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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Solar Cooling
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Plan Introduction : Why & What is Solar Cooling 1.Thermodynamic basics 2.Conventional Cooling Cycle 3.Thermal Solar Cooling Techniques 3.1. Absortion Cooling 3.2 Adsortion Cooling 3.3 Dessicant refrigeration 4.Using Solar Energy in Cooling Cycle 5.Consumption, performances and costs Comparative assessment COP Solar collectors used Investment cost Performance data Consumption of auxiliary equipment Water consumption
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 What’s Solar Cooling? The core idea is to use the solar energy directly to produce chilled water. The high temperature required by absorption chillers is provided by solar troughs. The system doesn’t require “strategic” materials (like in PV systems) and has peak production in the moment of peak demand. Heat Transfer Fluid Chilled water
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Why Solar Cooling? Dramatic increase of air conditioning since the early 80ies Cost of energy Issues related to environmental pollution –Due to energy production –Due to the use of CFC’s and HCFC’s Matches demand with source availability Crucial for improving life standards in developing countries
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net 1. Thermodynamic basis
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Underlying Physics Thermodynamics 1 st Law: The change of internal energy (U) of a system is equal to the heat absorbed (Q), plus the external work (W) done on the system W, Q related to the changes the system experiences when going from an initial to a final state
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Thermodynamic Cycle p V T I F Simple Transformation p V T I F Cyclical Transformation or Cycle
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Entropy The concept of entropy was originally introduced in 1865 by Rudolf Clausius. He defined the change in entropy of a thermodynamic system, during a reversible process in which an amount of heat ΔQ is applied at constant absolute temperature T, as ΔS = ΔQ / T Clausius gave the quantity S the name "entropy", from the Greek word τρoπή, "transformation". Since this definition involves only differences in entropy, the entropy itself is only defined up to an arbitrary additive constant
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Thermodynamics - 2 nd Law The most probable processes that can occur in an isolated system are those in which entropy increases or remains constant In other words: In an isolated system there is a well-defined trend of occurrence of process and this is determined by the direction in which entropy increases. In other words: Heat flows naturally from a system of higher temperature to a system of lower temperature.
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Ideal Carnot Refrigeration Cycle 1 2 Isothermal expansion 2 3 Adiabatic compression 3 4 Isothermal compression 4 1 Adiabatic expansion
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Coefficient of Performance (COP) COP = Useful cooling energy Net energy supplied by external sources
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 COP of the refrigeration sub-system Thermal-driven system Electricity-driven system Coefficient of Performance (COP) (2)
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 System Performance STR (System Thermal Ratio) : SEE (System electrical efficiency) : System efficiency :
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net 2. Conventional cooling cycle
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Conventional cooling cycle
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Compression Vapor is compressed and its temperature increases
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Condensation The fluid at "high pressure" is cooled by ambient air and therefore condensed
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Expansion The liquid refrigerant is depressurized and its temperature decreases
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Evaporation The liquid refrigerant at "low pressure" receives heat at low temperature and evaporates
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net 3. Thermal Solar Cooling Techniques
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Thermal Solar Cooling Techniques Absorption Cooling Desiccant Cooling Energy is transferred through phase-change processes Energy is transferred through latent heat processes Adsorption Cooling Energy is transferred through phase-change processes The cooling capacity is based on the physical properties of the cooling fluid, that will change phases at different temperatures, depending on its pressure.
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net 3. Thermal Solar Cooling Techniques 3.1 ABSORTION COOLING
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Absorption Cooling AbsorbentRefrigerant LiBrH2OH2O H2OH2ONH 3 Substances used
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 NH 3 systems -Improved reliability, at low cost, independent control of the cooling medium -Improved pump reliability at low cost -Improved reliability of the fluid level sensors -Increased performance of the various heat transfer processes in the machine -Simplified system concepts
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Properties of H 2 O – NH 3
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 LiBr systems -Increased performance and reduction of cost of solar collectors -Increased performance and reduction of cost of storage systems (e.g. thermochemical) Development of low capacity absorption machines -Development of low capacity air-cooled absorption machines -Increased performance of the various heat transfer processes in the machine
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Properties of LiBr – H 2 O
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Real application – Solar collectors Source: K. Sumathy, Z. C. Huang and Z. F. Li, Solar Energy, 2002, 72(2), 155-165
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Absorption machine Source: K. Sumathy, Z. C. Huang and Z. F. Li, Solar Energy, 2002, 72(2), 155-165
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Single effect Yazaki machine (10 ton LiBr)
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 System combined to sub-floor exchanger
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net 3. Thermal Solar Cooling Techniques 3.2 ADSORTION COOLING
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Adsorption cooling Adsorption is the use of solids for removing substances from gases and liquids The phenomenon is based on the preferential partitioning of substances from the gaseous or liquid phase onto the surface of a solid substrate. The process is reversible
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Adsorption Phase 1 Heating and pressurization The adsorbent temperature increases, which induces a pressure increase, from the evaporation pressure up to the condensation pressure. This period is equivalent to the "compression" phase in compression cycles.
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Adsorption Phase 2 During this period, the adsorber continues receiving heat while being connected to the condenser, which now superimposes its pressure. The adsorbent temperature continues increasing, which induces desorption of vapour. This desorbed vapour is liquified in the condenser. The condensation heat is released to the second heat sink at intermediate temperature. This period is equivalent to the "condensation" in compression cycles. Heating and desorption + condendsation
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Adsorption Phase 3 Cooling and depressurization During this period, the adsorber releases heat while being closed. The adsorbent temperature decreases, which induces the pressure decrease from the condensation pressure down to the evaporation pressure. This period is equivalent to the "expansion" in compression cycles.
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Adsorption Phase 4 During this period, the adsorber continues releasing heat while being connected to the evaporator, which now superimposes its pressure. The adsorbent temperature continues decreasing, which induces adsorption of vapor. This adsorbed vapour is evaporated in the evaporator. The evaporation heat is supplied by the heat source at low temperature. This period is equivalent to the "evaporation" in compression cycles. Cooling and adsorption + evaporation
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Adsorption Cooling - Summary The cycle is intermittent because production of cooling energy is not continuous: it occurs only during part of the cycle When there are two adsorbers in the unit, they can be operated separately and production of cooling energy can be quasi- continuous. When all the energy required for heating the adsorber(s) is supplied by the heat source, the cycle is termed single effect. Typically, for domestic refrigeration conditions, the COP of single effect adsorption cycles is of about 0.3-0.4. When there are two adsorbers or more, other types of cycles can be designed. In double effect cycles or in cycles with heat regeneration, some heat is internally recovered between the adsorbers, and that improves the COP.
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Adsorption cooling - Examples
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net 3. Thermal Solar Cooling Techniques 3.3 DESICCANT REFRIGERATION
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Desiccant refrigeration Addresses the issue of thermal comfort by modifying the water vapor content in a space.
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Desiccant refrigeration principle
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Desiccant refrigeration flow-chart
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net 4. Using Solar Energy in the Cooling Cycle
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Working fluids Solar collector sub-cycle Refrigeration sub-cycle
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Basic Refrigeration Cycle
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Heat-driven systems (1) Absorption
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Heat-driven systems (2) Adsorption
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Heat-driven systems (3) Chemical reaction
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Heat-driven systems (4) Desiccant system
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Heat-driven systems (5) Rankine
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Heat-driven systems (6) Ejector
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 PV-driven systems (1) Thermo-electric (Peltier)
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 PV-driven systems (2) Stirling
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net 5. Consumption, performances and costs
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Comparative assessment Evaluation criteria
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 COP 0.660.600.59 T hot ( o C) 60-11052-8266 0.51 0.74 120 0.85 117 0.49
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Solar collectors used - Flat-plated (63%) - Vacuum tube (21%) - Parabolic : Fixed (10%) Moving (6%) Average specific collector area :3,6 m 2 /kW
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Investment cost Depends on: - power rate - collector type - development phase - operating principle Average investment 4012 Εuro/kW
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Performance data Highest performance LiBr / H 2 O systems Lowest performance NH 3 /H 2 O diffusion system Average annual COP = 0.58
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Consumption of auxiliary equipment Lowest consumption: Absorption systems LiBr/H 2 O systems = 0.018 kWh/kWh Mean annual electricity consumption of fans and pumps = 0.225 kWh electric/kWh thermal
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S ustainable A rchitecture Applied to R eplicable Public A ccess Buildings www.sara-project.net Contract: TREN/04/FP6EN/S07.31838/50 3118 Water consumption Highest consumption Adsorption systems: 7.1 kg.h -1 /kW Majority of systems: 4-6 kg.h -1 /kW Mean annual water consumption : = 5.3 kg.h -1 /kW
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