Solar Powered Air Conditioning


Options For Solar Air Conditioning

1. Photovoltaics
2.Absorption: NH3/H2O or Ammonia/Water
3.Absorption: Water/Lithium Bromide
4. Absorption: Water/Lithium Chloride
5. Adsorption: Water/Silica Gel
6. Adsorption: Activated Carbon/Methanol
7. Open Loop Sorption, Solid Desiccant
8. Open Loop Sorption, Liquid Desiccant
9. Rankine Thermal Heat Pump, Heat Engine
10.Steam Jet Heat Engine
11. Hybrid or Solar Assisted Air Conditioning
12. ThermoElectric Air Conditioning


Solar Air Conditioning Advantages


There are a number of reasons to consider Solar Air Conditioning cooling over conventional cooling technology. The more intense the sun's solar radiation, the higher the ambient temperature so the more we need air-cooling. Solar air-conditioning's cooling capacity will be at it's peak then also. This is the ideal state of harmony between machine and nature. The machines generally utilize environmentally friendly refrigerants. Instead of Chlorofluorocarbon refrigerants used in compression vapor cooling machines, in most cases water is utilized which has no greenhouse potential. Because the systems merely require auxiliary energy for the operation of pumps and heat rejection they utilize significantly less power (or no other power). Solar machines have few moving parts and a long life if designed correctly. The electricity grid is also relieved, since the mass operation of electrical air-conditioners in summer occasionally leads to severe strain on the electricity grid. In addition to cooling, the solar collector system can also provide thermal energy for domestic hot water preparation and heating support which leads to a further reduction of emissions. Furthermore, noise emissions are significantly lower since most of the machines work without compressors.
Some of the disadvantages are so far are the systems are not real efficient, costs are high and many systems have high maintenance. Even with these problems solar powered air cooling and refrigeration is increasing and encouraged by governments. The United States with the [[http://www.smartgrid.gov/sites/default/files/pdfs/Energy_Independence_and_Security_Act_of_2007.pdf|Energy Independence and Security Act of 2007(Public Law 110-140) and specifically Solar Air Conditioning Research and Development Program (Sec. 606)]] is using [[http://www.solar.lynnautorepair.com/content/us-government-solar-air-conditioning-program|taxpayer funding of research and development of solar energy through 2012]].
Solar irradiation must first be converted into a secondary energy in order to be useful for cooling purposes. The two choices are to electricity by photovoltaic modules or to heat by solar thermal collectors.

Compare Solar Air Conditioning Systems ChartCompare Solar Air Conditioning Systems Chart

Photovoltaics:

(sun to electricity) A PV air-conditioning system, consists of PV cells providing electrical energy to run a vapor compression system.
Solar SplitCool DC Air ConditioningSolar SplitCool DC Air Conditioning
Some advantages of this architecture are that after the solar array power is changed to AC, through an inverter, off the shelf products can be used, even for very small systems. Excess power can easily be used in the internal grid or sold to the public grid. Decentralized systems can be used. An already existing conventional vapor compression system, even if decentralized, can easily be converted to a solar-assisted system by simply adding PV cells to the internal grid. Another solar option is to directly use the DC array current and charge up a battery bank and feed a DC air conditioning system.

Some solar test air cooling machines have used photovoltaics to run a Peltier system. A Peltier system is a solid state refrigerator, or thermoelectric cooler. Thermoelectric elements are made of semiconducting materials such as bismuth telluride and antimony telluride alloys (Bi2Te3 and Sb2Te3). Since they have neither moving parts nor refrigerant and can be made very small, they have been used in electronic chip cooling, portable refrigerators and in space applications like satellite and space ships where physical size of a cooling system is extremely limited.
COP of this system is currently very low, ranging from 0.3 to 0.6. Small thermoelectric air-conditioners with a few hundred Watt capacity are available in the market.


Absorption: NH3/H2O or Ammonia/Water

In this system ammonia is used as the refrigerant and water is used as the absorbent. Ammonia-water solution is highly stable and works well with many materials except copper and its alloys that get corroded in the presence of ammonia.
Ammonia & Water Absorption CoolingAmmonia & Water Absorption Cooling

Efficient ammonia/water absorption chillers require water of at least 190 °F (88 °C). Ammonia is toxic and its usage is limited in some countries to the large capacity systems, or secondary heat exchangers to isolate the ammonia.
Single, double or triple absorption cooling cycles are used in different solar-thermal-cooling system designs. Possibly, the more cycles, the more efficient they are.
Parts of a Typical Ammonia/Water Absorption Coolers
1) Evaporator: It is in the evaporator where the refrigerant pure ammonia (NH3) in liquid state produces the cooling effect. It absorbs the heat from the substance to be cooled and gets evaporated. From here, the ammonia passes to the absorber in the gaseous state.
2) Absorber: In the absorber the weak solution of ammonia-water is already present. The water, used as the absorbent in the solution, is unsaturated and it has the capacity to absorb more ammonia gas. As the ammonia from evaporator enters the absorber, it is readily absorbed by water and the strong solution of ammonia-water is formed. During the process of absorption heat is liberated which can reduce the ammonia absorption capacity of water; hence the absorber is cooled by the cooling water. Due to absorption of ammonia, strong solution of ammonia-water is formed in the absorber.
3) Pump: The strong solution of ammonia and water is pumped by the pump at high pressure to the generator.
4) Generator: The strong solution of ammonia refrigerant and water absorbent are heated by the external source of heat such as steam or hot water. It can also be heated by other sources like natural gas, electric heater, waste exhaust heat etc. Due to heating the refrigerant ammonia gets vaporized and it leaves the generator. However, since water has strong affinity for ammonia and its vaporization point is quite low some water particles also get carried away with ammonia refrigerant, so it is important to pass this refrigerant through analyzer.
5) Analyzer: One of the major disadvantages of the ammonia-water vapor absorption refrigeration system is that the water in the solution has quite low vaporizing temperature, hence when ammonia refrigerant gets vaporized in the generator some water also gets vaporized. Thus the ammonia refrigerant leaving the generator carries appreciable amount of water vapor. If this water vapor is allowed to be carried to the evaporator, the capacity of the refrigeration system would reduce. The water vapor from ammonia refrigerant is removed by analyzer and the rectifier.
The analyzer is a sort of the distillation column that is located at the top of the generator. The analyzer consists of number of plates positioned horizontally. When the ammonia refrigerant along with the water vapor particles enters the analyzer, the solution is cooled. Since water has higher saturation temperature, water vapor gets condensed into the water particles that drip down into the generator. The ammonia refrigerant in the gaseous state continues to rise up and it moves to the rectifier.
6) Rectifier or the reflex condenser: The rectifier is a sort of the heat exchanger cooled by the water, which is also used for cooling the condenser. Due to cooling the remaining water vapor mixed with the ammonia refrigerant also gets condensed along with some particles of ammonia. This weak solution of water and ammonia drains down to the generator.
7) Condenser and expansion valve: The pure ammonia refrigerant in the vapor state and at high pressure then enters the condenser where it is cooled by air or water. The refrigerant ammonia gets converted into the liquid state and it then passes through the expansion valve where its temperature and pressure falls down suddenly. Ammonia refrigerant finally enters the evaporator, where it produces the cooling effect. This cycle keeps on repeating continuously.
Meanwhile, when ammonia gets vaporized in the generator, weak solution of ammonia and water is left in it. This solution is expanded in the expansion valve and passed back to the absorber and its cycle repeats.
Some examples of NH3/H2O are SolarNext chillii PSC12.


3. Absorption: Water/Lithium Bromide

First tested in the 1940's with the water-lithium bromide absorption refrigeration system, water is used as the refrigerant while lithium bromide (Li Br) is used as the absorbent.
Water & Lithium Bromide Absorption Cooler: The first solar LiBr based air conditioning system was installed in an experimental solar house in University of Queensland, Australia in 1966.Water & Lithium Bromide Absorption Cooler: The first solar LiBr based air conditioning system was installed in an experimental solar house in University of Queensland, Australia in 1966.
Parts of a Typical Lithium Bromide/Water Absorption Cooler
1) Evaporator: Water as the refrigerant enters the evaporator at very low pressure and temperature. Since very low pressure is maintained inside the evaporator the water exists in the partial liquid state and partial vapor state. This water refrigerant absorbs the heat from the substance to be chilled and gets fully evaporated. It then enters the absorber.
2) Absorber: In the absorber concentrated solution of lithium bromide is already available. Since water is highly soluble in lithium bromide, solution of water-lithium bromide is formed. This solution is pumped by the pump to the generator.

Lithium Bromide & Water Solar Air Conditioning Schematic: There are 4 loops in this single-effect absorption LiBr/Water   1. LiBr/H2O Loop    2. Chilled Water Loop (could flow space air and cool that instead)    3. Solar Hot Water Loop    4. Cooling Water Loop (to cool condensor & absorber)(could use air)Lithium Bromide & Water Solar Air Conditioning Schematic: There are 4 loops in this single-effect absorption LiBr/Water 1. LiBr/H2O Loop 2. Chilled Water Loop (could flow space air and cool that instead) 3. Solar Hot Water Loop 4. Cooling Water Loop (to cool condensor & absorber)(could use air)
3) Generator: The heat is supplied to the refrigerant water and absorbent lithium bromide solution in the generator from the steam or hot water. Due to heating water gets vaporized and it moves to the condenser, where it gets cooled. As water refrigerant moves further in the refrigeration piping and though nozzles, it pressure reduces and so also the temperature. This water refrigerant then enters the evaporator where it produces the cooling effect. This cycle is repeated continuously. Lithium bromide on the other hand, leaves the generator and reenters the absorber for absorbing water refrigerant.
-Advantages of H2O/LiBr over Ammonia/water absorption-
LiBr is a salt (normally solid) and non-volatile compared to NH3. Simpler mechanical systems, do not require rectifiers or condensate pre-coolers. Higher COP than ammonia-water. Water is an excellent refrigerant due to its high latent heat.
-Disadvantages- LiBr/H2O is restricted to applications in which cooling requirements are above its freezing point (0°C). Crystallization is a problem if the --------- is too hot.

Solar Collector Rule of Thumb Sizing:
3 square meters of absorber are per kW of cooling capacity or,114 ft square feet per 12,000 Btu = 1 ton of refrigeration
Equivalent to 48 6 foot vacuum tubes

Some examples of LiBr/H2O solar absorption chillers are Yazaki WRC-SC5, EAW Wegracal SE15, Sonnenklima Suninverse 10 and Rotartica Solar 045.


Absorption: Water/Lithium Chloride

This machine does not need the temperature or flow rate controlled, but will charge with different power depending on the temperature and flow.

ClimateWell 10 Solar Air ConditioningClimateWell 10 Solar Air Conditioning
Examples: ClimateWell 10, by Climatewell Sweden
ClimateWell 10 is a modular absorption machine that differs from the “standard” Lithium Bromide type absorption machines in three main aspects:
It has internal storage in each of the two accumulators. This allows the machine to store chemical energy with a very high density. This energy can subsequently be used both for cooling and heating. It is important to emphasize that this is chemical energy, not thermal energy that is stored. 2. It works intermittently with two parallel accumulators. 3. It is designed to use relatively low temperatures and is hence optimized for usage with solar thermal collectors. ClimateWell 10 is made up of two “barrels” each consisting of a reactor and condenser/evaporator. The two barrels can operate in parallel.


Adsorption Chiller: Water/Silica Gel or Water/Zeolite

This adsorption chiller is a closed system.
Silica Gel Solar Air Conditioning SWAC-10: Powered by 55-85°C hot water.  Suitable to be driven by solar water heater or waste heat from other sources?  Small mass production  10 kW, 20kW,50kW,100kW,200kWSilica Gel Solar Air Conditioning SWAC-10: Powered by 55-85°C hot water. Suitable to be driven by solar water heater or waste heat from other sources? Small mass production 10 kW, 20kW,50kW,100kW,200kWThe Silica Gel/Water chiller uses water as it’s cooling agent. Water evaporates in a vacuum at room temperature and thereby extracts heat from its surroundings (evaporation energy). Through this process, a cooling takes place in the circuit.
Compared to open systems, the evaporated water is not released as steam into the surroundings, but recondensed within the machine. The direct and quick condensation of the evaporated water is thermodynamically difficult, requiring large heat removal and steady pressure. Therefore, the water is first adsorbed by a solid carrier material. This material consists of silica-gel, a material related to quartz or sand. In refrigeration engineering the principle of adsorption " the collection of water vapour in the air by a hydroscopic material (silica-gel, zeolithe)" is commonly used to dehumidify the air. Utilizing the warm waste air in such systems, the material used is constantly regenerated (disc wheels or etc).
The same process takes place in the packaged chiller. With the use of hot water, the adsorbed water on the carrier material (silica-gel) is again evaporated and thereby the carrier material is regenerated. Condensation of the secondary evaporated water (off the carrier material) is, opposed to the primary evaporated water (out of the cooling circuit), now easy.

The following factors are essential for the process:
Silica-gel can easily take up water (adsorb), without causing a structural change or volume expansion.
Silica-gel can easily release the stored water through a temperature increase.
--This process is reversible and unlimitedly repeatable.--
The evaporation process is temperature and pressure dependent. Under normal atmospheric pressure (760 mm Hg), water evaporates at 100°C. If the surrounding pressure drops, the evaporating temperature of the water also decreases.
With the achievement of a high enough vacuum, the water evaporates at a lower temperature.
For the purpose used in the adsorption chiller, a vacuum in the area of 10-20 mm Hg, is sufficient. If water is sprayed or injected into a vessel under vacuum, it evaporates spontaneously and extracts energy from it’s surroundings.
The adsorption chiller utilizes the following properties:
a) the reversible adsorption and desorption process of water on silica-gel
b) the spontaneous evaporation of water on silica-gel
c) the easy condensation
-Advantages- There is no danger of crystallization and thus no limitation in temperatures. There is no internal solution pump and electricity consumption is reduced to a minimum.
Examples of H20/Silica gel are SorTech ACS 08, SorTech ACS 15, SJTU SWAC-10
Example of H2O/Zeolith are InvenSor HTC 10


Adsorption: Activated Carbon/Methanol

Activated Carbon/Methanol  Solar Air Conditioning: An adsorption Activated Carbon/Methanol air conditioning system was developed by Wang in 2001 to be powered by heat sources with temperatures close to 100 °C. Evacuated tube collectors could be used to supply hot water at this level of temperature. The system, had two adsorbers with 26 kg of carbon inside each one and used methanol as refrigerant. The COP and the SCP of this system were significantly influenced by the cycle time. The operation of the system with a cycle time of 30 minutes leads to a COP of 0.15 and a cooling power of 3.84 kW while operation with a cycle time of 60 minutes leads to a COP of 0.21 and cooling power of 3.03 kW.  In both situations, the evaporation temperature was close to 6 °C. To improve the performance of the system, the authors changed the adsorbers, keeping the same charge of carbon, and used a tube and plate heat exchanger being the carbon placed outside the tubes, between the plates. With this new design, the COP obtained was 0.4 and the cooling power was 3.80 kW.  The experimental conditions in this case were: a heat source temperature of 100 °C, an evaporation temperature of 10 °C, a condensing temperature of 24 °C and a cycle time of 50 minutes.Activated Carbon/Methanol Solar Air Conditioning: An adsorption Activated Carbon/Methanol air conditioning system was developed by Wang in 2001 to be powered by heat sources with temperatures close to 100 °C. Evacuated tube collectors could be used to supply hot water at this level of temperature. The system, had two adsorbers with 26 kg of carbon inside each one and used methanol as refrigerant. The COP and the SCP of this system were significantly influenced by the cycle time. The operation of the system with a cycle time of 30 minutes leads to a COP of 0.15 and a cooling power of 3.84 kW while operation with a cycle time of 60 minutes leads to a COP of 0.21 and cooling power of 3.03 kW. In both situations, the evaporation temperature was close to 6 °C. To improve the performance of the system, the authors changed the adsorbers, keeping the same charge of carbon, and used a tube and plate heat exchanger being the carbon placed outside the tubes, between the plates. With this new design, the COP obtained was 0.4 and the cooling power was 3.80 kW. The experimental conditions in this case were: a heat source temperature of 100 °C, an evaporation temperature of 10 °C, a condensing temperature of 24 °C and a cycle time of 50 minutes.

In the mid 1980’s Pons and Guilleminot developed a prototype solar powered activated carbon-methanol ice maker. This machine produced almost 6 kg of ice per m2 of solar panel when the insolation was about 20 MJ day-1, with a solar COP of 0.12. This rate of ice production remains one of the highest obtained by a solar powered icemaker.


Open Loop Sorption, Solid Desiccant

Water/ silica gel or Water/ lithium chloride
Open cycle systems allow complete air-conditioning by supplying cooled and dehumidified air. The “refrigerant” is always water, which is brought into open direct contact with the atmosphere. The most common open systems are desiccant cooling systems with a rotating dehumidification wheel and a solid sorbent.
Solid Desiccant Solar Open Loop Air Conditioning: Warm and humid air enters the slowly rotating desiccant wheel and is dehumidified by adsorption of water (1-2). Since the air is heated up by the adsorption heat, a heat recovery wheel is passed (2-3), resulting in a significant pre-cooling of the supply air stream. Subsequently, the air is humidified and thus further cooled by a controlled humidifier (3-4) according to the set-values of supply air temperature and humidity. The exhaust air stream of the rooms is humidified (6-7) close to the saturation point to exploit the full cooling potential in order to allow an effective heat recovery (7-8). Finally, the sorption wheel has to be regenerated (9-10) by applying heat in a comparatively low temperature range from 50 °C-75 °C and to allow a continuous operation of the dehumidification process.   http://www.solair-project.eu/146.0.htmlSolid Desiccant Solar Open Loop Air Conditioning: Warm and humid air enters the slowly rotating desiccant wheel and is dehumidified by adsorption of water (1-2). Since the air is heated up by the adsorption heat, a heat recovery wheel is passed (2-3), resulting in a significant pre-cooling of the supply air stream. Subsequently, the air is humidified and thus further cooled by a controlled humidifier (3-4) according to the set-values of supply air temperature and humidity. The exhaust air stream of the rooms is humidified (6-7) close to the saturation point to exploit the full cooling potential in order to allow an effective heat recovery (7-8). Finally, the sorption wheel has to be regenerated (9-10) by applying heat in a comparatively low temperature range from 50 °C-75 °C and to allow a continuous operation of the dehumidification process. http://www.solair-project.eu/146.0.html
Flat-plate solar thermal collectors are normally applied as heating system in solar assisted desiccant cooling systems. The solar system may consist of collectors using water as fluid and a water storage, which will increase the utilization of the solar system. This configuration however requires an additional water/air heat exchanger, to connect the solar system to the air system.

Special design of the desiccant cycle is needed in case of extreme outdoor conditions such as the high humidity of ambient air, a standard configuration of the desiccant cooling cycle is not able to reduce the humidity down to a level that is low enough to employ direct evaporative cooling. More complex designs of the desiccant air handling unit employing for instance another enthalpy wheel or additional air coolers supplied by chilled water can overcome this problem. A novel approach is the dehumidification and simultaneously cooling of the supply air in an air-to-air heat exchanger, in which the supply air is dehumidified through sorptive coatings at the heat exchanger wall, and cooled by the returned air, which was humidified close to saturation in order to lower the return air temperature before entering the heat exchanger. The simultaneously dehumidification and cooling improves the efficiency of the system. As a consequence, the supply air humidification may be avoided in moderate climates. Since the sorption material in the supply side of the heat exchanger will be saturated after some time, a periodic operation with two heat exchangers of which one is regenerated, is required.


Open Loop Sorption, Liquid Desiccant

Water/ calcium chloride or Water/ lithium chloride.
Schematic of Liquid Desiccant System for Fresh Air DehumidificationSchematic of Liquid Desiccant System for Fresh Air DehumidificationLiquid Desiccant Air Conditioning SystemLiquid Desiccant Air Conditioning System
These systems have a typical very low driving temperature of 50- 70 °C. Has been called a DER (Dehumidifier–Evaporator–Regenerator). It consists of six major components; an indirect contact evaporative cooler, an air dehumidifier or absorber, a solution regenerator or desorber, two air/air heat exchangers and a solution/solution heat exchanger.
A desiccant can be mixed with water to create an attractive recirculating waterfall, that dehumidifies a room using solar thermal energy to regenerate the liquid, and a PV-powered low-rate water pump.


Rankine & Stirling Thermal Heat Pump, Heat Engine

In the heat engine driven system the heat from the solar collectors is first transformed into mechanical work.
Rankine Solar Thermal Heat Engine: The main equipments include: CPC collector array, heat storage facility, gas boiler, turbine generator unit, and condenser, water circulating pump, valves and pipelines.  This paper designs a solar-heated generation system with  10kW of electricity generation. The steam temperature at the  inlet of turbomachine is 250? with the inlet pressure is  2MPa.  The analysis of four typical working processes under the  different weather conditions is as follows:  (1) When the weather is fine, the steam at the outlet of  collector with high temperature can satisfy the request of  steam admission. Then open the valve V1, V2, and parts of  steam required enter the turbomachine for generating, while  the other steam enter the heat storage facility and deposited.    The boiler is out of work, and the valves V3, V4 are both  closed.  (2) When the weather is not good enough, the steam or  water at the outlet of collector can not satisfy the request of  steam admission of turbomachine. Now open the valve V2  and V4, and close the valve V1 and V3. The fluid at the  collector outlet enters the heat storage facility directly,  mixed with the original water in the container. The  preheated water enters the gas boiler, for heating to the  required steam of turbomachine for generating.  (3) When the weather is bad or it’s at night, the CPC  collector arrays are out of work nearly. Now close the valve  V1, V2, and open the valve V3, V4. The circled water is  delivered to the heat storage facility directly and is mixed  with the original hot water, and then enters the gas boiler.  This method can reduce the resistance loss when the water  flows through the CPC collector array.  (4) When the volume of saturated water in the heat  storage facility reaches to the 90% of the designed and the  temperature reaches to the saturation temperature, close the  valve V2 and open the blow-off valve, emptying the  redundant steam for protecting the heat storage facility. This  kind of state is rare, it appears only in several hottest weeks  every year.  The electricity generation flow processes of this paper can  ensure the system keeps generating steady under four typical  work conditions above in conjunction with the switch of  automatic valvesRankine Solar Thermal Heat Engine: The main equipments include: CPC collector array, heat storage facility, gas boiler, turbine generator unit, and condenser, water circulating pump, valves and pipelines. This paper designs a solar-heated generation system with 10kW of electricity generation. The steam temperature at the inlet of turbomachine is 250? with the inlet pressure is 2MPa. The analysis of four typical working processes under the different weather conditions is as follows: (1) When the weather is fine, the steam at the outlet of collector with high temperature can satisfy the request of steam admission. Then open the valve V1, V2, and parts of steam required enter the turbomachine for generating, while the other steam enter the heat storage facility and deposited. The boiler is out of work, and the valves V3, V4 are both closed. (2) When the weather is not good enough, the steam or water at the outlet of collector can not satisfy the request of steam admission of turbomachine. Now open the valve V2 and V4, and close the valve V1 and V3. The fluid at the collector outlet enters the heat storage facility directly, mixed with the original water in the container. The preheated water enters the gas boiler, for heating to the required steam of turbomachine for generating. (3) When the weather is bad or it’s at night, the CPC collector arrays are out of work nearly. Now close the valve V1, V2, and open the valve V3, V4. The circled water is delivered to the heat storage facility directly and is mixed with the original hot water, and then enters the gas boiler. This method can reduce the resistance loss when the water flows through the CPC collector array. (4) When the volume of saturated water in the heat storage facility reaches to the 90% of the designed and the temperature reaches to the saturation temperature, close the valve V2 and open the blow-off valve, emptying the redundant steam for protecting the heat storage facility. This kind of state is rare, it appears only in several hottest weeks every year. The electricity generation flow processes of this paper can ensure the system keeps generating steady under four typical work conditions above in conjunction with the switch of automatic valves This mechanical work can either be used directly to power a mechanical heat pump or be converted into electricity. The electricity is then used to power a electrically driven heat pump. It can also be used to power a decentralized system. Excess electricity can just as in the PV cell air-conditioning system, be feed to the grid. An electric generator/motor can be connected to the power cycle, the refrigeration cycle, or both by means of clutches. In this way excess power can be taken out to be feed to the grid and auxiliary power can be feed to the refrigeration cycle. Solar Rankine systems were investigated in the 1970s and 1980s. Prigmore and Barber (1975) designed a water-cooled organic Rankine cycle based on R-113 to produce turbine shaft work from 101.7°C water from solar collectors.
Stirling engines can operate at a very high temperature at which a Rankine engine cannot. In order for a solar thermo-mechanical refrigeration system to be competitive, the combination of a solar collector and a heat engine should be at least comparable to a solar electric panel in terms of price.


Steam Jet Heat Engine

Ejector refrigeration technology was used for air conditioning of trains and large buildings (Garris et al., 1998). With a generator temperature between 85 and 95 _C, COPs reported are in the range of 0.2–0.33 for a condenser temperature between 28.

The solar panels must create a steam of 120°C-180°C to drive a steam turbine that does mechanical work. If water is sprayed into a chamber where a low pressure is maintained, a part of the water will evaporate. The enthalpy of evaporation will cool the remaining water to its saturation temperature at the pressure in the chamber. Obviously lower temperature will require lower pressure. Water freezes at 0°C hence temperature lower than 4°C cannot be obtained with water. In this system, high velocity steam is used to entrain the evaporating water vapor. High-pressure motive steam passes through either convergent or convergent-divergent nozzle where it acquires either sonic or supersonic velocity and low pressure of the order of 0.009 kPa corresponding to an evaporator temperature of 4°C. The high momentum of motive steam entrains or carries along with it the water vapor evaporating from the flash chamber. Because of its high velocity it moves the vapors against the pressure gradient up to the condenser where the pressure is 5.6-7.4 kPa corresponding to condenser temperature of 35-45°C. The motive vapor and the evaporated vapor both are condensed and recycled. This system is known as steam jet refrigeration system. Figure 1.7 shows a schematic of the system. It can be seen that this system requires a good vacuum to be maintained. Sometimes, booster ejector is used for this purpose. This system is driven by low- grade energy like solar concentrating collectors can supply.


Hybrid Solar Air Conditioning or (Solar Assisted Air Conditioning)

A conventional air conditioning system uses the compressor (powered by electricity) to pressurize and heat the refrigerant gas up to about 170 degrees. Hybrid Solar Air Conditioning: A standard air conditioning system uses a compressor to increase the pressure on the gas, forcing it into a liquid in the condenser coil. The change of state of the refrigerant starts to take place approximately 2/3rds of the way down the condenser.    A Solar Hybrid Air Conditioning System uses a different method. It uses the heat from the sun to superheat the refrigerant which enables it to begin changing state in the top 2/3rds of the condenser coil.    By using this method it reduces the superheat of compression required to achieve the cooling process in the conventional cooling system as well as utilizing more of the cooling face of the condenser coil.Hybrid Solar Air Conditioning: A standard air conditioning system uses a compressor to increase the pressure on the gas, forcing it into a liquid in the condenser coil. The change of state of the refrigerant starts to take place approximately 2/3rds of the way down the condenser. A Solar Hybrid Air Conditioning System uses a different method. It uses the heat from the sun to superheat the refrigerant which enables it to begin changing state in the top 2/3rds of the condenser coil. By using this method it reduces the superheat of compression required to achieve the cooling process in the conventional cooling system as well as utilizing more of the cooling face of the condenser coil. It then travels into the outside condensing coils where it changes from a gas into a saturated gas (partial liquid). Typically this occurs in the final third of the condensing coil. From there the saturated gas passes through an expansion devise that allows the refrigerant to become a gas again. Once this happens it can absorb heat from the air passing through the inside coil of the air conditioner. From there the refrigerant goes back to the compressor where it starts the whole cycle again.
Hybrid Solar Air Conditioning DiagramHybrid Solar Air Conditioning Diagram

A hybrid solar air conditioning system uses the same basic equipment as a conventional system with a specialized solar collector that is placed between the compressor and the condensing coils. The primary task of the compressor is to pressurize and heat the refrigerant. The hotter it gets the better. A hybrid solar air conditioning system uses a highly efficient vacuum tube collector filled with an organic liquid product. The collector heats the organic substance to over 350 degrees using the power of the sun to superheat the refrigerant above what the compressor would be able to heat it with electricity. The resulting efficiency derived from the solar collector allows for the refrigerant to work more efficiently with no additional moving parts or motors. This increases the ability of the gas to change back into a liquid much quicker and dramatically reduces the energy requirement of the compressor. The gas now condenses back into saturated gas in the first third of the condensing coil not the final third. Therefore by the time the refrigerant reaches the expansion devise in the inside coil, it is already almost a liquid. This allows the near liquid refrigerant to be more efficient at absorbing heat, making it 5-6 degrees cooler in the inside coil, delivering colder, drier air to the building. Refrigerant Type - 407c or 410


ThermoElectric Seebeck Effect Air Conditioning


A full electrical heat to cold option without any mechanical work has such a low COP that at today's advances it is not practical.
Two stages:
The first stage, call it a thermoelectric generator, is the Seeback Effect where the heat from the solar collector is transferred into electrical energy. As with the thermoelectric coolers thermoelectric generators are currently very ineffective due to large leakage of heat through conduction from the hot to the cold side. This could as in the case with the thermoelectric coolers be prevented by a small vacuum gap between hot and cool side. Projected Carnot efficiency for a thermoelectric generator with a vacuum gap is according to Borealis exploration limited 70-80%, which is a very high efficiency.
The second stage, is the Peltier Effect where electricity is changed directly into a temperature effect.

Using the sun's energy through the Photovoltaics solar option instead of the first stage (using thermal solar to electric energy), then use thermoelectric cooling (Peltier) second stage has been experimented with more often and is more efficient than the combinations of Seebeck and Peltier. Advantages of the two stage thermoelectric is it would be a very compact system, no or few moving parts and can handle heavy vibrations.


http://www.fafcosolar.com
http://www.solair-project.eu/146.0.html
http://www.brighthub.com/engineering/mechanical/articles/66301.aspx
http://gwri-ic.technion.ac.il/pdf/Professors/Gershon_Grosman/1.pdf
http://hvac.me.pusan.ac.kr/Data_Lecture/Environmental/5-2.%20Solar%20Ref...
http://en.wikipedia.org/wiki/Solar_air_conditioning
http://www.solarserver.com/solarmagazin/solar-report_0210_e.html
http://www.iea-shc.org/events/exco/68/workshop/Henning-Solar_AC_and_Refr...
http://www.polycity.net/abschlusskonferenz/files/01_dai_yanjun.pdf
http://www.aprekh.org/files/Milind_Rane.pdf