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“Hybrid solar Desiccant Cooling System”
ABSTRACT
Using excess summer heat from solar collectors to drive desiccant cooling systems is often proposed. A two wheel desiccant system using solar heat for desiccant regeneration is typically discussed. The two wheel system uses a desiccant wheel that is “matched” with a heat exchanger wheel. The heat exchanger recycles heat for the desiccant regeneration and improves system efficiency. These systems are generally limited to delivering warm dry air or cool humid air in most parts of the US. A newly patented desiccant cooling cycle creates two dry air streams. This new cycle uses indirect evaporative cooling of one air stream to cool the second stream. Additional direct evaporative cooling allows cool and dry air to be delivered to the building. Regeneration exhaust heat can provide water heating. Combining the system with a new solar air heating system should provide a significant solar heating, cooling, and hot water delivery system.
Table Of Contents
1. Introduction 1.1 Desiccants
2. Desiccant Evaporative Cooling System 3. Solar Desiccant Evaporative Cooling System 3.1 Development Of An Integrated Solar Desiccant Evaporative Cooling Cycle 3.2 New Technologies
4. NovelAire Desiccant Evaporative Cooling System 5. Hybrid Desiccant Evaporative Cooling System 6. Performance Analysis 7. Advantages 8. Application and Additional Research 9. Result and Conclusion
1.0 INTRODUCTION
Low temperature heating dominates all residential, commercial, and industrial end uses of energy within buildings. Nearly 61% of the energy used across all sectors of the economy is for low temperature heating uses. These heating end uses include space heating, industrial process heating, water heating, boiler heating, and clothes drying. The second greatest energy end use is for cooling. Another 13% of all building energy end use is for refrigeration or space cooling. In the late 1990's, the combination of all heating and cooling energy end uses cost US consumers nearly $180 billion per year. Most of this energy use requires the consumption of fossil fuels. In most cases, the energy conversion devices, such as boilers or electric heat pumps, operate at low efficiency compared to the fuel they consume. In almost all fossil energy heating and cooling systems, the conversion from the primary fuel (gas, oil, coal, etc.) to heating or cooling is done at less than 100% efficiency. This is often described as a coefficient of performance of less than 1.0. (COP < 1) However, there are three technologies that operate at what can be called super efficiencies. These technologies convert primary energy into heating or cooling capacity with COP’s between 2 and 5. These three technologies include solar thermal heating, evaporative cooling, and desiccant drying. By using a combination of simple, low energy, physical phenomena, and widely distributed low cost energy and water resources, these three technologies are recognized as super efficient at delivering heating and cooling. Solar air and water heating system have been shown to have a COP of 4 or greater at providing solar heat with little expense in fan or pumping primary energy. Evaporative cooling systems have been demonstrated to operate at a COP of 5 when used in dry conditions. Desiccant system with evaporative final cooling can operate at a COP of more than 2. However, the application of these technologies has been restricted by their individual limits in responding to: 1) High temperature or 2) High levels of humidity, or 3) Harsh economic realities caused by seasonal idleness of expensive heating and cooling equipment. Evaporative cooling is only effective for comfortable cooling in dry climates. When outdoor humidity rises, the cooling capability of direct evaporative systems declines unless occupants are willing to suffer with high humidity. Even in climates that suffer only a few weeks of high humidity, most consumers will select low efficiency compression refrigeration cooling systems for comfort cooling. Since most customers buy only one system, the low COP
compression systems will be the only cooling systems installed. Thus, the rest of the year’s super efficient evaporative cooling capacity is lost for lack of a few weeks of dry air. Solar space heating suffers a similar fate due to the typical high cost of flat plate collector systems and the lack of useful energy cost savings delivered in the summer months. The seasonal decline in cost savings reduces the overall cost savings the systems can deliver in any given year. This stretches out payback periods for traditional flat plate systems and makes them uneconomic for most space heating applications.
1.1 DESICCANT A desiccant material naturally attracts moisture from gases and liquid. The material becomes as moisture is absorbed or collected on the surface; but when heated, the desiccant dries out-or-regenerate and can be use again. Conventional solid desiccant include silica gel, activated alumina, lithium chlorate salt and molecular sieves. Titanium Silicate a class of material called 1m, and synthetic polymer are new solid desiccant material design to be more effective for cooling application. Liquid desiccant include lithium chlorate, lithium bromide, calcium chloride and triethylene glycol solution. In a dehumidifier, the desiccant removes moisture from the air, which release heat and rises the air temperature. The air is then cooled by heat re-covers units and cooling devices such as evaporative cooler or the cooling coil of a conventional air conditional. In a stand alone desiccant system, air is first dried, and then cooled by a heat exchanger and a set of evaporative coolers. This system is free of ozone-depleting CFC and HCFC refrigerant. In most systems, a wheel containing desiccant continuously dehumidify outside air entering the cooling unit. The desiccant is then regenerated by thermal energy. Supply by natural gas, waste heat, or the sun. A desiccant system can also supplement a conventional air conditioning system. The desiccants remove the humidity load while the evaporator of the air conditioner lowers the air temperature. Generally desiccant wheel are used. Fig.1 shows wheel containing desiccant.
2.0 DESICCANT EVAPORATIVE COOLING SYSTEM A typical desiccant cycle can be cost effective when removing humidity from the air. However, regeneration of the desiccant requires heating roughly equal to the energy it provides for dehumidification. When using evaporative final cooling, the system can deliver a range of warm dry air or cool humid air at relatively high COP. A typical two wheel desiccant cycle is shown in Figure 2. The psychometrics for the cycle is shown in Figure 3 along the lines from A to B to C and the “2 wheel limit line”. The regeneration cycle is shown along E, G, I and J. The “2 wheel limit line” in Figure 3 represents the continuum of temperature and humidity possible by evaporative cooling the dry air from point C to D. As shown, the line does not deliver both cooler and drier air than the original state point E. To achieve the necessary cooling that removes both internal and external heat gain and humidity loads, the condition along the line C to D must be substantially cooler and drier than the existing state point E within the building. The line C’ D represents one such cooler drier condition. To achieve this condition usually requires an additional cooling system that completes the final cooling from point C to point C’. Compression refrigeration is most often used for this final cooling in conjunction with a desiccant system for dehumidification. However, in most cases, consumers will buy only one cooling system, a compression system, to meet their entire cooling needs.
Fig.2: Two wheel desiccant cycle
Fig.3: Desiccant psychometrics
3.0SOLAR DESICCANT EVAPORATIVE COOLIONG SYSTEM
3.1 DEVELOPMENTOF AN INTEGRATED SOLAR DESICCANT EVAPORATIVE COOLING CYCLE
With the solar, desiccant, and evaporative cooling industries each targeting different geographic or technological problems, there has been little t development. Solar thermal work is concentrated on flat plate water heating systems, which are generally not cost effective for space heating applications. In general, the northern climates, with high heating needs, are where solar space heating could deliver the greatest value, but this is also where minimal cooling energy is required in the summer. Evaporative cooling is targeted to the dry southwest. Desiccant cooling is targeted to the humid southeast. Despite the differences in geographic, technological, and economic conditions that favor the limited separate use of individual technologies, there is a potential to draw together the best characteristics of each of these super efficient technologies into one super efficient system. The combined solar desiccant evaporative system can provide a significant portion of the space heating, hot water heating and space cooling needs of residential and commercial consumers.
3.2 NEW TECHNOLOGIES Recent patents in each technology have overcome some of the problems holding back greater deployment. Tests of these new technologies in the past 4 years indicate that workable systems can be deployed. These systems have shown the technical capacity to deliver solar heating and desiccant cooling with indirect and direct evaporative cooling. Specifically, these new technologies include the solar thermal tile system shown in Figures 4 and 5 and the NovelAire desiccant evaporative cooling cycle shown schematically, in Figure 6. The solar thermal tile system is a mid temperature air heating collector. It is designed to function as the weather tight roof of a building or as a rack mounted solar collector on low sloped roofs or in ground mounted applications. It is designed to be installed at a cost comparable to high quality slate and tile roofing, which is substantially less expensive than existing mid temperature collectors. As a result, the system can be economically installed to
handle the larger space heating loads, even with the seasonal reduction in productivity during the summer months. Stagnation tests show that the systems can achieve internal air temperatures of greater than 200 degrees F (94 C) and more than 130F (72 C) above ambient temperature. An air flow test with an early prototype showed outlet air temperatures of 160 -180 F (71-82 C) are possible. Higher temperatures are expected with optimal orientation, improved materials such as selective surface absorbers, and optimal air flow. The system is of sufficiently low cost to deploy a large area to deliver a large volume of air for winter space heating, and deliver high air outlet temperatures particularly in the summer. This provides an opportunity to desiccant regeneration with the large quantities of excess summer heat. Because the system is an air heating system, it is well suited for direct delivery of solar heated air for desiccant regeneration.
Fig. 4: Solar thermal tile system
Fig.5: Side view, solar thermal tile system
4.0 NOVELAIRE DESICCANT EVAPORATIVE COOLING SYSTEM One version of the NovelAire desiccant evaporative cooling cycle is shown in Figure 6. The cycle uses excess air ing through the desiccant wheel to create excess dry air to the evaporative cooling process. After leaving the desiccant wheel (B), the hot dry air is cooled in the supply side of a heat exchanger (C). The warm dry air is then split into two air streams. The first stream (C-CX-CY) s an indirect evaporative cooling of the second stream (C-C’). This cools the second stream without adding any humidity at state point C’. The final direct evaporative cooling stage from point C’ to D can adjust the temperature and humidity to any point on the line CD shown in the psychometric chart in Figure 3. The regeneration side of the NovelAire cycle begins by recovering heat via the exhaust side of the heat exchanger. The heat transfer in the supply side of the heat exchanger is from the full air stream with excess dry air. This is more air flow than the reduced volume air which actually enters the building and returns as exhaust. As a result, the smaller volume of exhaust air from the building is not sufficient, by itself, to cool the full excess air flow in the heat exchanger. Therefore, the initial cooling of the exhaust side of the heat exchanger is from a stream of outside air at state point A.
This outside air flow, ing through the first stage of the heat exchanger, cools the hottest air entering at state point B on the supply side. The outside air is then exhausted back to the atmosphere. Then the exhaust air from within the building, es through the second stage of the heat exchanger. The exhaust air further cools the supply air to state point C, while the exhaust air heats to state point G. The exhaust air is then heated from state point G to I by an external heat source, such as gas heat, shown in Figure 6. The high temperature exhaust is then used to regenerate the desiccant and exhausted to the atmosphere at state point J. The obvious difference in the psychometric is that the final cooling line C’ D is moved to a cooler temperature than the “2 wheel limit line”. This allows cool dry air to be introduced to the building to overcome the internal and external heating and humidity loads that a traditional 2 wheel systems can not handle. What is not obvious from the psychometrics is that the gas heating of the smaller exhaust air stream must be increased to regenerate the larger volume of desiccant in the larger wheel. The larger wheel is required to dry the excess air required by the cycle. NovelAire constructed and tested a desiccant evaporative cooling system in the mid 1990s. Patent documentation from 1998 provides an example calculation for a cycle that would produce 5.4 tons of cooling (64 MJ) with a COP of about 0.92. If the system were solely dependent on natural gas or other traditional energy source, then other cooling technologies, such as compression refrigeration, would generally be more cost effective. However, if large volumes of low cost solar heated air are available, then the economics can swing in favor of the solar desiccant evaporative cooling cycle. In addition, because the COP of the solar thermal system is much higher that for natural gas combustion (~4 for solar vs. 1 max. for gas) the COP of the integrated cooling systems can be greatly increased. The efficiency of the system is further improved by using the high temperature waste heat from any of the available air streams involved in the desiccant regeneration. These air streams from the heat exchanger exhaust or from the desiccant wheel exhaust are between 45 and 70 degrees C (112-158 F). By using this heat source to heat water for domestic use, the system increases its productivity, with essentially no additional primary energy being used.
Fig.5: NovelAire DES-EVAP system schematic
5.0 HYBRID DESICCANT EVAPORATIVE COOLING SYSTEM There are several ways to integrate the two technologies. One version of the integrated cycle is shown in Figure 7. The cycle shown includes: 1) A solar thermal tile system. 2) A NovelAire desiccant evaporative cooling systems. 3) One additional evaporative cooling system between state points E and F, and 4) A hot water heating system using the waste heat from the desiccant regeneration at state point J. The psychometrics of the integrated cycle is shown in Figure 8. The increased cooling for the heat exchanger by the building air can be seen from the change in state point temperature from E to F. The first stage cooling of the heat exchanger from A to L can also be seen. The particular integrated cycle shown in Figure 8 does not use recovered heat from the heat exchanger for desiccant regeneration. Instead, the excess solar heated air from the solar
thermal tile roof is used as the primary heating source for desiccant regeneration. (An alternative cycle could introduce air from point L into the solar thermal tile roof system.) Supplemental gas heat, as shown in Figure 8, is used to desiccant regeneration during cloudy days, and possibly early evening cooling hours, or other hours when solar heating is not 100% effective at delivering cool dry air for cooling or dehumidification. With minor adaptation, the supplemental gas heat can also provide the peak space heating required during the coldest winter days. The hot water heating systems uses waste heat from the desiccant regeneration to heat water via an air-to-water heat exchanger. During the rest of the year, solar heated air from the thermal tile roof would be ducted to the same air- to-water heat exchanger for hot water production. Because the solar heating system would provide an air to water heat exchanger for domestic water heating in non summer months, there is little added cost for the heat recovery for water heating. The only added cost would be the duct work and dampers to by the desiccant regeneration when cooling is not required.
Fig.7: Integrated SOLAR-DES-EVAP cycle
Fig. 8: Integrated SOLAR-DES-EVAP psychometrics
6.0 PERFORMANCE ANALYSIS The solar thermal tile roof has been demonstrated to reach stagnation temperatures of 200+ deg. F. (93+ C) and 130 F (72 C) above ambient. Even though delivered air temperatures would be somewhat below the 200 degree F (93 C) temperature, these outlet conditions are sufficient to desiccant regeneration. However, there is a significant likelihood (probability) of raising collector outlet temperatures using several routine measures that were not incorporated in the original stagnation tests. For example, the solar thermal tile test section used painted absorber plates instead of selective surfaces. No anti- reflective coatings were used on the tiles. The collector was at a slope of 20 degrees from the horizontal, an angle that would roughly equal a roof pitch of 4 in 12. The sun was at an angle of 37 degrees below perpendicular to the collector. Given improvements in any of these test conditions, the collector would likely sustain higher delivered air temperatures. These higher temperatures are comparable to other mid temperature air heating collectors which were widely researched in the late 1970s and early 1980s. The higher temperatures would also provide additional desiccant regeneration capacity and greater cooling. Finally, because the output of the solar thermal tile system is heated air, it is compatible with the air drying of the desiccants. This eliminates the temperature drop from a water-to-air heat exchanger that would be required for a liquid based system.
Reference 3 described the economics of the solar thermal tile system. The analysis indicated that the 600 sq ft. (56 sq. m.) solar thermal tile system used for heating only could save $655 per year when competing against $9 per million BTU delivered natural gas. Under these conditions, the system showed a 10 year payback for space heating and water heating and handled 56 % of the total space heating and hot water load for a 2000 sq. ft. (186 sq. m.) house in a Boston, MA climate. The analysis has been extended to the integrated system and evaluated based on climate conditions for Charlotte, NC. Charlotte has both heating and air conditioning loads. The 600 sq. ft. (56 sq. m.) system would deliver energy cost savings as shown in Figure 9. The total energy savings across the year would be 116 gigajoules (110 million Btu) and only 28 gigajoules (26 million Btu) of fan power would be required. The system would handle 87 % of the annual household heating, cooling, and hot water energy load as derived from EIA data from 1993 (Ref. 4). The system would save $847 per year with gas at $9 per million Btu ($8.86/gigajoule) and electricity at $.0785 per KWHR. In the summer months, the system would handle 100% of the cooling load of the 2000 sq ft. (186 sq. m.) house. These calculations assume a collector efficiency of 35% even during summer cooling with high collector operating temperatures. Fig. 7: Integrated SOLAR-DESEVAP psychometrics However, if the collector operating temperatures reduce efficiency to only 20%, the system still handles 81% of the seasonal cooling load. Throughout the year, the systems would handle 74% of the space heating load and 75% of the water heating load, for a total of 87% of the entire heating and cooling load.
Fig.9: Integrated cycle energy cost saving
7.0 ADVANTAGES (1) Desiccant evaporative cooling, used as stand-alone system or to supplement conventional cooling equipment, removes moisture from the air without the use of ozone-depleting compounds. (2) Micro organism are well protected indoors by the moisture surrounding them if humidity is above 70% they can cause acute diseases and cause the building structure and it’s contain to deteriorate. (3)
Direct indirect and evaporative cooling system is less expensive than vapour compression system.
(4) Hybrid system can provide year round comfort. (5) It decreases the electrical demand. (6) Desiccant based system can reduce moisture much below 40f dew point temperature, while the conventional cooling can only dehumidify the air to temperature above 40f dew point temperature. (7) Desiccant system can often permit reduction in size of the conventional system (vapour compression system), because part of cooling load (dehumidification load) is shifted to desiccant system. Size reduction not only save the energy, but it also decreases the electrical demand and may reduce initial capital investment.
8.0 APPLICATION •
DEFENCE The desiccant equipment has been used by national defenses all over the world for
preservation of tank, ships, aircraft, weapon and supplies are kept in dry storages, provided by dehumidifiers. The technology enables an increased combat readiness as well as drastically reducing preservation costs. •
ARMED FORCES USING DEHUMIDIFIER Royal navy and fleet air arm, royal air force, British army, French army, German army,
Israel army, Swedish army and marines, Swiss army, Thai army. •
FOOD AND CONFECTIONERY More and more food confectionary manufacturers are discovering the benefit of low
temperature drying. Hot air drying is either slow or damage the product the affect on
production cause by seasonal weather changes can be minimized if humidity is control. Desiccant drying is essential if quality is to be maintained during the manufacturing of temperature sensitive food product. •
FISH Drying the surface of the fish prevent further moisture loss during the smoking process.
•
SUGAR Sugar will absorb free moisture in the air, causing it to become lumpy. A low relative
humidity is essential in maintaining the sugar in a fluent state. Dry air is normally recirculated through storage silos. •
CHOCOLATE Drying the cooling air before it enters the tunnel allow much colder air to be used without
the risk of condensation. This result in a much faster cooling rate and an improved surface finish on the product. •
Food companies using dehumidifier British sugar, c food, dandy, Cadbury-schweppes, milko, Jordan’s cereals, mars
confectionary, master foods, marabou, trebor Bassett, and lekandbrod.
•
PHARMACIEUTICAL The sscr rotor is ideal for use in pharmaceuticals applications as there are no desiccant
particles carried over with the air flow, as so often happen with lower quality rotor. The sscr rotor is also non toxic and bacteriostatic. •
TABLETTING During tablet production, dry air can prevent agglomeration, moisture regain, disfigured or
crumbling tablet and inconsistent moisture content. •
FLUIDIZEDBED With desiccant dehumidification the drying time can be reduced by as much as 50%. For
temperature sensitive product low temperature drying is essential. •
GELATINE CAPSULE Hygroscopic material such as gelatine required protection from moisture until the capsule is
sealed.
•
COATING Many drugs now required coating using a water base product. During manufacture coating
often require drying before the moisture begin to affect the drug. Removal of moisture from the air before heating greatly increases drying capacity. • PACKING To prevent soluble and effervescent tablets from dissolving prematurely, a low humidity required during the packing process. Even after packing, boxes and sticky labels can be protected from the effect of humidity. •
POWERPLANT Machinery installed in power plant requires protection against moisture. Evaporation
occurs from water surface and pipe containing water resulting in high humidity condition within the normally well insulated building. Condensation will occur whenever the warm air comes into with the surface of pump and pipes containing cold water. To prevent the onset of corrosion, the humidity level should be maintained below 50%. A dehumidifier will control the humidity level within preset condition in
one or more
rooms. By adopting dehumidification, corrosion and malfunction of electrical switch gear and electronics pump and machinery can be greatly reduced. This also leads to reduced maintenance cost.
•
MUSEUMS moisture is one of the many threats against us in our fight to preserve the antique object that make up preserve, lines and other items made of organic materials contain micro-organism which thrive and multiply in high humidity condition, causing damage by mould and fungus growth. Metallic object of all type are susceptible to corrosive degradation in the presence of high humidity condition, causing irreparable damage in some instance.
To avoid expensive and complicated restoration costs, the condition that promotes the damage should be avoided. If the relative humidity is kept within controlled limit, no microorganism or bacteria activity will occur, no corrosion will form on metallic surfaces ensuring that heritage is preserved for further.
8.2 ADDITIONAL RESEARCH Additional research is recommended in the following areas: 1) Evaluate alternative solar tile roof components to establish the most cost effective summer outlet temperature for the solar roof when ing desiccant regeneration. 2) Prepare a desiccant wheel that is optimized to the outlet temperatures of the solar roof. 3) Assemble the components in an operational prototype and test for cooling performance in a suburban setting.
9.0 RESULT AND CONCLUSION The man aim of the study was to investigate change in energy consumption resulting from the use of the hybrid system instead of normal vapour compression unit. The study also compare the energy consumption of these two system with the third option which is the combination of PHE and vapour compression unit is used due the difference in the quality of energy formed being used to run the system, the comparison are made on the basis of energy use and primary energy used. In doing this it is assumed that electricity having thermal energy of 12 Mw\hr. The hybrid cycle can use less energy than a normal vapour compression unit. Considering a case of high effectiveness hybrid cycle meeting the high sensible load. The
average energy saving in the summer and winter conditions are considered is 24%. The saving in resource energy are at least equal to and typically higher than this (27% and40% respectively).the energy saving are the a result of the potential for indirect evaporative cooling which has been used in the cycle to meet the sensible load through the PHE or latent load when the PHE is in conjunction with the desiccant dehumidifier. In almost of the cases the PHE and desiccant dehumidifier can meet the latent load by using only the energy rejected in the condenser of the vapour compression unit for regeneration of the desiccant, when the cooling required is sensible, the PHE can meet a substantial part of it for both climates considered. If the solar energy is used instead of the condenser energy to regenerate the desiccant dehumidifier further energy is possible. The saving is depending on the size of the solar energy system associated with the hybrid cycle. Since solar energy replaces thermal energy needed In the dehumidifier the solar\ hybrid cycle is more promising in the higher latent load and higher ambient humidity cases. Using less effective component also has a significant effect on the hybrid system performance. Considering the case of the cycle meeting a largely sensible load, the energy saving over a vapour compression system drop from 25-12% when the effectiveness drop from the high low values is used. The effect dose not appears as significant as desiccant cooling system. The result indicate that, for the two climate type considered and high sensible load, the hybrid cycle uses 25-40% less energy over January and July than a conventional vapour compression unit.
Bibliography 1) P.
L.
Dhar,
S.
C
Kaushik,
sanjeev
Jain,
Thermodynamics
analysis
of
desiccant augmented evaporative cooling cycle for Indian condition, ASHRAE TRANSACTIONS, 1995. 2) William a Blending, Marc P. F. Delmas, novel desiccant cooling system using indirect evaporative cooler, ASHRAE TRANSACTION, 1997. 3) U.S. Patent 5,651,226 to Archibald dated July 29, 1997. 4) U.S. Patent 5,758,508 to Belding, et.al. dated June 2,1998.
5) John Archibald, Building Integrated Solar Thermal Roofing Systems; History, Current Status, and Future Promise, Proceedings of the ASES Annual Conference, American Solar Energy Society, 1999 Report on Solar Water Heating Quantitative Survey Dec 1997-Sept 1998, Focus Marketing Services, NREL report SR-550-26484, April 1999 6) Energy Information istration, Household Energy Consumption and Expenditures 1993, October 1995.
Website 1) www.americansolar.com
ABSTRACT
Using excess summer heat from solar collectors to drive desiccant cooling systems is often proposed. A two wheel desiccant system using solar heat for desiccant regeneration is typically discussed. The two wheel system uses a desiccant wheel that is “matched” with a heat exchanger wheel. The heat exchanger recycles heat for the desiccant regeneration and improves system efficiency. These systems are generally limited to delivering warm dry air or cool humid air in most parts of the US. A newly patented desiccant cooling cycle creates two dry air streams. This new cycle uses indirect evaporative cooling of one air stream to cool the second stream. Additional direct evaporative cooling allows cool and dry air to be delivered to the building. Regeneration exhaust heat can provide water heating. Combining the system with a new solar air heating system should provide a significant solar heating, cooling, and hot water delivery system.
Table Of Contents
1. Introduction 1.1 Desiccants
2. Desiccant Evaporative Cooling System 3. Solar Desiccant Evaporative Cooling System 3.1 Development Of An Integrated Solar Desiccant Evaporative Cooling Cycle 3.2 New Technologies
4. NovelAire Desiccant Evaporative Cooling System 5. Hybrid Desiccant Evaporative Cooling System 6. Performance Analysis 7. Advantages 8. Application and Additional Research 9. Result and Conclusion
1.0 INTRODUCTION
Low temperature heating dominates all residential, commercial, and industrial end uses of energy within buildings. Nearly 61% of the energy used across all sectors of the economy is for low temperature heating uses. These heating end uses include space heating, industrial process heating, water heating, boiler heating, and clothes drying. The second greatest energy end use is for cooling. Another 13% of all building energy end use is for refrigeration or space cooling. In the late 1990's, the combination of all heating and cooling energy end uses cost US consumers nearly $180 billion per year. Most of this energy use requires the consumption of fossil fuels. In most cases, the energy conversion devices, such as boilers or electric heat pumps, operate at low efficiency compared to the fuel they consume. In almost all fossil energy heating and cooling systems, the conversion from the primary fuel (gas, oil, coal, etc.) to heating or cooling is done at less than 100% efficiency. This is often described as a coefficient of performance of less than 1.0. (COP < 1) However, there are three technologies that operate at what can be called super efficiencies. These technologies convert primary energy into heating or cooling capacity with COP’s between 2 and 5. These three technologies include solar thermal heating, evaporative cooling, and desiccant drying. By using a combination of simple, low energy, physical phenomena, and widely distributed low cost energy and water resources, these three technologies are recognized as super efficient at delivering heating and cooling. Solar air and water heating system have been shown to have a COP of 4 or greater at providing solar heat with little expense in fan or pumping primary energy. Evaporative cooling systems have been demonstrated to operate at a COP of 5 when used in dry conditions. Desiccant system with evaporative final cooling can operate at a COP of more than 2. However, the application of these technologies has been restricted by their individual limits in responding to: 1) High temperature or 2) High levels of humidity, or 3) Harsh economic realities caused by seasonal idleness of expensive heating and cooling equipment. Evaporative cooling is only effective for comfortable cooling in dry climates. When outdoor humidity rises, the cooling capability of direct evaporative systems declines unless occupants are willing to suffer with high humidity. Even in climates that suffer only a few weeks of high humidity, most consumers will select low efficiency compression refrigeration cooling systems for comfort cooling. Since most customers buy only one system, the low COP
compression systems will be the only cooling systems installed. Thus, the rest of the year’s super efficient evaporative cooling capacity is lost for lack of a few weeks of dry air. Solar space heating suffers a similar fate due to the typical high cost of flat plate collector systems and the lack of useful energy cost savings delivered in the summer months. The seasonal decline in cost savings reduces the overall cost savings the systems can deliver in any given year. This stretches out payback periods for traditional flat plate systems and makes them uneconomic for most space heating applications.
1.1 DESICCANT A desiccant material naturally attracts moisture from gases and liquid. The material becomes as moisture is absorbed or collected on the surface; but when heated, the desiccant dries out-or-regenerate and can be use again. Conventional solid desiccant include silica gel, activated alumina, lithium chlorate salt and molecular sieves. Titanium Silicate a class of material called 1m, and synthetic polymer are new solid desiccant material design to be more effective for cooling application. Liquid desiccant include lithium chlorate, lithium bromide, calcium chloride and triethylene glycol solution. In a dehumidifier, the desiccant removes moisture from the air, which release heat and rises the air temperature. The air is then cooled by heat re-covers units and cooling devices such as evaporative cooler or the cooling coil of a conventional air conditional. In a stand alone desiccant system, air is first dried, and then cooled by a heat exchanger and a set of evaporative coolers. This system is free of ozone-depleting CFC and HCFC refrigerant. In most systems, a wheel containing desiccant continuously dehumidify outside air entering the cooling unit. The desiccant is then regenerated by thermal energy. Supply by natural gas, waste heat, or the sun. A desiccant system can also supplement a conventional air conditioning system. The desiccants remove the humidity load while the evaporator of the air conditioner lowers the air temperature. Generally desiccant wheel are used. Fig.1 shows wheel containing desiccant.
2.0 DESICCANT EVAPORATIVE COOLING SYSTEM A typical desiccant cycle can be cost effective when removing humidity from the air. However, regeneration of the desiccant requires heating roughly equal to the energy it provides for dehumidification. When using evaporative final cooling, the system can deliver a range of warm dry air or cool humid air at relatively high COP. A typical two wheel desiccant cycle is shown in Figure 2. The psychometrics for the cycle is shown in Figure 3 along the lines from A to B to C and the “2 wheel limit line”. The regeneration cycle is shown along E, G, I and J. The “2 wheel limit line” in Figure 3 represents the continuum of temperature and humidity possible by evaporative cooling the dry air from point C to D. As shown, the line does not deliver both cooler and drier air than the original state point E. To achieve the necessary cooling that removes both internal and external heat gain and humidity loads, the condition along the line C to D must be substantially cooler and drier than the existing state point E within the building. The line C’ D represents one such cooler drier condition. To achieve this condition usually requires an additional cooling system that completes the final cooling from point C to point C’. Compression refrigeration is most often used for this final cooling in conjunction with a desiccant system for dehumidification. However, in most cases, consumers will buy only one cooling system, a compression system, to meet their entire cooling needs.
Fig.2: Two wheel desiccant cycle
Fig.3: Desiccant psychometrics
3.0SOLAR DESICCANT EVAPORATIVE COOLIONG SYSTEM
3.1 DEVELOPMENTOF AN INTEGRATED SOLAR DESICCANT EVAPORATIVE COOLING CYCLE
With the solar, desiccant, and evaporative cooling industries each targeting different geographic or technological problems, there has been little t development. Solar thermal work is concentrated on flat plate water heating systems, which are generally not cost effective for space heating applications. In general, the northern climates, with high heating needs, are where solar space heating could deliver the greatest value, but this is also where minimal cooling energy is required in the summer. Evaporative cooling is targeted to the dry southwest. Desiccant cooling is targeted to the humid southeast. Despite the differences in geographic, technological, and economic conditions that favor the limited separate use of individual technologies, there is a potential to draw together the best characteristics of each of these super efficient technologies into one super efficient system. The combined solar desiccant evaporative system can provide a significant portion of the space heating, hot water heating and space cooling needs of residential and commercial consumers.
3.2 NEW TECHNOLOGIES Recent patents in each technology have overcome some of the problems holding back greater deployment. Tests of these new technologies in the past 4 years indicate that workable systems can be deployed. These systems have shown the technical capacity to deliver solar heating and desiccant cooling with indirect and direct evaporative cooling. Specifically, these new technologies include the solar thermal tile system shown in Figures 4 and 5 and the NovelAire desiccant evaporative cooling cycle shown schematically, in Figure 6. The solar thermal tile system is a mid temperature air heating collector. It is designed to function as the weather tight roof of a building or as a rack mounted solar collector on low sloped roofs or in ground mounted applications. It is designed to be installed at a cost comparable to high quality slate and tile roofing, which is substantially less expensive than existing mid temperature collectors. As a result, the system can be economically installed to
handle the larger space heating loads, even with the seasonal reduction in productivity during the summer months. Stagnation tests show that the systems can achieve internal air temperatures of greater than 200 degrees F (94 C) and more than 130F (72 C) above ambient temperature. An air flow test with an early prototype showed outlet air temperatures of 160 -180 F (71-82 C) are possible. Higher temperatures are expected with optimal orientation, improved materials such as selective surface absorbers, and optimal air flow. The system is of sufficiently low cost to deploy a large area to deliver a large volume of air for winter space heating, and deliver high air outlet temperatures particularly in the summer. This provides an opportunity to desiccant regeneration with the large quantities of excess summer heat. Because the system is an air heating system, it is well suited for direct delivery of solar heated air for desiccant regeneration.
Fig. 4: Solar thermal tile system
Fig.5: Side view, solar thermal tile system
4.0 NOVELAIRE DESICCANT EVAPORATIVE COOLING SYSTEM One version of the NovelAire desiccant evaporative cooling cycle is shown in Figure 6. The cycle uses excess air ing through the desiccant wheel to create excess dry air to the evaporative cooling process. After leaving the desiccant wheel (B), the hot dry air is cooled in the supply side of a heat exchanger (C). The warm dry air is then split into two air streams. The first stream (C-CX-CY) s an indirect evaporative cooling of the second stream (C-C’). This cools the second stream without adding any humidity at state point C’. The final direct evaporative cooling stage from point C’ to D can adjust the temperature and humidity to any point on the line CD shown in the psychometric chart in Figure 3. The regeneration side of the NovelAire cycle begins by recovering heat via the exhaust side of the heat exchanger. The heat transfer in the supply side of the heat exchanger is from the full air stream with excess dry air. This is more air flow than the reduced volume air which actually enters the building and returns as exhaust. As a result, the smaller volume of exhaust air from the building is not sufficient, by itself, to cool the full excess air flow in the heat exchanger. Therefore, the initial cooling of the exhaust side of the heat exchanger is from a stream of outside air at state point A.
This outside air flow, ing through the first stage of the heat exchanger, cools the hottest air entering at state point B on the supply side. The outside air is then exhausted back to the atmosphere. Then the exhaust air from within the building, es through the second stage of the heat exchanger. The exhaust air further cools the supply air to state point C, while the exhaust air heats to state point G. The exhaust air is then heated from state point G to I by an external heat source, such as gas heat, shown in Figure 6. The high temperature exhaust is then used to regenerate the desiccant and exhausted to the atmosphere at state point J. The obvious difference in the psychometric is that the final cooling line C’ D is moved to a cooler temperature than the “2 wheel limit line”. This allows cool dry air to be introduced to the building to overcome the internal and external heating and humidity loads that a traditional 2 wheel systems can not handle. What is not obvious from the psychometrics is that the gas heating of the smaller exhaust air stream must be increased to regenerate the larger volume of desiccant in the larger wheel. The larger wheel is required to dry the excess air required by the cycle. NovelAire constructed and tested a desiccant evaporative cooling system in the mid 1990s. Patent documentation from 1998 provides an example calculation for a cycle that would produce 5.4 tons of cooling (64 MJ) with a COP of about 0.92. If the system were solely dependent on natural gas or other traditional energy source, then other cooling technologies, such as compression refrigeration, would generally be more cost effective. However, if large volumes of low cost solar heated air are available, then the economics can swing in favor of the solar desiccant evaporative cooling cycle. In addition, because the COP of the solar thermal system is much higher that for natural gas combustion (~4 for solar vs. 1 max. for gas) the COP of the integrated cooling systems can be greatly increased. The efficiency of the system is further improved by using the high temperature waste heat from any of the available air streams involved in the desiccant regeneration. These air streams from the heat exchanger exhaust or from the desiccant wheel exhaust are between 45 and 70 degrees C (112-158 F). By using this heat source to heat water for domestic use, the system increases its productivity, with essentially no additional primary energy being used.
Fig.5: NovelAire DES-EVAP system schematic
5.0 HYBRID DESICCANT EVAPORATIVE COOLING SYSTEM There are several ways to integrate the two technologies. One version of the integrated cycle is shown in Figure 7. The cycle shown includes: 1) A solar thermal tile system. 2) A NovelAire desiccant evaporative cooling systems. 3) One additional evaporative cooling system between state points E and F, and 4) A hot water heating system using the waste heat from the desiccant regeneration at state point J. The psychometrics of the integrated cycle is shown in Figure 8. The increased cooling for the heat exchanger by the building air can be seen from the change in state point temperature from E to F. The first stage cooling of the heat exchanger from A to L can also be seen. The particular integrated cycle shown in Figure 8 does not use recovered heat from the heat exchanger for desiccant regeneration. Instead, the excess solar heated air from the solar
thermal tile roof is used as the primary heating source for desiccant regeneration. (An alternative cycle could introduce air from point L into the solar thermal tile roof system.) Supplemental gas heat, as shown in Figure 8, is used to desiccant regeneration during cloudy days, and possibly early evening cooling hours, or other hours when solar heating is not 100% effective at delivering cool dry air for cooling or dehumidification. With minor adaptation, the supplemental gas heat can also provide the peak space heating required during the coldest winter days. The hot water heating systems uses waste heat from the desiccant regeneration to heat water via an air-to-water heat exchanger. During the rest of the year, solar heated air from the thermal tile roof would be ducted to the same air- to-water heat exchanger for hot water production. Because the solar heating system would provide an air to water heat exchanger for domestic water heating in non summer months, there is little added cost for the heat recovery for water heating. The only added cost would be the duct work and dampers to by the desiccant regeneration when cooling is not required.
Fig.7: Integrated SOLAR-DES-EVAP cycle
Fig. 8: Integrated SOLAR-DES-EVAP psychometrics
6.0 PERFORMANCE ANALYSIS The solar thermal tile roof has been demonstrated to reach stagnation temperatures of 200+ deg. F. (93+ C) and 130 F (72 C) above ambient. Even though delivered air temperatures would be somewhat below the 200 degree F (93 C) temperature, these outlet conditions are sufficient to desiccant regeneration. However, there is a significant likelihood (probability) of raising collector outlet temperatures using several routine measures that were not incorporated in the original stagnation tests. For example, the solar thermal tile test section used painted absorber plates instead of selective surfaces. No anti- reflective coatings were used on the tiles. The collector was at a slope of 20 degrees from the horizontal, an angle that would roughly equal a roof pitch of 4 in 12. The sun was at an angle of 37 degrees below perpendicular to the collector. Given improvements in any of these test conditions, the collector would likely sustain higher delivered air temperatures. These higher temperatures are comparable to other mid temperature air heating collectors which were widely researched in the late 1970s and early 1980s. The higher temperatures would also provide additional desiccant regeneration capacity and greater cooling. Finally, because the output of the solar thermal tile system is heated air, it is compatible with the air drying of the desiccants. This eliminates the temperature drop from a water-to-air heat exchanger that would be required for a liquid based system.
Reference 3 described the economics of the solar thermal tile system. The analysis indicated that the 600 sq ft. (56 sq. m.) solar thermal tile system used for heating only could save $655 per year when competing against $9 per million BTU delivered natural gas. Under these conditions, the system showed a 10 year payback for space heating and water heating and handled 56 % of the total space heating and hot water load for a 2000 sq. ft. (186 sq. m.) house in a Boston, MA climate. The analysis has been extended to the integrated system and evaluated based on climate conditions for Charlotte, NC. Charlotte has both heating and air conditioning loads. The 600 sq. ft. (56 sq. m.) system would deliver energy cost savings as shown in Figure 9. The total energy savings across the year would be 116 gigajoules (110 million Btu) and only 28 gigajoules (26 million Btu) of fan power would be required. The system would handle 87 % of the annual household heating, cooling, and hot water energy load as derived from EIA data from 1993 (Ref. 4). The system would save $847 per year with gas at $9 per million Btu ($8.86/gigajoule) and electricity at $.0785 per KWHR. In the summer months, the system would handle 100% of the cooling load of the 2000 sq ft. (186 sq. m.) house. These calculations assume a collector efficiency of 35% even during summer cooling with high collector operating temperatures. Fig. 7: Integrated SOLAR-DESEVAP psychometrics However, if the collector operating temperatures reduce efficiency to only 20%, the system still handles 81% of the seasonal cooling load. Throughout the year, the systems would handle 74% of the space heating load and 75% of the water heating load, for a total of 87% of the entire heating and cooling load.
Fig.9: Integrated cycle energy cost saving
7.0 ADVANTAGES (1) Desiccant evaporative cooling, used as stand-alone system or to supplement conventional cooling equipment, removes moisture from the air without the use of ozone-depleting compounds. (2) Micro organism are well protected indoors by the moisture surrounding them if humidity is above 70% they can cause acute diseases and cause the building structure and it’s contain to deteriorate. (3)
Direct indirect and evaporative cooling system is less expensive than vapour compression system.
(4) Hybrid system can provide year round comfort. (5) It decreases the electrical demand. (6) Desiccant based system can reduce moisture much below 40f dew point temperature, while the conventional cooling can only dehumidify the air to temperature above 40f dew point temperature. (7) Desiccant system can often permit reduction in size of the conventional system (vapour compression system), because part of cooling load (dehumidification load) is shifted to desiccant system. Size reduction not only save the energy, but it also decreases the electrical demand and may reduce initial capital investment.
8.0 APPLICATION •
DEFENCE The desiccant equipment has been used by national defenses all over the world for
preservation of tank, ships, aircraft, weapon and supplies are kept in dry storages, provided by dehumidifiers. The technology enables an increased combat readiness as well as drastically reducing preservation costs. •
ARMED FORCES USING DEHUMIDIFIER Royal navy and fleet air arm, royal air force, British army, French army, German army,
Israel army, Swedish army and marines, Swiss army, Thai army. •
FOOD AND CONFECTIONERY More and more food confectionary manufacturers are discovering the benefit of low
temperature drying. Hot air drying is either slow or damage the product the affect on
production cause by seasonal weather changes can be minimized if humidity is control. Desiccant drying is essential if quality is to be maintained during the manufacturing of temperature sensitive food product. •
FISH Drying the surface of the fish prevent further moisture loss during the smoking process.
•
SUGAR Sugar will absorb free moisture in the air, causing it to become lumpy. A low relative
humidity is essential in maintaining the sugar in a fluent state. Dry air is normally recirculated through storage silos. •
CHOCOLATE Drying the cooling air before it enters the tunnel allow much colder air to be used without
the risk of condensation. This result in a much faster cooling rate and an improved surface finish on the product. •
Food companies using dehumidifier British sugar, c food, dandy, Cadbury-schweppes, milko, Jordan’s cereals, mars
confectionary, master foods, marabou, trebor Bassett, and lekandbrod.
•
PHARMACIEUTICAL The sscr rotor is ideal for use in pharmaceuticals applications as there are no desiccant
particles carried over with the air flow, as so often happen with lower quality rotor. The sscr rotor is also non toxic and bacteriostatic. •
TABLETTING During tablet production, dry air can prevent agglomeration, moisture regain, disfigured or
crumbling tablet and inconsistent moisture content. •
FLUIDIZEDBED With desiccant dehumidification the drying time can be reduced by as much as 50%. For
temperature sensitive product low temperature drying is essential. •
GELATINE CAPSULE Hygroscopic material such as gelatine required protection from moisture until the capsule is
sealed.
•
COATING Many drugs now required coating using a water base product. During manufacture coating
often require drying before the moisture begin to affect the drug. Removal of moisture from the air before heating greatly increases drying capacity. • PACKING To prevent soluble and effervescent tablets from dissolving prematurely, a low humidity required during the packing process. Even after packing, boxes and sticky labels can be protected from the effect of humidity. •
POWERPLANT Machinery installed in power plant requires protection against moisture. Evaporation
occurs from water surface and pipe containing water resulting in high humidity condition within the normally well insulated building. Condensation will occur whenever the warm air comes into with the surface of pump and pipes containing cold water. To prevent the onset of corrosion, the humidity level should be maintained below 50%. A dehumidifier will control the humidity level within preset condition in
one or more
rooms. By adopting dehumidification, corrosion and malfunction of electrical switch gear and electronics pump and machinery can be greatly reduced. This also leads to reduced maintenance cost.
•
MUSEUMS moisture is one of the many threats against us in our fight to preserve the antique object that make up preserve, lines and other items made of organic materials contain micro-organism which thrive and multiply in high humidity condition, causing damage by mould and fungus growth. Metallic object of all type are susceptible to corrosive degradation in the presence of high humidity condition, causing irreparable damage in some instance.
To avoid expensive and complicated restoration costs, the condition that promotes the damage should be avoided. If the relative humidity is kept within controlled limit, no microorganism or bacteria activity will occur, no corrosion will form on metallic surfaces ensuring that heritage is preserved for further.
8.2 ADDITIONAL RESEARCH Additional research is recommended in the following areas: 1) Evaluate alternative solar tile roof components to establish the most cost effective summer outlet temperature for the solar roof when ing desiccant regeneration. 2) Prepare a desiccant wheel that is optimized to the outlet temperatures of the solar roof. 3) Assemble the components in an operational prototype and test for cooling performance in a suburban setting.
9.0 RESULT AND CONCLUSION The man aim of the study was to investigate change in energy consumption resulting from the use of the hybrid system instead of normal vapour compression unit. The study also compare the energy consumption of these two system with the third option which is the combination of PHE and vapour compression unit is used due the difference in the quality of energy formed being used to run the system, the comparison are made on the basis of energy use and primary energy used. In doing this it is assumed that electricity having thermal energy of 12 Mw\hr. The hybrid cycle can use less energy than a normal vapour compression unit. Considering a case of high effectiveness hybrid cycle meeting the high sensible load. The
average energy saving in the summer and winter conditions are considered is 24%. The saving in resource energy are at least equal to and typically higher than this (27% and40% respectively).the energy saving are the a result of the potential for indirect evaporative cooling which has been used in the cycle to meet the sensible load through the PHE or latent load when the PHE is in conjunction with the desiccant dehumidifier. In almost of the cases the PHE and desiccant dehumidifier can meet the latent load by using only the energy rejected in the condenser of the vapour compression unit for regeneration of the desiccant, when the cooling required is sensible, the PHE can meet a substantial part of it for both climates considered. If the solar energy is used instead of the condenser energy to regenerate the desiccant dehumidifier further energy is possible. The saving is depending on the size of the solar energy system associated with the hybrid cycle. Since solar energy replaces thermal energy needed In the dehumidifier the solar\ hybrid cycle is more promising in the higher latent load and higher ambient humidity cases. Using less effective component also has a significant effect on the hybrid system performance. Considering the case of the cycle meeting a largely sensible load, the energy saving over a vapour compression system drop from 25-12% when the effectiveness drop from the high low values is used. The effect dose not appears as significant as desiccant cooling system. The result indicate that, for the two climate type considered and high sensible load, the hybrid cycle uses 25-40% less energy over January and July than a conventional vapour compression unit.
Bibliography 1) P.
L.
Dhar,
S.
C
Kaushik,
sanjeev
Jain,
Thermodynamics
analysis
of
desiccant augmented evaporative cooling cycle for Indian condition, ASHRAE TRANSACTIONS, 1995. 2) William a Blending, Marc P. F. Delmas, novel desiccant cooling system using indirect evaporative cooler, ASHRAE TRANSACTION, 1997. 3) U.S. Patent 5,651,226 to Archibald dated July 29, 1997. 4) U.S. Patent 5,758,508 to Belding, et.al. dated June 2,1998.
5) John Archibald, Building Integrated Solar Thermal Roofing Systems; History, Current Status, and Future Promise, Proceedings of the ASES Annual Conference, American Solar Energy Society, 1999 Report on Solar Water Heating Quantitative Survey Dec 1997-Sept 1998, Focus Marketing Services, NREL report SR-550-26484, April 1999 6) Energy Information istration, Household Energy Consumption and Expenditures 1993, October 1995.
Website 1) www.americansolar.com
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