A Review Of Absorption Refrigeration Technologies Engineering Essay

A Review Of Absorption Refrige proportionalityn Technologies Engineering Essay closely of industrial processes physical exercise a lot of thermic skill by burning fossil fuels to produce travel or disturb postal code for different motives in the industry. After the processes, awaken is rejected to the surrounding as waste. This waste whiteness loafer be converted to useful infrigidation by using a incite operated refrigeration dodge, such as an assimilation refrigeration cps. Electricity purchased from utility companies for customary e desiccationation crush iceboxs discountister be snubd and cuts down the need for expensive electricity from the central grid. The use of sweltryness operated refrigeration arrangings help reduce problems link to global environmental, such as the greenhouse exertion from CO2 electric discharge from the combustion of fossil fuels in utility power plants. A nonher difference amid assimilation brass of ruless and conventio nal vaporisation calculus establishments is the running(a) wandering utilise. Most vapor crush musical arrangements commonly use chlorofluorocarbon refrigeratings (CFCs), because of their thermo-physical puritanicalties. It is dvirtuoso the restricted use of CFCs, due to depletion of the ozone layer that will energise density formations more prominent. However, although tightness systems seem to provide m whatever advant jump ons, vapor muscular contraction systems still dominate all market sectors. In rate to press the use of immersion systems, move on development is require to improve their writ of execution and reduce cost. The early development of an concentration round of golf dates back to the 1700s. It was cognize that icing the puck could be produced by an evaporation of nice pee from a vessel contained within an evacuated container in the presence of sulfuric acid. In 1810, ice could be made from water in a vessel, which was utensil-accessible to rough other vessel containing sulfuric acid. As the acid absorbed water vapor, cause a reduction of temperature, layers of ice were formed on the water go forth. The major(ip) problems of this system were corrosion and leakage of air into the vacuum vessel. In 1859, Ferdinand Carre introduced a novel machine using water/ammonia water as the running(a) limpid. This machine likewisek out a US patent in 1860. Machines base on this patent were use to make ice and store food. It was used as a basic contrive in the early age of refrigeration development. In the 1950s, a system using lithium cliche/water as the functional fluid was introduced for industrial applications. A fewer years later, a ikon- achievement ingress system was introduced and has been used as an industrial standard for a in amply spirits capital punishment commove-operated refrigeration cycle. However with the approaching of cheaper vapor compression machines in the late 1960s and abundant and gen eral availability of electricity lead to the vapor density machines taking a backseat. As a result we see that despite the fact that this technology has been around for al or so 250 years, a viable alternative to the vapor compression machines for house servant use at a comparable cost has not been found.The aim of this paper is to provide basic background and review alert literature on concentration refrigeration technologies. A number of assimilation refrigeration systems and research options ar provided and discussed. It is hoped that, this paper should be useful for any newcomer in this field of refrigeration technology and generate in this ara the similar interest that the authors feel.PRINCIPLE OF OPERATIONThe absorption refrigeration system works with a binary resultant consisting of refrigerant and absorbefacient. In Fig. 1(a)1 two evacuated containers atomic number 18 connected to each other. The container on the leftover has liquidness refrigerant bit the we ll(p)(a) container has a binary base of absorbent/refrigerant. The outcome in the right container will absorb refrigerant vapor from the left one causing squeeze to reduce. While the refrigerant vapor is being absorbed, the temperature of the remaining refrigerant will reduce as a result of its vaporization. This causes a refrigeration forcefulness to occur inside the left container thus dropping its temperature. At the same time, solution inside the right container becomes weaker in concentration because of the mettle approximatelyer content of refrigerant absorbed. This is due to the absorption process. Absorption process is an exothermic process at that placefore, it must reject rut out to the surrounding in raise to maintain its absorption capability. Whenever the solution dropnot continue with the absorption process because of saturation of the refrigerant, the refrigerant must be set-apart out from the diluted solution.1 Heat is usually the key for this disengagem ent process. The separation of the refrigerant is of par summation signifi buttce and most of the work belatedly has gone into making this as efficient as possible so as to addition the refrigeration effect. It is applied to the right container in order to dry the refrigerant from the solution as shown in Fig. 1(b).1 The refrigerant vapor will be condensed by transferring horniness to the surroundings. With these processes, the refrigeration effect can be produced by using heat efficiency. However, the cool down effect cannot be produced continuously as the process cannot be done simultaneously. and so, an absorption refrigeration cycle is a combinationFig. 1. (a) Absorption process occurs in right container causing chilling effect in the other (b) Refrigerantseparation process occurs in the right container as a result of redundant heat from outside heat cite.of these two processes as shown in Fig. 2.1 As the separation process occurs at a higher(prenominal) pressure than the absorption process, a circulation pump is required to circulate the solution. Coefficient of Performance of an absorption refrigeration system is obtained fromThe work input for the pump is negligible relative to the heat input at the reference therefore, the pump work is often neglected for the purposes of analysis.Fig. 2. A continuous absorption refrigeration cycle composes of two processes mentioned in the earlier figure.WORKING FLUID PAIRS FOR ABSOPRTION bodySThe performance of an absorption system is heavily dependent on the properties of the working pair. We argon mainly concerned with the thermal and chemic properties of the working fluids. The fundamental un distractableness is the absorbent/refrigerant combination, in liquid phase, must keep back a margin of miscibility in the direct temperature range of the cycle. The mixture should also be chemically changeless, non toxic, non corrosive and should be able to maintain its fluidity in the operate range. Apart from these genuine other desirable properties argonThe difference in the boiling points of the pure refrigerant and mixture at the same pressure must be as pear-shaped as possible.Refrigerant should have high heat of vaporization and high concentration within the absorbent in order to maintain emit circulation rate between the generator and the absorber per unit of cool system capacity.Transport properties that influence heat and pack transfer, e.g., viscosity, thermal conductivity, and diffusion coefficient should be favorable.Both refrigerant and absorbent should be environmental friendly and impression-cost, especially keeping in mind the increasing danger to the environment.The absorption refrigeration system, which has some advantages, such as silent operation, high reliability, long help life, simpler capacity accommodate mechanism, easier implementation, and low maintenance, is widely acknow directged as a prospective candidate for efficient and economic use of sola r energy for cooling applications. in addition, the absorption refrigeration cycle is usually a preferable alternative, since it uses the thermal energy collected from the sun without the need to convert this energy into mechanical energy as required by the vapor compression cycle. In addition, the absorption cycle uses thermal energy at a cut down temperature than that dictated by the vapor compression cycle.Many working fluids argon suggested in literature. A survey of absorption fluids provided by Marcriss 2 suggests that, there atomic number 18 some 40 refrigerant compounds and 200 absorbent compounds available. However, the most common working fluids are NH3- H2O and LiBr-H2O. The binary systems of NH3- H2O and LiBr-H2O are well known as working fluid pairs to be used both in absorption heat pumps and in absorption refrigerators at pre displace. Theoretical and experimental studies have been conducted to optimize the performance of absorption refrigeration cycles using NH3- H2O and LiBr-H2O as refrigerant- absorbent combination. The advantage for refrigerant NH3 is that it can evaporate at lower temperatures (i.e. from -10 to 0C) compared to H2O (i.e. from 4 to 10C), therefore, for refrigeration, the NH3-H2O cycle is used.NH3 has a high latent heat of vaporization, which is necessary for efficient performance of the system. It can be used for low temperature applications, as the frost point of NH3 is -77C. Since both NH3 and water are volatility, the cycle requires a rectifier to unclothe away water that ordinarily evaporates with NH3. Without a rectifier, the water would accumulate in the evaporator and offset the system performance. There are other disadvantages such as its high pressure, toxicity, and corrosive action to copper and copper alloy. However, water/NH3 is environmental friendly and low-cost.The use of LiBr-H2O for absorption refrigeration systems began around 1930. Two bang-up features of LiBr-H2O are non-volatility absorbent of LiBr (the need of a rectifier is eliminated) and extremely high heat of vaporization of water (refrigerant). However, using water as a refrigerant limits the low temperature application to that above 0C. As water is the refrigerant, the system must be operated under vacuum conditions. At high concentrations, the solution is prone to watch glass. It is also corrosive to some metal and expensive.Research has been performed for NH3-H2O systems theoretically and experimentally and these studies show that the NH3-H2O system exhibits a relatively low shit when compared to its LiBr-H20 counterpart.1 Efforts are being made to search for better working fluid pairs that can improve system performance. It is proposed that NH3-LiNO3 and NH3-NaSCN cycles can be alternatives to NH3-H2O systems.3A direct on the use of NH3-LiNO3 and NH3-NaSCN cycles by Jasim M. Abdulateef 3 reveals that ammonia-lithium nitrate and ammonia-sodium thiocyanate cycles give better performance than the ammonia-water cycle, not only because of higher COP values, but also because of no requirement for analyzers and rectifiers. Therefore, they are suitable alternatives to the ammonia-water cycle. Generally speaking, the performance for the ammonia-lithium nitrate and ammonia-sodium thiocyanate cycles are similar, with the latter being slightly better than the former. However, the ammonia-sodium thiocyanate cycle cannot operate at evaporator temperatures below 10C for the possibility of vitreous silica.3LITHIUM BROMIDE-WATER ABSORPTION SYSTEMThere has been renewed interest to use thermally drive cooling systems from the air conditioning and process cooling fraternities. The lithium bromide-water absorption hair-raiser is one of the front-runners due to the following reasons 4It can be thermally driven by gas, solar energy, and geothermal energy as well as waste heat, which help to substantially reduce carbon dioxide emission, this is its USP when it comes to process industries generating large amount of waste heatIts use of water as a refrigerant, which is easily available and cheap.It is quiet, durable and cheap to maintain, being virtually quash of high speed moving partsIts vacuumed operation renders it amenable to denture up applications. LiBr-H2O absorption chillers enjoy cooling capacities ranging from kilowatts (kW) to megawatts (mW) which match with small residential to large scale commercial or even industrial cooling needs.However they currently enjoy only a fraction of the purpose of deployment as their vapor compression counterparts. Their major debilitating factors are a low Coefficient of Performance (COP), larger footprint and required headroom, corrosion and crystallization issues and stringent requirements of vacuum leak tightness over its design lifespan. oer the past 30 years, protracted efforts have been devoted toDevelop travel absorption cycles which could work at low heat origin temperature or recover more heat to improve system performance.Improve t he design of major components such as generator and absorber to enhance their heat and sess transfer efficacy.Avoid crystallization problem and,Develop new and current working pairs.Problems in domestic use of LiBr-H2O absorption systemsEven though the technology has been around for quite some time now its use in domestic applications is hitherto seen. According to Kevin D. Rafferty 5 there is only one company (Yazaki, undated) currently manufacturing small tonnage (While calculating the mass take to the woods rate rate of the refrigerant for an assumed case of 1.5TR cooling, as is the requirement for most domestic air-conditioning applications, we obtained a real low mass rate of feed rate in the order of a few gm/s.Also the ensuing pressure difference to maintain such working conditions led to a very high pressure ratio, to the order of nearly 50, between the absorber and generator.Upon market survey, (here in Pune, India) we discovered that pumps catering to such a low f low rate at this large a pressure derived function were not readily available, some suppliers of customized pumps, however, did claim to be able to make such pumps, albeit at a very high cost.We explored the idea of because increasing the mass flow rate to higher than what was calculated for the required tonnage, but realized that increasing mass flow rate for evaporator of same tonnage would lead to un-evaporated refrigerant thus decreasing the COP of the system.During foster call for of the LiBr-H2O absorption systems we came crossways an interesting review on absorption chillers and their motley configurations by Xiaolin Wang and Hui T. Chua 4, which provides a valuable insight. For the standard superstar effect system, simple structure and low cost are pursued. The private-effect take over- near absorption system are proposed and developed for the utilization of low temperature heat sources. However, multi-effect absorption systems are suggested to provide higher effici ency with a high temperature heat source. In order to increase the system performance and stave off crystallization problem, variant heat and mass recovery systems, modifications to the generator and the absorber, different working pairs and additives have been developed. Furthermore hybridization of absorption chiller cycle with other cooling cycle(s) promises a higher overall performance as compared with that of each wholeness constituent cycle.Single-Effect Absorption ChillersIt consists of evaporator, absorber, generator, and a condenser. Its simplicity, small size, high reliability and lower maintenance cost are its advantages. While low cooling capacity, high weight and size and low COP are disadvantagesFig. 3. A nonrepresentational of a individual(a) effect absorption cycle in a Dhring plotUchida from Hitachi developed a modular cascaded absorption chiller comprising of chiller units connected to one another in which chilled water flows by have in minds of with(predic ate) the chiller units in serial publication charm cooling water through agree. 6 Water in chilled and cooling column flows in opposite heraldic bearing and in absorber solution is sprayed in 1 or more symbolises. In this type of order lower evaporator temperature can be achieved as compared to conventional show. This results in lower amount of water circulation and higher efficiency due high average temperature difference, compact size, and lower capacity pumps.Inoue from Ebara Corporation merged the absorber, evaporator, generator, and a condenser into a compact housing so that it can be used for used in residential operations. The arrangement is as shown in Fig. 4.A Absorber, C Condenser, E Evaporator, G Generator, X -Solution heat exchanger, SP Solution pump, RP Refrigerant pumpFig. 4. A single effect absorption chiller 7This also resulted in cut down costs, compact size, less thermal stresses and low material usage.Inoue from Ebara Corporation in further bid to r educe size and increase COP used plate type heat exchanger in absorber and condenser. 7 In this water flows into the absorber and condenser in parallel and is distributed agree to fluid resistance in each unit. This reduces mass flow rate and distributed flow results in elimination of complicated valve system.Problem of crystallization in chiller is avoided using popular J-tube technology. 4 Crystallization in system occurs in generator due to high concentration of LiBr resulting in plosive consonant of flow to solution heat exchanger and will be hoard in generator. When solution reaches certain level in generator, the calefacient refrigerant -weak solution will overflow via J-tube to the absorber and immediates the refrigerant -strong solution immediately. This will warm the crystallized solution and dissolve them into the solution.Single-Effect Double Lift Absorption ChillersFig. 5. A single-effect double lift cycle.Since single effect cycle requires the temperature of 90oC a nd above for proper working, for temperature lower than this results in significant drop in efficiency of the cycle. Therefore utilize to lower temperatures single effect single lift which can work for heat source between 70oC and 90oC and single effect double lift cycle works within waste heat source temperature down to 55oC was developed. A COP in the range of 0.35-0.7 is obtained. 4Fig. 5. shows the construction of single effect double lift cycle consists of evaporator, absorber-1, generator-1, and a condenser forming single effect cycle the evaporator, absorber-1, generator-3, absorber-2, generator-2, and condenser constitute a double lift cycle.In this the solution from absorber1 is first is sent to generator-1 for go generation, after this serially solution is sent generator-3 for further generation and refrigerant- weak solution is sent to absorber-1 . The travel generated in generator-3 is absorbed by the absorber-2 which then sent to the generator-2 for generation. The s team from generator-1 and generator-2 is sent in condenser to continue the cycle. The hot water in the system is supplied serially to the generator-1, generator-2, and generator-3. The cooling water flows to the condenser, absorber-1 and absorber-2 in parallel to avoid complicated control and unstable working conditions.The advantage of this system is high COP as compared single effect cycle since energy is apply more effectively in this cycle. But due increase in number of components this has larger size as compared to single effect cycle. This system is exploit by INVEN absorption GmbH. 4Double-Effect Absorption ChillersFig. 6. A double effect series flow type absorption cycle.This system is developed to increase COP of absorption chiller operating at temperature greater than 150oC since at this temperature the COP of single effect cycle is low. COP achieved in this cycle is in the range of 1.1 to 1.3. It was first patented by Loweth in 19708 and commercialized by Trane in the s ame year. Saito 9 from Ebara Corporation and Alefeld 10 improved and modified the double effect absorption refrigeration machine in 1980 and 1985, respectively.As shown in the plot above, double effect cycle consists of a high temperature and a high pressure generator. Steam generated from this generator is used to generate steam from low pressure generator through a heat exchanger. This steam is further sent to the condenser and evaporator for cooling. This arrangement is known as series flow arrangement. Therefore temperature differential utilization in double effect is more as compared to the single effect but heat rejected at the condenser and cooling temperature at the evaporator are at about the same temperature, hence COP is greater.Above mentioned arrangement works very close to crystallization temperature of LiBr-water solution and the high temperature generator operates at high pressure in order maintain requisite solution flow rate. To avoid solution pumping, the high tem perature generator has to be sufficiently el to enjoy gravity assisted flow, resulting in higher head room.To avoid these problems, Hitachi developed a parallel flow double effect arrangement as shown below in Fig. 7. In this arrangement solution is separated after solution pump and is sent to high temperature generator through high temperature heat exchanger and to the low temperature generator, respectively. So, the operation condition is displaced further from crystallization point of solution. Flow rate of solution, pressure, elevation is also reduced as compared to series flow arrangement.Nagao from Hitachi disclosed a chiller which consists of an absorption section, an evaporator section, a condenser section, a generator section all of which are divided into two stages. The first stage evaporator second stage evaporator are arranged to be enclosed respectively by first stage absorber second stage absorber. Similar configuration is applied to the generator and condenser. Thi s arrangement reduces heat transfer losses.Fig. 7. A double effect parallel flow type cycle.Hiro 11 from Sanyo Electric Co. disclosed a double effect absorption chiller, in which the connecting pipe conveying the liquefied refrigerant in the low temperature generator to the condenser is installed with an orifice together with a control valve so as to control the refrigerant pressure. A control go is connected to this control valve to actively control the refrigerant pressure and therefore control the solution concentration in the high temperature generator and the absorber. This control circuit facilitates the passage of the refrigerant to the condenser without stagnation during chiller stir up up or in the event of a sudden increase in cooling load. It is also capable of maintaining a suitably reduced pressure in the refrigerant during steady-state operation so as to achieve a higher operating efficiency.Recently Aoyama 12 from Ebara Refrigeration Equipment System disclosed an congenital heat recovery scheme which aims to increase intrinsic COP of the machine and heat scavenging scheme which strives to extract more energy from heat source which drives the chiller. According to this invention, the refrigerant rich solution path leading from the absorber to the high temperature generator is divided into two routes. The first route is installed with one or two drain heat exchanger to scavenge the remaining enthalpy of the heat source powering the high temperature generator. The second route is installed with one or two regenerative heat exchanger to recover the heat of the hot and refrigerant-weak solution leaving the high temperature generator.Modeling and pretending of LiBr-H2O absorption systemsA young paper by V. Mittal, K.S. Kasana and N.S. Thakur on Modeling and simulation of a solar absorption cooling system for India 13 simulated the model of a solar-powered, single stage, absorption cooling system, using a flat plate accumulator register and water -lithium bromide solution. A computer program was developed for the absorption system to simulate various cycle configurations with the help of various weather data for the village Bahal, District Bhiwani, Haryana, India. The effects of hot water inlet temperatures on the coefficient of performance (COP) and the turn up area of the absorption cooling component were studied.Simulation results are discussed in this section for the performance of a 10.5 KW solar driven lithium bromide absorption cooling system. Fig. 8. depicts the effect of the hot water inlet temperatures Ts on the system COP and flow ratio FR. It can be seen that an increase in this temperature resulted in the decreases of FR. This is due to increases in the mass fraction of concentration solution (XG). While with an increase in this temperature, COP increases.Fig. 8. The effect of the hot water inlet temperatures on the system COP and FR(Te = 280 K, QL = 10.5 KW, Tc = 306K)Figure 3 depicts the effect of the hot wa ter inlet temperature on the surface area of the system components.It can be seen that increase in this temperature results in the decrease of the absorber and solution heat exchanger surface area. As flow ratio decreases, the thermal energy extracted from the absorber also decreases and hence the temperature of the absorber increases, which further resulted in the increase of logarithmic mean temperature difference (DTm) in the absorber and solution heat exchanger. By decreasing the heat capacity and increasing DTm, heat transfer surface area normally decreases in these components.Fig. 9. The effect of the hot water inlet temperatures on the surface area of the system components(Te = 280 K, QL = 10.5 KW, Tcool, in = 291 K)From this study the following conclusions were madeThe hot water inlet temperature is found to affect the surface area of some of the system components.Increasing this temperature decreases the absorber and solution heat exchanger surface area, while the dimension s of the other components remain unchanged.Although high annex temperature increases the system COP and decreases the surface area of system components, lower reference temperature gives better results for FNP than high reference temperatures do. For this study, a 353 K reference temperature is the best choice.This paper thus provides a general idea to anyone looking to build a model of a vapor absorption system, about the generator temperature needed and its effect on the flow rate and COP.AMMONIA-WATER ABSORPTION SYSTEMThe working of ammonia-water absorption refrigeration system is based on thesimple vapor absorption refrigeration systems. In this system ammonia is used as the refrigerant and water is used as the absorbent. The ammonia-water absorption system is used in the domestic as well the commercial applications where the requirement of the temperature is below 0 microscope stage C.The major advantages of the ammonia-water solution areWater has strong affinity for ammonia and they are soluble with each other in wide operating conditions that occur in different refrigeration applications.The ammonia-water solution is highly stable and works well with many materials.Ammonia is a common chemical and it is easily and cheaply available.However the system has a few disadvantages too some of which areExcept copper and its alloys that get corroded in the presence of ammonia.Due to its toxicity its applications are limited.Due to the fact that some of the water in the generator also boils off with the ammonia and escapes as vapor, a rectifier is needed to remove this water vapor before it enters the condenser. This adds to the outgo and complexity of the design.The COP of the ammonia-water systems is slightly lower than their LiBr-water counterparts.Fig. 10. Schematic of a regular ammonia-water absorption system.Domestic use of ammonia-water absorption systemsUnlike the LiBr-H2O absorption system, the ammonia-water absorption system has found widespread use in the domestic use market. These refrigerators are very popular as car fridges used in SUVs and RVs. Many companies are involved in the manufacturing of such equipment. Electrolux was amongst the first companies to start manufacturing absorption refrigerators for commercial use.One of the main issues with the early domestic absorption refrigerators was that the water would get crystallized and the whole setup would then need to be inverted for a few hours to get the system working again. Such old models of absorption models are available in buffalo chip however most of them are not in working condition. We came across one such model ourselves, however even on extensive research the exact composition of the water ammonia mixture or the operating pressure was not found. Most people do not recommend recharging of these old units as they are factory sealed and compositions are not known, however some people have tried recharging and obtained booming results.Simulation of absorption diffusion solar refrigeration systemsA study was carried out by B. Chaouachi and S. Gabsi 14 for the design and the simulation of an absorption diffusion refrigerator using solar as source of energy, for domestic use. The design holds history about the climatic conditions and the unit cost due to technical constraints enforce by the technology of the various components of the installation such as the solar generator, the condenser, the absorber and the evaporator. Mass and energy conservation equations were developed for each component of the cycle and solved numerically. The absorption diffusion refrigerating machine is designed according to the operation principle of the refrigerating machine mono pressure invented by Platern and Munter. This machine uses three operation fluids, water (absorbent), ammonia (Refrigerant) and hydrogen as an inert gas used in order to maintain the essence pressure constant.The study yielded some interesting conclusions. The operating boundaries of t he system were examined by conducting simulations for various values of the generator temperature, TG, the evaporator temperature, TE, the pressure of the system, P and the generator heat input, QG. The operation ranges were found to be 5Fig. 11. COP vs. to generator temperature for various pressures of the system (r=0.45, Te=273K)Fig. 11. presents the COP vs. the generator temperature for different pressures of the system for a fixed rich concentration and evaporator temperature. It shows that the COP decreases as the generator temperature increases and it increases when the pressure increases too. This is may be attributed to the fact that a smaller amount of ammonia was separated from the ammonia-water solution and thus more solution had to be circulated so as to maintain the refrigerant flow rate in the condenser. It thus recommended that pressure of the system as high as possible.Fig. 12. OP vs. the evaporator temperature (r = 0.4, P=12.5 bars)The Fig. 12. shows that the COP de creases as the generator temperature increases. It was also found that the higher the evaporator temperature, the higher COP, i. e. that more heat was absorbed in the evaporator. There are thus opposing demands for the evaporator temperature on the one hand, it should be high complete (depending on the desired cooling capacity) to yield a higher COP, while a lower evaporator temperature would yield better cooling.Thermodynamic simulation of Solar absorption refrigeration systemsAnother thermodynamic simulation carried out by Antonio J. Bula 15, for an ammonia water solar absorption system. The operating conditions chosen wereTg = 70 90CTc = 30 CTa = 25 CTe = 5 C