Australian Solar Cooling Interest Group (ausscig) Conference

Transcription

1 Institute of Air-handling and Refrigeration (ILK Dresden) Component development and first test results of a directly air-cooled water/libr absorption chiller Australian Solar Cooling 2013 Conference, Sydney ILK Dresden R&D company Founded in 1964 Re-established as independent research institute in 1991 Employees: 145 Academics: 72 % mean age: ~44 Laboratory area: ~3000 m² Test rigs: ~56 Phys. / Chem. Laboratories: 25 Directly air-cooled absorption chiller - Australian Solar Cooling 2013 Conference - M. Safarik 2 2

2 Background and goal of the development Problems in systems with small scale chillers Complexity of the systems Interface problems because of different crafts (might be) involved Possibly high error rate during installation Auxiliary energy demand of the system Limited applicability of evaporative systems but high re-cooling sensibility of the cycle Directly air-cooled absorption chiller - Australian Solar Cooling 2013 Conference - M. Safarik 3 3 Challenges Avoiding of an intermediate circuit: - to minimize the auxiliary energy demand (as re-cooling circuit pump usually consumes a lot) - for a better approach of external and internal temperatures since temperature lift is limited Air-cooled absorber needed Water as refrigerant -> big free section needed? Air as heat transfer media -> big free section needed Directly air-cooled absorption chiller - Australian Solar Cooling 2013 Conference - M. Safarik 4 4

3 Distribution of the auxiliary energy demand of a small scale water cooled absorption chiller 35 % 22 % 25 % Nominal cooling capacity: 19,4 kw %-numbers: pump efficiency Directly air-cooled absorption chiller - Australian Solar Cooling 2013 Conference - M. Safarik 5 5 Auxiliary energy demand of the system Auxiliary energy demand of the system with constant speed pumps/fans as a function the cooling capacity Directly air-cooled absorption chiller - Australian Solar Cooling 2013 Conference - M. Safarik 6 6

4 Distribution of auxiliary energy demand Directly air-cooled absorption chiller - Australian Solar Cooling 2013 Conference - M. Safarik 7 7 Examples of air-cooled absorption chillers Source Helioplus H 2 O/LiBr, rotating HX, intermediate circuit Source: Rotartica NH 3 /H 2 O -> high working pressure! Gas driven -> high temperature Directly air-cooled absorption chiller - Australian Solar Cooling 2013 Conference - M. Safarik 8 8

5 Examples of air-cooled absorption chillers Source: Broad Source: Broad H 2 O/LiBr, gas driven, intermediate circuit Q 0 =23 kw; zetta=1,1, P el =1,8kW (COP el =12,7) Directly air-cooled absorption chiller - Australian Solar Cooling 2013 Conference - M. Safarik 9 9 Balancing Single Lift vs. Double Dift thw,e [ C] For chilled water out: 13 C Solid lines single effect/double durchgezogen lift; dashed - Double lines Lift single-effect/single / gestrichelt - Single Lift lift 60 0, t L,e [ C] 0,8 0,75 0,7 0,65 0,6 0,55 0,5 0,45 0,4 0,35 0,3 0,25 0,2 0,15 ζreal [-] Directly air-cooled absorption chiller - Australian Solar Cooling 2013 Conference - M. Safarik 10 10

6 Aimed specifications for the component development External Fluid Nominal Condition Operating Range Chilled water temperature (water w. 20 % Glycol) 18 C / 13 C (in/out) 6 C 20 C (out) Heating water temperature (water w. 20 % Glycol) Ambient air (for re- cooling) Cooling capacity 95 C / 87 C (in/out) 75 C 105 C (in) 32 C C / 42 C C (in/out) 10 C C 32 C (in) 8 kw Condenser and Absorber directly air-cooled Outdoor installation, frost save Auxiliary energy consumption at nominal conditions < 60 W el /kw 0 ( EER > 16) Single effect / single lift Directly air-cooled absorption chiller - Australian Solar Cooling 2013 Conference - M. Safarik Calculated cooling capacities for different temperatures 25 t AL [ C] - t KT,a [ C] Θo [kw o] t HW,e [ C] Directly air-cooled absorption chiller - Australian Solar Cooling 2013 Conference - M. Safarik 12 12

7 Design and testing of components (Samples) Even and permanent distribution of the solution onto vertical absorber tubes Good wetting inside the tubes over the whole lenght Increase of HX area on air side Efficiency of the fan vs. cost Model η Fan [-] cost [ ] Fan Arial 1 0, Axial 2 0, Axial 3 0, Radial 1 0, Radial 2 0, Directly air-cooled absorption chiller - Australian Solar Cooling 2013 Conference - M. Safarik Test of components within functional model Directly air-cooled absorption chiller - Australian Solar Cooling 2013 Conference - M. Safarik 14 14

8 First Results Criteria Design target Reached so far Cooling capacity 8 kw with inlet temperatures: 95 C; 32 C; 18 C 7,7 kw with inlet temperatures: 95 C; 29,5 C; 18 C Thermal EER 0,71 0,72 Auxiliary energy demand ( electrical EER ) 0,50 kw 62,5 Wel/kW0 EERel: > 16 0,64 kw 85 Wel/kW0 EERel: > 12 Directly air-cooled absorption chiller - Australian Solar Cooling 2013 Conference - M. Safarik First Results 8,0 7,5 MP 95/30/13 (t HW,e /t L,e /t KT,a ) Ventilator n=1 1,0 0,9 7,0 6,5 0,8 0,7 6,0 0,6 kw] Θo [k 5,5 5,0 0,5 0,4 ζ [-] 4,5 0,3 4,0 0,2 3,5 0,1 3,0 0, ς rl [l/h] Directly air-cooled absorption chiller - Australian Solar Cooling 2013 Conference - M. Safarik 16 16

9 Outlook Optimisation Decrease of air side pressure drop Prevention of air bypass Improvement of design and alignment of components Avoidance of solution displacement => Design and construction of an optimised prototype Build-up of an adapted testing infrastructure More detailed laboratory testing Monitoring and evaluation of two prototypes in field tests Directly air-cooled absorption chiller - Australian Solar Cooling 2013 Conference - M. Safarik ILK Dresden Thanks for your attention! Department of Applied Energy Engineering Bertolt-Brecht-Allee 20; Dresden; Germany Dr.-Ing. Mathias Safarik Tel.: mathias.safarik@ilkdresden.de 18