EVALUATION OF A LIQUID DESICCANT AIR CONDITIONING SYSTEM WITH SOLAR THERMAL REGENERATION

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Transcription:

EVALUATION OF A LIQUID DESICCANT AIR CONDITIONING SYSTEM WITH SOLAR THERMAL REGENERATION Stephen J. Harrison, Ph.D., P.Eng. Solar Calorimetry Laboratory Queen s University Kingston, Canada

Overview Main focus of Canadian government is combined heating and cooling systems Liquid Desiccant systems are being primarily evaluated Two LD systems: AIL LD prototype system and an Advantix DuCool air conditioning & dehumidification. Other systems operating in Canada, e.g., conventional absorption (EnerWorks) and large scale ClimateWell system.

Project Overview Liquid desiccant air conditioning (LDAC) demonstration project Phase I (completed): Used gas fired boiler to simulate solar input and drive LDAC Characterized and modelled LDAC performance Phase II (in progress): Installed evacuated tube solar array to drive LDAC Will test different configurations and compare with simulation results Phase III (beginning) Investigate methods to increase electrical COP Investigate additional desiccant storage Investigate optimal configurations and control schemes

Ventilation Load Index (kwh/m 3 /hr) EVALUATION OF A LIQUID DESICCANT AIR CONDITIONING SYSTEM WITH SOLAR Background Solar availability matched closely with cooling load LDAC applicable in Dedicated Outdoor Air System (DOAS) Designed to handle latent load Pair with evaporative cooler or small vapour compression system to handle sensible load Ensure adequate dehumidification and provide better control over humidity 16 14 12 10 8 6 4 2 0 Sensible Cooling Latent Cooling

Conditioner Strong desiccant absorbs moisture from process air Cooling water removes latent heat of condensation Regenerator Heating water added to re-concentrate desiccant Moisture in dilute desiccant desorbed to scavenging air stream Novel low flow configuration eliminates carry over, increases storage capacity Source: Lowenstein, A., Slayzak, S, and Kozubal, E. (2007). "A Zero Carryover Liquid-Desiccant Air Conditioner for Solar Applications," 2006 International Solar Energy Conference, ISEC2006, American Society of Mechanical Engineers, pp. 397-407.

LDAC Benefits Dehumidification without over-cool reheat Low temp (60-90⁰C) heat for regeneration, ideal for solar Loss-less energy storage

LDAC System Description Source: Jones, B.M. (2008). Field Evaluation and Analysis of a Liquid Desiccant Air Handling System, M.Sc. Thesis, Queen s University, Kingston, Ontario, Canada.

Cooling Tower System Operation Regenerator Air Inlet Scavenging Air Outlet Conditioner Air Inlet Process Air Outlet Heating Water Piping System Parameter Results Process Air Flow 1200 L/s Hot Water Flow 90 L/min Cold Water Flow 130 L/min Desiccant Concentration 25.64-42.73 wt% Conditioner Desiccant Flow 5.3 L/min Regenerator Desiccant Flow 6.5 L/min Regeneration Thermal COP 0.419 0.761 Heating Water Temperature 50-90 C Measured Latent Cooling Capacity 4.5 23.3 kw (1.3 6.6 tons) Measured Total Cooling Capacity 4.8 18.1 kw (1.4 5.1 tons)

Solar Array Description Cooling Water Heating Water Non-standard Operation Ball Valve Solenoid Valve Pump Parameter Design Value Design Temperature Rise 10⁰C Total Collector flow rate 40-50 L/min Collector Absorber Area 61m 2 Buffer Storage Size 870L Pumping Power (collector circulator) 25-450W Dry Cooler Rated Capacity 56.5kW Evacuated Tube Solar Collectors Cooling Tower Liquid Desiccant Air Handling Unit P3 Boiler Buffer Storage Dry Cooler P1 P4 P2

System Performance, Characterization and Modelling TRaNsient SYstem Simulation program (TRNSYS)

Thermal COP Electrical COP Regenerator COP COP T COP E COP R Q Q Q W Q Cooling heat, in Cooling elec, in Desorption Q heat, in LDAC Performance Collector Efficiency Solar Fraction Coll. SF mc A 1 p coll Q Q T I T aux load Solar Performance

Solar Fraction EVALUATION OF A LIQUID DESICCANT AIR CONDITIONING SYSTEM WITH SOLAR Simulation Results 1 0.9 0.8 0.7 0.6 0.5 0.4 0.3 0.2 0.1 0 Solar Fraction Collector Stagnation Design point 0 20 40 60 80 100 120 Collector Absorber Area (m 2 ) 0.5 0.4 0.3 0.2 0.1 0 Percentage of Time in Stagnation TRNSYS simulations used to size array Large array increases cost, time in stagnation, pumping power Sized for 65% solar Storage implementation to increase SF and utilization

Performance predicted for series (top) and parallel (bottom) boiler configurations

Boiler setpoint temperature important system parameter Increases cooling capacity and LDAC performance Decreases collector efficiency

Conclusions Installation of 95m 2 evacuated tube solar array for low flow LDAC demonstration project TRNSYS simulations predict 65% solar fraction 65% collector efficiency based on absorber area (41% gross area) Typical LDAC COP T 0.4-.52 Average LDAC latent cooling power between 13 and 23kW (3.8-6.6 tons)

Energy [kwh] EVALUATION OF A LIQUID DESICCANT AIR CONDITIONING SYSTEM WITH SOLAR Future Work Improve system by replacing inefficient fans and pumps and integrating variable speed pump control Implement desiccant storage in demonstration project, use modelling to determine optimal storage configurations Monitor array to determine capacity for space heating and evaluate potential for solar combi-system 4000 3000 2000 Space Heating Load Domestic Hot Water Load Cooling Potential Global Radiation on Collector Solar Energy to Load, Qsol 1000 0

Natural Resources Canada Solar Buildings Research Network Queen s University Mechanical Engineering AIL Research