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Thesis Defense for the Degree of Master of Science




                                                              2010
                                         MAY 3, ANKARA

NUMERICAL MODELING AND
PERFORMANCE ANALYSIS
OF SOLAR-POWERED IDEAL
ADSORPTION COOLING SYSTEMS




                     Department of Mechanical Engineering
                           Middle East Technical University
Presentation Outline
2
    1.         Motivation
    2.         Adsorption Cycle Descriptions
         i.        Simple cycle
         ii.       Cycle enhancements
    3.         Scope of the Study
    4.         Models
    5.         Conditions Analyzed
    6.         Results
    7.         Conclusions
    8.         Future Work
               Onur TAYLAN                     Thesis Defense
               METU                             May 3, 2010
1. Motivation
3

       Electricity demand exceed supply in Turkey in
        2016-2017 (TEIAS, 2009)
       Increasing cooling loads  Increase in electricity
        demand especially on Mediterranean coast
       Many hotels use conventional AC systems in
        Antalya
       Need to decrease the electricity demand for
        cooling in Antalya
       Need for sustainable and renewable solutions
        Onur TAYLAN                                 Thesis Defense
        METU                                         May 3, 2010
2. Adsorption Cycle Descriptions
4

       Simple Cycle




                            Baker and Kaftanoglu (2007)
         Onur TAYLAN                        Thesis Defense
         METU                                May 3, 2010
2. Adsorption Cycle Descriptions
5

       Cycle Enhancements
         Heat recovery cycle
         Mass recovery cycle

         Heat and mass recovery cycle

         Thermal regeneration
            Thermal     wave
                   Thermal wave cycle with mass recovery
            Convectivethermal wave
            Rotary beds



         Onur TAYLAN                                        Thesis Defense
         METU                                                May 3, 2010
2. Adsorption Cycle Descriptions
6

       Heat Recovery Cycle
                                      Two  adsorbent beds
                                       operating out of phase
                                      Heat transferred from
                                       bed being cooled to
                                       bed being heated
                                      Increase in COP



                       Wang (2001)


         Onur TAYLAN                                  Thesis Defense
         METU                                          May 3, 2010
2. Adsorption Cycle Descriptions
7

       Thermal Wave Cycle




                                                  Taylan et al. (2009)
         Two beds connected via HTF
         HTF between Thot and To

         Sorption processes create dT1 and dT2

         Onur TAYLAN                                       Thesis Defense
         METU                                               May 3, 2010
3. Scope of the Study
8

             What was available           What was needed

       Thermodynamic models         Assess the feasibility of
        of                            using solar energy for
                                      adsorption cooling
         Simple                      systems
         Heat recovery              Develop fast models to
         Thermal wave                perform a large number
                                      of parametric studies
       MATLAB models of
                                     Obtain basic
         Simple
                                      performance trends as
         Heat   recovery             operating conditions vary
         Onur TAYLAN                                    Thesis Defense
         METU                                            May 3, 2010
3. Scope of the Study
9

                           What has been added

       TRNSYS-compatible MATLAB model of thermal wave
        cycle
       Thermodynamic models of
         Thermal wave with adiabatic mass recovery (AMR)
         Thermal wave with isothermal mass recovery (IMR)

       TRNSYS model of solar-thermal system
       Three commercial collector models (two flat plate and
        one evacuated tube) integrated with the solar-thermal
        system
         Onur TAYLAN                                         Thesis Defense
         METU                                                 May 3, 2010
3. Scope of the Study
10

                        What has been added (cont’d)

        Modeling five commonly-used adsorbent –
         refrigerant (working) pairs using MATLAB
        Developing a normalized seasonal model
        Running steady and seasonal-transient simulations
         with the integrated model
        Investigating basic trends in the cycle and system
         performances as some design parameters are
         varied
          Onur TAYLAN                                  Thesis Defense
          METU                                          May 3, 2010
4. Models
11

        Solar Thermal System Model




                        TRNSYS Model   MATLAB Model
                                          Taylan et al. (2010)
          Onur TAYLAN                                Thesis Defense
          METU                                        May 3, 2010
4. Models
12

        Normalized Cooling Load
                              To  ti   Trfrc
         q load,N  ti  =
                             Max To  Trfrc 
        Normalized Cooling Capacity
                                q F  ti × COPads  ti 
         q clg,N  ti  = S×
                                Max  qF ×COPads 
        Normalized Match Factor
         qMatch,N  ti  = qclg,N  ti   qload,N  ti 

          Onur TAYLAN                                       Thesis Defense
          METU                                               May 3, 2010
4. Models
13

        Storage (qStorage,N and qStorage,max)
        Loss (qLoss,N) if qStorage,N = qStorage,max and qclg,N > qload,N
        Backup (qBackup,N) if qStorage,N = 0 and qclg,N < qload,N

        Solar Fraction ( f ) & Loss Fraction ( l )

            qclg,tot      q
                          i
                               clg,N    ti         qLoss,tot     q
                                                                   i
                                                                       Loss,N     ti 
     f=                 =                       l=               =
            qload,tot     q
                          i
                              load,N    ti         qload,tot     q
                                                                   i
                                                                        load,N    ti 


          Onur TAYLAN                                                     Thesis Defense
          METU                                                             May 3, 2010
4. Models
14

        Normalized Collector Area
                                q clg,N  ti 
          Acoll , N =
                      G  ti 
                                     × COPsys  ti 
                               Grfrc

        Normalized Mass of Adsorbent
                      Max  X  
                                      -1

           mads,N   =            
                      X base 

          Onur TAYLAN                                  Thesis Defense
          METU                                          May 3, 2010
5. Conditions Analyzed
15
        Adsorption cycle types
            Reversible (Rev)
            Simple
            Heat recovery with two spatially isothermal beds (HRec)
            Thermal wave with no mass recovery (NMR)
            Thermal wave with adiabatic mass recovery (AMR)
            Thermal wave with isothermal mass recovery (IMR)
        Adsorbent – Refrigerant (working) pairs
            Zeolite NaX – Water (Z1)
            Zeolite X13 – Water (ZW)
            Silica Gel – Water (SG)
            Activated Carbon – Ammonia (CA)
            Activated Carbon – Methanol (CM)
          Onur TAYLAN                                                  Thesis Defense
          METU                                                          May 3, 2010
5. Conditions Analyzed
16
        Collector types
          Flat plate collector (FP)
          Evacuated tube collector (ET)

        Cooling tower types or condensation temperature Tcond
          Dry cooling tower
          Wet cooling tower

        Evaporation temperature Tevap
        Excess bed temperature Texcess  To  Tcond
        Heat capacity ratio R   mshell cshell  mHTF cHTF  mads cads  1


        Maximum bed temperature Thot
          Onur TAYLAN                                                    Thesis Defense
          METU                                                            May 3, 2010
6. Results
17

                Comparison of different adsorption cycles
          5.0
          4.5
          4.0                                                                       Reversible
          3.5                                                                       NMR with bypass
          3.0                                                                       NMR without bypass
     COPads




          2.5                                                                       AMR with bypass
          2.0                                                                       AMR without bypass
          1.5                                                                       IMR with bypass
          1.0                                                                       IMR without bypass
          0.5                                                                       Heat Recovery
          0.0                                                                       Simple
                 90    100       110 120 130 140 150 160 170               180
                                 Maximum Bed Temperature, Thot (oC)
              Base Case: Z1 pair, Tcond = 30oC, Tevap = 10oC, R = 10 and Texcess = 0oC
                   Onur TAYLAN                                                            Thesis Defense
                   METU                                                                    May 3, 2010
6. Results
18

                 Comparison of working pairs
          1.4
          1.2
          1.0
                                                                                                        Rev
 COPsys,clg




          0.8                                                                                           Z1
                                                                                                        ZW
          0.6
                                                                                                        SG
          0.4                                                                                           CA
          0.2                                                                                           CM

          0.0
                80      90     100   110 120 130 140 150 160                170       180      190
                                     Maximum Bed Temperature, Thot (oC)
              Base Case: NMR, Tcond = 30oC, Tevap = 10oC, R = 10 and Texcess = 0oC
                     Onur TAYLAN                                                            Thesis Defense
                     METU                                                                    May 3, 2010
6. Results
19

            Comparison of collectors and solar radiation levels
          0.14
          0.12
          0.10
                                                                                           FP,500
 COPsys




          0.08                                                                             FP,750
          0.06                                                                             FP,1000
                                                                                           ET,500
          0.04                                                                             ET,750
          0.02                                                                             ET,1000

          0.00
                 90        100      110       120       130         140           150
                                 Maximum Bed Temperature, Thot (oC)
          Base Case: Z1 pair, Tcond = 20oC, Tamb = 35oC, Tevap = 10oC, R = 10 and Texcess = 10oC
                 Onur TAYLAN                                                        Thesis Defense
                 METU                                                                May 3, 2010
6. Results
20

                    Comparison of cooling towers and Tevap
              0.16
              0.14
              0.12                                                                             Simple,Dry
              0.10                                                                             HRec,Dry
 COPsys,clg




                                                                                               Simple,Wet
              0.08
                                                                                               HRec,Wet
              0.06                                                                             Simple,5
              0.04                                                                             Simple,15
              0.02                                                                             HRec,5
                                                                                               HRec,15
              0.00
                     90   100       110   120   130   140   150   160    170   180   190
                                    Maximum Bed Temperature, Thot (oC)
               Base Case: Z1 pair, Tcond = 30oC, Tevap = 10oC, R = 10 and Texcess = 10oC
                      Onur TAYLAN                                                           Thesis Defense
                      METU                                                                   May 3, 2010
6. Results
21

                    Comparison of Texcess and R
              0.30

              0.25
                                                                                    Simple,DTexcess=0
 COPsys,clg




              0.20                                                                  Simple,DTexcess=10
                                                                                    HRec,DTexcess=0
              0.15                                                                  HRec,DTexcess=10
                                                                                    Simple,R=0
              0.10                                                                  Simple,R=3
                                                                                    HRec,R=0
              0.05
                                                                                    HRec,R=3
              0.00
                     80     90    100      110      120     130     140     150
                             Maximum Bed Temperature, Thot (oC)
               Base Case: CA pair, Tcond = 30oC, Tevap = 10oC, R = 10 and Texcess = 10oC
                      Onur TAYLAN                                                           Thesis Defense
                      METU                                                                   May 3, 2010
6. Results
22

            Comparison of investigated operating conditions
      9.0
      8.0
      7.0                                                                          base
                                                                                   Tcond=20
      6.0
                                                                                   Tcond=40
 COPads




      5.0
                                                                                   Tevap=5
      4.0                                                                          Tevap=15
      3.0                                                                          DTexcess=0
      2.0                                                                          DTexcess=10
      1.0                                                                          Tcond=20, R=0
      0.0                                                                          Tcond=20, R=10
            90      100    110 120 130 140 150 160                 170    180
                            Maximum Bed Temperature, Thot (oC)
          Base Case: IMR with Z1 pair, Tcond = 30oC, Tevap = 10oC, R = 3 and Texcess = 5oC
                 Onur TAYLAN                                                         Thesis Defense
                 METU                                                                 May 3, 2010
6. Results
23

        Normalized Results (Solar and Loss Fractions)
         f and l not affected by cycle type
          Using ET increases both f and l

          Using wet cooling tower increases f and l for FP and
           decreases l for ET
          Decreasing Texcess or R or increasing S increases f and
           decreases l
          As Thot increases f and l decrease

          1 – f proportional to qBackup


          Onur TAYLAN                                      Thesis Defense
          METU                                              May 3, 2010
6. Results
24

                                        Normalized Results (Required Collector Area)
                                      1000
 Normalized Collector Area, Acoll,N




                                                                                                      FP,Simple,Dry,R=10
                                      100                                                             FP,Simple,Wet,R=10
                                                                                                      FP,HRec,Dry,R=10
                                                                                                      FP,HRec,Wet,R=10
                                                                                                      FP,Simple,Dry,R=0
                                       10
                                                                                                      FP,HRec,Wet,R=0
                                                                                                      ET,Simple,Dry,R=10
                                                                                                      ET,HRec,Dry,R=10
                                        1
                                             90                 120             150             180
                                                           Maximum Bed Temperature, Thot (oC)
                                             Onur TAYLAN                                                   Thesis Defense
                                             METU                                                           May 3, 2010
6. Results
25

                             Normalized Results (Required Adsorbent Mass)
                        2.5
Normalized Adsorbent Mass




                            2.0

                                                                                           Dry+10degC
                            1.5
                                                                                           Dry+5degC
          mads,N




                                                                                           Dry
                            1.0                                                            Wet+10degC
                                                                                           Wet+5degC
                            0.5                                                            Wet


                            0.0
                                  90                120               150            180
                                                Maximum Bed Temperature, Thot (oC)
                                  Onur TAYLAN                                              Thesis Defense
                                  METU                                                      May 3, 2010
7. Conclusions
26

        Suggested configuration
          Thermal  wave cycle
          Evacuated tube collector
          Wet cooling tower
          High evaporation temperature
          Low excess bed temperature
          Low heat capacity ratio for simple and heat recovery
           cycles
          High storage capacity

        Other parameters vary between analyzed cases
          Onur TAYLAN                                    Thesis Defense
          METU                                            May 3, 2010
7. Conclusions
27

        Working pair selection depends on the available
         maximum bed temperature
        Implementing heat recovery increases the
         performance of simple cycle
        Implementing mass recovery to thermal wave cycles
         does not increase the performance significantly,
         although it increases the complexity of the system
        Backup power needed for Antalya

          Onur TAYLAN                                Thesis Defense
          METU                                        May 3, 2010
8. Future Work
28

        Implementing heat and mass transfer and diffusion
         equations based on the specific thermal design of
         the adsorbent bed
        Extending the current analysis with exergy analysis
        Modeling some other kinds of thermal wave
        Modeling heat recovery cycle with infinite number
         of beds and comparing with thermal wave cycle
        Introducing new adsorbent – refrigerant pairs
        Verifying the results of the present study
         experimentally, especially the thermal wave cycle
          Onur TAYLAN                                 Thesis Defense
          METU                                         May 3, 2010
References
29
        Baker, D. K., and Kaftanoglu, B., "Limits to the Thermodynamic Performance of a
         Thermal Wave Adsorption Cooling Cycle," Proceedings of HEFAT 2007, pp. 6, Sun
         City, South Africa, 2007.
        Taylan, O., Baker, D. K., and Kaftanoglu, B., "Parametric Study and Seasonal
         Simulations of a Solar Powered Adsorption Cooling System," Proceedings of ECOS
         2009, pp. 833 - 842, Foz do Iguacu, Parana, Brazil, 2009.
        Taylan, O., Baker, D. K., and Kaftanoglu, B., "COP Trends for Ideal Thermal Wave
         Adsorption Cooling Cycles with Enhancements," Int. J. of Refrigeration: Under
         Review, 2009.
        Taylan, O., Baker, D. K., and Kaftanoglu, B., "Adsorbent – Refrigerant Comparison
         for a Solar Powered Adsorption Cooling System Using Seasonal Simulations,"
         Proceedings of 10th REHVA World Congress, Antalya, Turkey, 2010.
        "Turkish Electrical Energy 10-Year Generation Capacity Projection," Turkish
         Electricity Transmission Co. (TEIAS), Ankara, 2009.
        Wang, R. Z., "Performance Improvement of Adsorption Cooling by Heat and Mass
         Recovery Operation," Int. J. of Refrigeration, vol. 24, no. 7, pp. 602-611, 2001.
          Onur TAYLAN                                                          Thesis Defense
          METU                                                                  May 3, 2010
Thank you!


                                Onur TAYLAN
                               M.Sc. Candidate
Department of Mechanical Engineering             Thesis Defense
Middle East Technical University                  May 3, 2010

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My Thesis Defense Presentation

  • 1. Thesis Defense for the Degree of Master of Science 2010 MAY 3, ANKARA NUMERICAL MODELING AND PERFORMANCE ANALYSIS OF SOLAR-POWERED IDEAL ADSORPTION COOLING SYSTEMS Department of Mechanical Engineering Middle East Technical University
  • 2. Presentation Outline 2 1. Motivation 2. Adsorption Cycle Descriptions i. Simple cycle ii. Cycle enhancements 3. Scope of the Study 4. Models 5. Conditions Analyzed 6. Results 7. Conclusions 8. Future Work Onur TAYLAN Thesis Defense METU May 3, 2010
  • 3. 1. Motivation 3  Electricity demand exceed supply in Turkey in 2016-2017 (TEIAS, 2009)  Increasing cooling loads  Increase in electricity demand especially on Mediterranean coast  Many hotels use conventional AC systems in Antalya  Need to decrease the electricity demand for cooling in Antalya  Need for sustainable and renewable solutions Onur TAYLAN Thesis Defense METU May 3, 2010
  • 4. 2. Adsorption Cycle Descriptions 4  Simple Cycle Baker and Kaftanoglu (2007) Onur TAYLAN Thesis Defense METU May 3, 2010
  • 5. 2. Adsorption Cycle Descriptions 5  Cycle Enhancements  Heat recovery cycle  Mass recovery cycle  Heat and mass recovery cycle  Thermal regeneration  Thermal wave  Thermal wave cycle with mass recovery  Convectivethermal wave  Rotary beds Onur TAYLAN Thesis Defense METU May 3, 2010
  • 6. 2. Adsorption Cycle Descriptions 6  Heat Recovery Cycle  Two adsorbent beds operating out of phase  Heat transferred from bed being cooled to bed being heated  Increase in COP Wang (2001) Onur TAYLAN Thesis Defense METU May 3, 2010
  • 7. 2. Adsorption Cycle Descriptions 7  Thermal Wave Cycle Taylan et al. (2009)  Two beds connected via HTF  HTF between Thot and To  Sorption processes create dT1 and dT2 Onur TAYLAN Thesis Defense METU May 3, 2010
  • 8. 3. Scope of the Study 8 What was available What was needed  Thermodynamic models  Assess the feasibility of of using solar energy for adsorption cooling  Simple systems  Heat recovery  Develop fast models to  Thermal wave perform a large number of parametric studies  MATLAB models of  Obtain basic  Simple performance trends as  Heat recovery operating conditions vary Onur TAYLAN Thesis Defense METU May 3, 2010
  • 9. 3. Scope of the Study 9 What has been added  TRNSYS-compatible MATLAB model of thermal wave cycle  Thermodynamic models of  Thermal wave with adiabatic mass recovery (AMR)  Thermal wave with isothermal mass recovery (IMR)  TRNSYS model of solar-thermal system  Three commercial collector models (two flat plate and one evacuated tube) integrated with the solar-thermal system Onur TAYLAN Thesis Defense METU May 3, 2010
  • 10. 3. Scope of the Study 10 What has been added (cont’d)  Modeling five commonly-used adsorbent – refrigerant (working) pairs using MATLAB  Developing a normalized seasonal model  Running steady and seasonal-transient simulations with the integrated model  Investigating basic trends in the cycle and system performances as some design parameters are varied Onur TAYLAN Thesis Defense METU May 3, 2010
  • 11. 4. Models 11  Solar Thermal System Model TRNSYS Model MATLAB Model Taylan et al. (2010) Onur TAYLAN Thesis Defense METU May 3, 2010
  • 12. 4. Models 12  Normalized Cooling Load To  ti   Trfrc q load,N  ti  = Max To  Trfrc   Normalized Cooling Capacity q F  ti × COPads  ti  q clg,N  ti  = S× Max  qF ×COPads   Normalized Match Factor qMatch,N  ti  = qclg,N  ti   qload,N  ti  Onur TAYLAN Thesis Defense METU May 3, 2010
  • 13. 4. Models 13  Storage (qStorage,N and qStorage,max)  Loss (qLoss,N) if qStorage,N = qStorage,max and qclg,N > qload,N  Backup (qBackup,N) if qStorage,N = 0 and qclg,N < qload,N  Solar Fraction ( f ) & Loss Fraction ( l ) qclg,tot q i clg,N  ti  qLoss,tot q i Loss,N  ti  f= = l= = qload,tot q i load,N  ti  qload,tot q i load,N  ti  Onur TAYLAN Thesis Defense METU May 3, 2010
  • 14. 4. Models 14  Normalized Collector Area q clg,N  ti  Acoll , N = G  ti  × COPsys  ti  Grfrc  Normalized Mass of Adsorbent  Max  X   -1 mads,N =   X base  Onur TAYLAN Thesis Defense METU May 3, 2010
  • 15. 5. Conditions Analyzed 15  Adsorption cycle types  Reversible (Rev)  Simple  Heat recovery with two spatially isothermal beds (HRec)  Thermal wave with no mass recovery (NMR)  Thermal wave with adiabatic mass recovery (AMR)  Thermal wave with isothermal mass recovery (IMR)  Adsorbent – Refrigerant (working) pairs  Zeolite NaX – Water (Z1)  Zeolite X13 – Water (ZW)  Silica Gel – Water (SG)  Activated Carbon – Ammonia (CA)  Activated Carbon – Methanol (CM) Onur TAYLAN Thesis Defense METU May 3, 2010
  • 16. 5. Conditions Analyzed 16  Collector types  Flat plate collector (FP)  Evacuated tube collector (ET)  Cooling tower types or condensation temperature Tcond  Dry cooling tower  Wet cooling tower  Evaporation temperature Tevap  Excess bed temperature Texcess  To  Tcond  Heat capacity ratio R   mshell cshell  mHTF cHTF  mads cads  1  Maximum bed temperature Thot Onur TAYLAN Thesis Defense METU May 3, 2010
  • 17. 6. Results 17  Comparison of different adsorption cycles 5.0 4.5 4.0 Reversible 3.5 NMR with bypass 3.0 NMR without bypass COPads 2.5 AMR with bypass 2.0 AMR without bypass 1.5 IMR with bypass 1.0 IMR without bypass 0.5 Heat Recovery 0.0 Simple 90 100 110 120 130 140 150 160 170 180 Maximum Bed Temperature, Thot (oC) Base Case: Z1 pair, Tcond = 30oC, Tevap = 10oC, R = 10 and Texcess = 0oC Onur TAYLAN Thesis Defense METU May 3, 2010
  • 18. 6. Results 18  Comparison of working pairs 1.4 1.2 1.0 Rev COPsys,clg 0.8 Z1 ZW 0.6 SG 0.4 CA 0.2 CM 0.0 80 90 100 110 120 130 140 150 160 170 180 190 Maximum Bed Temperature, Thot (oC) Base Case: NMR, Tcond = 30oC, Tevap = 10oC, R = 10 and Texcess = 0oC Onur TAYLAN Thesis Defense METU May 3, 2010
  • 19. 6. Results 19  Comparison of collectors and solar radiation levels 0.14 0.12 0.10 FP,500 COPsys 0.08 FP,750 0.06 FP,1000 ET,500 0.04 ET,750 0.02 ET,1000 0.00 90 100 110 120 130 140 150 Maximum Bed Temperature, Thot (oC) Base Case: Z1 pair, Tcond = 20oC, Tamb = 35oC, Tevap = 10oC, R = 10 and Texcess = 10oC Onur TAYLAN Thesis Defense METU May 3, 2010
  • 20. 6. Results 20  Comparison of cooling towers and Tevap 0.16 0.14 0.12 Simple,Dry 0.10 HRec,Dry COPsys,clg Simple,Wet 0.08 HRec,Wet 0.06 Simple,5 0.04 Simple,15 0.02 HRec,5 HRec,15 0.00 90 100 110 120 130 140 150 160 170 180 190 Maximum Bed Temperature, Thot (oC) Base Case: Z1 pair, Tcond = 30oC, Tevap = 10oC, R = 10 and Texcess = 10oC Onur TAYLAN Thesis Defense METU May 3, 2010
  • 21. 6. Results 21  Comparison of Texcess and R 0.30 0.25 Simple,DTexcess=0 COPsys,clg 0.20 Simple,DTexcess=10 HRec,DTexcess=0 0.15 HRec,DTexcess=10 Simple,R=0 0.10 Simple,R=3 HRec,R=0 0.05 HRec,R=3 0.00 80 90 100 110 120 130 140 150 Maximum Bed Temperature, Thot (oC) Base Case: CA pair, Tcond = 30oC, Tevap = 10oC, R = 10 and Texcess = 10oC Onur TAYLAN Thesis Defense METU May 3, 2010
  • 22. 6. Results 22  Comparison of investigated operating conditions 9.0 8.0 7.0 base Tcond=20 6.0 Tcond=40 COPads 5.0 Tevap=5 4.0 Tevap=15 3.0 DTexcess=0 2.0 DTexcess=10 1.0 Tcond=20, R=0 0.0 Tcond=20, R=10 90 100 110 120 130 140 150 160 170 180 Maximum Bed Temperature, Thot (oC) Base Case: IMR with Z1 pair, Tcond = 30oC, Tevap = 10oC, R = 3 and Texcess = 5oC Onur TAYLAN Thesis Defense METU May 3, 2010
  • 23. 6. Results 23  Normalized Results (Solar and Loss Fractions) f and l not affected by cycle type  Using ET increases both f and l  Using wet cooling tower increases f and l for FP and decreases l for ET  Decreasing Texcess or R or increasing S increases f and decreases l  As Thot increases f and l decrease  1 – f proportional to qBackup Onur TAYLAN Thesis Defense METU May 3, 2010
  • 24. 6. Results 24  Normalized Results (Required Collector Area) 1000 Normalized Collector Area, Acoll,N FP,Simple,Dry,R=10 100 FP,Simple,Wet,R=10 FP,HRec,Dry,R=10 FP,HRec,Wet,R=10 FP,Simple,Dry,R=0 10 FP,HRec,Wet,R=0 ET,Simple,Dry,R=10 ET,HRec,Dry,R=10 1 90 120 150 180 Maximum Bed Temperature, Thot (oC) Onur TAYLAN Thesis Defense METU May 3, 2010
  • 25. 6. Results 25  Normalized Results (Required Adsorbent Mass) 2.5 Normalized Adsorbent Mass 2.0 Dry+10degC 1.5 Dry+5degC mads,N Dry 1.0 Wet+10degC Wet+5degC 0.5 Wet 0.0 90 120 150 180 Maximum Bed Temperature, Thot (oC) Onur TAYLAN Thesis Defense METU May 3, 2010
  • 26. 7. Conclusions 26  Suggested configuration  Thermal wave cycle  Evacuated tube collector  Wet cooling tower  High evaporation temperature  Low excess bed temperature  Low heat capacity ratio for simple and heat recovery cycles  High storage capacity  Other parameters vary between analyzed cases Onur TAYLAN Thesis Defense METU May 3, 2010
  • 27. 7. Conclusions 27  Working pair selection depends on the available maximum bed temperature  Implementing heat recovery increases the performance of simple cycle  Implementing mass recovery to thermal wave cycles does not increase the performance significantly, although it increases the complexity of the system  Backup power needed for Antalya Onur TAYLAN Thesis Defense METU May 3, 2010
  • 28. 8. Future Work 28  Implementing heat and mass transfer and diffusion equations based on the specific thermal design of the adsorbent bed  Extending the current analysis with exergy analysis  Modeling some other kinds of thermal wave  Modeling heat recovery cycle with infinite number of beds and comparing with thermal wave cycle  Introducing new adsorbent – refrigerant pairs  Verifying the results of the present study experimentally, especially the thermal wave cycle Onur TAYLAN Thesis Defense METU May 3, 2010
  • 29. References 29  Baker, D. K., and Kaftanoglu, B., "Limits to the Thermodynamic Performance of a Thermal Wave Adsorption Cooling Cycle," Proceedings of HEFAT 2007, pp. 6, Sun City, South Africa, 2007.  Taylan, O., Baker, D. K., and Kaftanoglu, B., "Parametric Study and Seasonal Simulations of a Solar Powered Adsorption Cooling System," Proceedings of ECOS 2009, pp. 833 - 842, Foz do Iguacu, Parana, Brazil, 2009.  Taylan, O., Baker, D. K., and Kaftanoglu, B., "COP Trends for Ideal Thermal Wave Adsorption Cooling Cycles with Enhancements," Int. J. of Refrigeration: Under Review, 2009.  Taylan, O., Baker, D. K., and Kaftanoglu, B., "Adsorbent – Refrigerant Comparison for a Solar Powered Adsorption Cooling System Using Seasonal Simulations," Proceedings of 10th REHVA World Congress, Antalya, Turkey, 2010.  "Turkish Electrical Energy 10-Year Generation Capacity Projection," Turkish Electricity Transmission Co. (TEIAS), Ankara, 2009.  Wang, R. Z., "Performance Improvement of Adsorption Cooling by Heat and Mass Recovery Operation," Int. J. of Refrigeration, vol. 24, no. 7, pp. 602-611, 2001. Onur TAYLAN Thesis Defense METU May 3, 2010
  • 30. Thank you! Onur TAYLAN M.Sc. Candidate Department of Mechanical Engineering Thesis Defense Middle East Technical University May 3, 2010