY of AMMONIA Ammonia is difficult to ignite and exhibits a narrow range of flammability (it is flammable only at high concentrations and under extremely limited conditions). Because ammonia will not sustain a flame on its own, ignition of ammonia vapor requires an uninterrupted external flame source. Ammonia's burning velocity, at a maximum of 8 cm/s, is substantially lower than other flammable refrigerants, and is not high enough to create an explosion. For these reasons, ammonia explosions are rare. Properly designed ammonia refrigeration systems that are well ventilated and free of open flames or ignition sources mitigate against potential explosion. 6
  • 7. ROUNDTABLE ON CLIMATE & OZONE-FRIENDLY TECHNOLOGIES Belgrade, May 10, 2011 WHY PROPYLEN GLYCOL (as a secondary fluid)? Cost of maintaining: low; Bio degradability in water: good, fluid is completely water soluble; Toxicity: medium (based on mono propylene glycol and corrosion inhibitors); Flash point: 420° C; Operational temperature: –30°to 50° C; Fluid is suitable for mixed metal systems; Thermophysical properties: poor! 7
  • 8. ROUNDTABLE ON CLIMATE & OZONE-FRIENDLY TECHNOLOGIES Belgrade, May 10, 2011 REFRIGERATION LOAD Evaporator Temperature of Refrigeration Nr. Refrigerant Temperature of the Consumer Secondary Fluid Capacity Primary System / / °C °C kW / freezing tunnel, plate 1. ammonia -42 - 682.0 heat exchangers 2. ammonia -33 - 204.2 frozen food storage 3. ammonia -10 - 847.0 technology equipment cooling chambers (25) 4. propylene-glycol, 40% -16 -12/-8 1361.8 at -5 to +0°C cooling chambers (24) 5. propylene-glycol, 25% -10 -5/-1 1496.2 at +2 to +8°C 6. propylene-glycol, 25% -10 +7/12 451.7 air handling units propylene-glycol, 25% - -12/-8 7. “ice water” (tertiary -16 34.3 technology equipment +0.5/+5.5 refrigerant ) 8
  • 9. ROUNDTABLE ON CLIMATE & OZONE-FRIENDLY TECHNOLOGIES Belgrade, May 10, 2011 9
  • 10. ROUNDTABLE ON CLIMATE & OZONE-FRIENDLY TECHNOLOGIES Belgrade, May 10, 2011 10
  • 11. ROUNDTABLE ON CLIMATE & OZONE-FRIENDLY TECHNOLOGIES Belgrade, May 10, 2011 SCREW COMPRESSOR UNITS Installed Working Swept volume Refrigeration Nr. Swept volume electric condititons (calculated) capacity power / tO/ tC, °C m3/h m3/h kW kW CP-1 2300,0 379,3 132 -42/-10 4157 CP-2 2300,0 379,3 132 CP-3 -33/-10 786 846,5 231,2 55 CP-4 1486,0 830,3 315 -16/+35 2391 CP-5 1126,1 613,6 250 CP-6 2311,6 1481,8 450 CP-7 -10/+35 6697 2311,6 1481,8 450 CP-8 2311,6 1481,8 450 Total: 2.234 11
  • 12. ROUNDTABLE ON CLIMATE & OZONE-FRIENDLY TECHNOLOGIES Belgrade, May 10, 2011 TABLE T-4. EVAPORATIVE CONDENSERS Working condititons Number of Make-up Installed electric Nr. Capacity condensers Water Flow power TDB/TWB / kW / m3/h kW 1. +35/+24 1.500 5 2.62x5=13.1 5x42.0=210 2. +35/+24 2.000 1 3.6 51.0 Total: 9.500 / 16.9 261.0 12
  • 13. ROUNDTABLE ON CLIMATE & OZONE-FRIENDLY TECHNOLOGIES Belgrade, May 10, 2011 PRESSURE VESSELS Temperature of Volume of Mass of Nr. Type of Vessel Dimensions Ammonia Amonia Amonia - °C mm m3 kg Low-Pressure Suction 1. -42 Φ1300x5000 1.66 1.150 Accumulator Low-Pressure Suction 2. -33 Φ800x2600 0.33 225 Accumulator High-Pressure Suction 3. -16 Φ1200x4000 1.15 605 Accumulator High-Pressure Suction 4. -10 Φ1200x3250 0.92 600 Accumulator High-Pressure Suction 5. Accumulator/Intercooler and -10 Φ1400x5000 1.95 1260 Subcooler High-Pressure Suction 6. -10 Φ800x2500 0.32 205 Accumulator 7. Thermosiphon Accumulator +35 0.2604x20.000 0.53 310 8. High-Pressure Receiver +35 Φ1000x3500 1.37 805 Total: 5.160 13
  • 14. ROUNDTABLE ON CLIMATE & OZONE-FRIENDLY TECHNOLOGIES Belgrade, May 10, 2011 BENEFITS: The amount of ammonia used in the system is relatively high. One of the reason is two- stage compression. However, ammonia system components are located just close to the compressor room; thus there is not ammonia in the production and storage units; The refrigeration system inludes the subsystem for using the waste heat (i.e. heat extracted through compressor oil cooling); heat of cooling is used for sanitary water heating; The working fluid is an 40% water solution of propylene-glycol; The total heat power of heating is as 802.9 kW ; Energy efficiency of the refrigeration plant could be additionaly increassed by using a certain part of condenastion heat for water heating purposses. 14
  • 15. ROUNDTABLE ON CLIMATE & OZONE-FRIENDLY TECHNOLOGIES Belgrade, May 10, 2011 Ammonia refrigeration safety features address minimizing the refrigerant charge, suitable ventilation, ammonia absorbing systems, restricting the use of ammonia in public locations, and promoting indirect cooling systems With regulations properly tailored to ammonia refrigeration systems, the application of ammonia refrigeration systems will probably become more widespread. 15
  • 16. ROUNDTABLE ON CLIMATE & OZONE-FRIENDLY TECHNOLOGIES Belgrade, May 10, 2011 THANK YOU! 16