ࡱ> uwtF5@ %bjbj22 "XX+;  ===8=t\> x2>A(AAAMMMsuuuuuu$R PL"MPPAAA 2dddP A AsdPsddeD > A> @mL?=\lc&/DH0x"ĐXcL  MMdN|OMMM /=d =AVAILABLE ENERGY OF THE AIR IN SOLAR CHIMNEYS AND THE POSSIBILITY OF ITS GROUND-LEVEL CONCENTRATION N. Ninic - Faculty of Electrical Engineering, Mechanical Engineering and Naval Architecture in Split, Croatia Abstract Solar chimneys are described as low temperature solar thermal power plants, which use the atmospheric air as a working fluid, where only one part of the thermodynamic cycle is utilized within the plant. The available work potential that atmospheric air acquires while passing through the collector has been determined and analysed. The dependence of the work potential of the air flowing into the air collector on the heat gained inside the collector, air humidity and atmospheric pressure as a function of elevation is determined. Various collector types using dry and humid air have been analyzed. The influence of various chimneys and different plant efficiencies on the air work potential is established. The possible higher utilization factors of the available hot air energy potential without use of high solid chimneys were discussed. It has been shown that vortex flow motion downstream of the turbine maintains under pressure and can possibly take over the role of the solid structure chimney. Thus, a part of an available energy potential acquired in the collector will be used to maintain the vortex flow in the air column above the ground-level turbine. Basic conditions for the maintenance of such a flow regime are described and compared to the phenomenon of a tornado. INTRODUCTION Solar thermal power plants can be roughly classified by their characteristics in two categories, dependent on the temperature level, to high and low temperature power plants. High temperature solar power plants collect direct solar radiation by means of solar concentrators and use a closed thermodynamic process, where the whole process takes place within the plant itself. These plants are characterized by relatively high efficiency, but unfortunately also by high capital costs. They also have higher operational costs, which are mostly due to measures which are used to compensate the short and long time fluctuations of the solar radiation input. Low temperature power plants, which are typically in use, are hydro and wind power plants, where the cycle of the working fluid is kept predominantly in the free atmosphere. Capital costs per power unit are also relatively high for such plants since the working potential, which is spontaneously created in the atmosphere, is not concentrated. Solar thermal power plants based on solar chimneys (SC) by characteristics are closer to low temperature power plants. A survey of technical characteristics, costs and environmental impacts of diverse solar power plants, as well as the survey of regions of different solar radiation levels was given earlier by Trieb (1997). Power plants using solar chimneys have not been built yet, but the operating and design characteristics of such plants have been tested on the prototype which was built in Manzanares, in Spain. Data regarding the structure and operating capabilities of this prototype were given by Haaf (1983,1984). Profitability analysis of SC power plants, based on the experience acquired by the plant prototype with regard the operating capabilities was described by Schlaich (1995). Schlaich has shown that SC plants are presently competitive for global radiation in excess of 1950 kWh/m2a. Areas of such radiation level comprise a great part of Africa, the Near East and the whole of southwestern Asia with a considerable part of India, as well as a great part of Australia and parts of North and South America. At the electricity price per kWh, as assessed by Schlaich (1995), SC plants could even cope with the long distance transfer losses of generated electric power, e.g. between the Sahara and Central Europe, and have the potential to become one of the global energy sources. The principle of operation and performance characteristics of a typical SC power plant are described along with the plant crosssectional view, based on the power plant project described by Schlaich (1995). In Fig.1, the ground is denoted by A, glass roof (single-layer and in the higher air temperature zone double-layer) of the solar air collector is marked by B, chimney marked by C, in which air (heated in the air collector) is exerted and drawn by the buoyancy force and D denotes the block of air turbines together with a genetator set at the basement of the chimney. The nominal chimney, as shown in Fig.1, is 950m high and 115m in diameter. The incident solar radiation of 2300kWh/m2a was supposed as nominal. In the nominal case, air temperature in the air collector is increased by about 36C, the collector efficiency amounts to  EMBED Equation.DSMT4 , the turbine pressure drop is assumed to be about 900Pa, the total friction loss of the collector at the chimney's outlet amounts to 80Pa, the kinetic energy loss at the chimney's outlet amounts to 120Pa (at the air velocity of 15m/s). It was anticipated that 10% of the total power generated was gained by the accumulated ground heat. Adiabatic processes in the turbine and ''chimney'' are part of the Brayton cycle. In this cycle, the collector air rises through turbine and the chimney to the atmosphere in the presence of the gravitational field. The overall SC power plant efficiency was assessed to be 1.3%. In our case, the process taking place in the turbine differs considerably from the process in the wind turbine, where the pressure drop of 900Pa, by kinetic energy utilization of 60%, corresponds to a wind speed of about 200km/h. Figure 1. Crosssection of the SC power plant with 100MW nominal power Although requiring high global radiation and capital costs, SC power plants would also have some important advantages, like a long service lifetime lasting several decades, application of technology allowing utilization of local material and human resources, as well as the utilization of a solar collector area at the peripheral as a greenhouse and/or dryer. AVAILABLE ENERGY OF THE COLLECTOR AIR Standard thermodynamic analysis of solar chimneys was given by Schleich (1995) and Gannon (2000). By use of the optimal thermodynamic process, for given dimensions of solar collectors and height of the chimney, the maximum obtainable thermal power is determined by relation  EMBED Equation.DSMT4 . (1) Here: G is an instantaneous global solar radiation falling upon the unit area [W/m2], Acoll is the collector area [m2],  EMBED Equation.DSMT4  is the solar air collector efficiency,  EMBED Equation.DSMT4  is the efficiency based on the ideal Brayton cycle, where its thermodynamic parameters are determined by the height of the chimney and temperatures at the collector inlet and outlet, and  EMBED Equation.DSMT4  is the turbine efficiency. The turbine efficiency takes partly into account the non ideal cycle properties reducing the turbine work by the kinetic energy of the air at the turbine outlet, which is approximately equal to that one at the chimney outlet. In a standard theoretical approach based on eq.(1), one type of hot air utilization was adopted. In general, this type when implemented with a solid chimney, does not provide an adequate basis for the analysis of optimum engineering solutions. Our goal was to maximize the output of technical work from the air flow, which leaves the collector and disperses into the atmosphere. Maximum work, that can be produced by bringing a fluid in equilibrium with the environment is exergy (Bonjakovi 1965) defined by:  EMBED Equation.DSMT4  (2) where  0 denotes the state of the air in a thermodynamic equilibrium with an environment. The environment is usually taken as the air at the bottom of the atmosphere. In the case of the SC, the upper layers of the atmosphere can be considered as an indefinite number of environments. A detailed analysis, based on the eq.(2), in a Mollier h-s diagram is shown in Fig.2. Figure 2. Exergy and its technically feasible part Here: C - represents the state of air at the collector output, and O - represents the state of air in a mechanical and thermal equilibrium with an environment. In the mechanical equilibrium of the collector and ambient air exposed to a gravitation field, the collector and ambient air are exerted to the same pressure and force of buoyancy equals zero. This equilibrium state in Fig.2 is denoted by O'''. The exergy CO'', as given by eq. (2) shows a maximally available technical work. One of its mutually equivalent equilibrium transition could be performed by the adiabatic process CO''', and followed by the isobar O'''O transition, along with a reversible utilization of the heat quantity Cp(TO''' T0). This utilization, for example, could be performed by means of a sequence of Carnot cycles between the isobar of p=p0 and isotherm T=T0. The Carnot cycles would result in an additional work O'''O'', and the overall work equals to hcoll hO''. However, any kind of controlled heat exchange above ground level is technically not feasible, and therefore that portion of exergy is also technically not feasible. Thus, for overall work it follows ecoll tech = hcoll ho (3) Index tech is used to denote the technically feasible part of exergy ecoll. The specific enthalpy of the collector air at the atmospheric pressure and height H, where the buoyancy force disappears is denoted by hO'''. In such state, the collector air was considered to be in an equilibrium with the environment. Although this equilibrium is only mechanical, the still existing temperature imbalance in this state cannot be technically used. The CO''' process shown in Fig.2 is the adiabatic transition in the gravitational field. The first law of thermodynamics for the moving observer doesn't take into account the potential energy change. Hence, the net executed work of the collector air becomes  EMBED Equation.DSMT4 , (4) and finally  EMBED Equation.DSMT4 . (5) The same result could be derived even if we did not start from eq.(3). According to the second law of thermodynamics to which all the reversible processes are mutually equivalent, it is sufficient to calculate the work for one of these processes. Such an imaginary process would be an adiabatic elevation of a unit portion of the collector air under the buoyancy force, wherefrom directly follows the equation (5). With presently unspecified upper endpoint, the height H, the integral equation (5) is the required equation which shows the maximum technically feasible net work output. In other words,  EMBED Equation.3  is the height potential of the collector air. HEIGHT POTENTIAL IN THE STANDARD ATMOSPHERE Regarding the relationship per height for pressure, temperature and air density, the reference atmospheric profile as adopted here, corresponds to the parameters of the International Standard Atmosphere SA73 or US Standard Atmosphere (NOAA 1976). It represents mean values at the geographical latitude of 45, within an average activity of the Sun. The height dependence of pressure and volume are shown in Fig. 3 by curve OA. Curves OB and O'C, for the same pressure relationship by altitude OA, represent a distribution of densities at an adiabatic quasi-static elevation of dry air having initial temperatures of 15C and 45C, respectively (curves OB and O'C). The narrow wedgeshaped hatched area OO'F between the curves OA and O'C represents, according to eq. (5), the maximally available net technical work of dry air in the standard atmosphere at a ground temperature of 45C. At the intersection of curves OA and O'C (point F), the buoyancy force, in relation to the local atmosphere, disappears at the maximal elevation height of H = HF = 7000 m. Thus, point F automatically determines the upper boundary of the integral in the equation (5). However, in accordance with Fig.3, the height of an air layer of tropopause, which is the boundary between troposphere and stratosphere, can be taken as a final elevation limit. That specific height can be applied only if there are no other intersections of curves OA and curves of adiabatic elevation of collector air at some of the lower altitudes. Homogeneity of atmospheric temperature above the tropopause is equivalent to the state of intensive air mixing, which destructs any possible residual exergy of the collector air. The elevation of such characteristics is about 10000m. Figure 3 Standard atmospheric and isentropic specific volume profiles The area beneath the OF curve along the ordinate equals the specific potential energy in the gravitational field at the height HF, i.e. 68670J/kg. To prove it, let us suppose the isotropic fluid is lifted up (with no buoyancy force), while all the expansion work (area along the ordinate) tends to increase the potential energy. If the collector air expands according to the curve OF, the tech area along the ordinate is the technically feasible exergy ecoll tech; and net work e EMBED Equation.DSMT4  equals the hatched area OOF. By integration of the OOF area, the height potential (i.e.the net work) of the dry air in a the standard atmosphere having a ground level temperature of 45C could be calculated giving the result of  EMBED Equation.DSMT4 . Michaud (1999), who started directly from eq. (3), obtained similar results in a different way. There are only numerically different due to different parameters of calculation. THE ROLE OF THE SOLID CHIMNEY The act of the buoyancy force on a fraction of hot air have their origin in a pressure difference below and above that fraction of air, which is determined by the surrounding atmosphere. However, if we imagine the elevating air as separate from the surrounding atmosphere by a solid structure chimney of height Hc, the chimney will eliminate pressure differences all along its length, and will keep the hot air separate from the surrounding atmosphere. That way, the chimney will be summing up all elementary pressure differences developed at its bottom, resulting in density differences between th e internal hot air and external atmospheric air on the bottom of the chimney. The accumulated pressure difference developed with regard to the surrounding atmosphere, amounts to  EMBED Equation.DSMT4 . That pressure difference is linked to the maximal work output of the collector air in the following way:  EMBED Equation.3  EMBED Equation.DSMT4  (6) In the diagram shown in Fig.3. and enlarged in Fig. 3.a length OH represents the contour line of zero height for atmospheric and collector air at the bottom of the chimney height of HC = 1000m corresponding to the pressure difference of  EMBED Equation.DSMT4 . Fig. 3.a Enlarged figure of chimney role in ground-level concentration of the height potential Based on eq. (6), the two areas,  EMBED Equation.3 as shown in the diagram Fig.3. and Fig. 3.a are equal large. The ratio between the theoretical work available from the chimney of height HC, according to Fig.3 and the heat assumed in the collector can be taken as definition of the chimneys efficiency. It may be suggested to describe the above ratio as a buoyancy conversion efficiency  EMBED Equation.DSMT4  and shown as a product with two factors  EMBED Equation.DSMT4  (7) where  EMBED Equation.DSMT4  and  EMBED Equation.DSMT4  are theoretical and relative chimney efficiencies, respectively. The theoretical efficiency is ratio between height potential of the collector air and the heat assumed in collector. The relative chimney efficiency takes into account the limited height of the chimney. In the particular case  EMBED Equation.DSMT4  and  EMBED Equation.DSMT4  are obtained, and the buoyancy conversion efficiency of  EMBED Equation.DSMT4  is derived. Schleich (1995) and Michaud (1999) for  EMBED Equation.DSMT4  quoted the approximate equation:  EMBED Equation.DSMT4  (8) which gives  EMBED Equation.DSMT4 . The reasons for the different results as obtained by equations (7) and (8) are different reference profile of atmospheric pressure vs. height taken earlier by the two authors, and the aberrance of eq. (8) from the more accurate eq.(7). According to Fig.3, the buoyancy efficiency is roughly proportional to the chimney height up to HC,max = 3000 m, which already exceeds the technical design possibilities of the solid structure chimney. In general, considering the height potential utilization, eq. (8) becomes quite useless. For example for HC = 7000m, which is the upper elevation height, the eq. (8) shows an error of approximately 100% . The present analysis shows in headlines how to work out the calculation of the exergy (maximum work output) of the collector air from the net technically feasible potential and separate it from the achievable potential  EMBED Equation.3 , if chimneys made of reinforced concrete, were used. THE IMPACT OF HUMIDITY ON THE HEIGHT POTENTIAL The presence of humidity in the collector air would certainly increase its operating potential due to the condensation of a moisture, thus slowing down the adiabatic decrease of temperature and speed up the density decrease of ascending air. The change of the air moisture content at its equilibrium adiabatic expansion can be calculated by use of its entropy as a function of the pressure, temperature and humidity. The approximate graphic procedure was suggested by Bosnjakovic (1965), and the results obtained for saturated air at the temperature of 45 C are given by curve O''E in Fig.3. In such a way, the condensed moisture has been included into the density, as if it had not been separated from the air flow. Net technically feasible part of exergy corresponds now to the area OO''EA, which is substantially larger (10360J/kg) than the one for the dry air at the same initial temperature (3735J/kg). Even in the case of a relatively modest chimney height of 1000m, which is technically possible with solid structure workmanship, the work output availability is about 62 % higher, and amounts to 1480 instead of 912J/kg. However, by moistening a dry collector air at the temperature of 15C in order to get it saturated at the temperature of 45C, the solar radiation heat of 200kJ/kg must be available and given up to the collector air, which is more than six times in excess of the solar energy needed by a dry collector air for the same change of temperature. In comparison, the theoretical buoyancy efficiency of the solar collector filled by dry air amounts to 0.124, whereas for a collector with hot saturated air, it amounts to only 0.050. Concequently, from the point of view of overall system efficiency, the collector air moistering up to its saturation level at the collector outlet would not be profitable. On the other hand, the moisture content of the air at the given temperature at the collector inlet should be as high as possible. The results of impact analysis of air humidity at the collector inlet on the change of its specific volume in the course of the adiabatic elevation are shown as a bundle of curves O'D in Fig.3. If relative humidity at the collector inlet increases from 30 to 90%, the curve bundle will slightly separate from the dry air curve O'C. In addition, the intersection point F disappears and looks like a bottleneck in the height potential. A major increase of work potential increasing the humidity can only be reached at elevations above 7000m. The influence of the temperature and relative humidity at the collector outlet on the exergy potential have been additionally analysed and its results are shown in Fig.4. The two curves for dry and 18% humid air at the temperature of 40C at the collector outlet show the change of air pressure and volume vs. height. The hatched areas between these two curves and reference atmospheric conditions curve SA-73, represent the available net technically feasible part of exergy. Figure 4. Influence of air temperature and humidity variation on a net technically feasible part of exergy For tcoll = 40 C and (coll = 0, e EMBED Equation.DSMT4 ( 2630 J/kg , end for tcoll = 40 C and (coll = 18%, e EMBED Equation.DSMT4 ( 5370J/kg. The results obtained from the analysis of the air collector height potential by taking into account diverse ways contributing to overall humidity are summerized as follows: 1. The overall height potential of the collector dry air is several times higher than that encountered in conventional SC plants using solid chimneys. 2. The height potential will be considerably increased if the air at the collector inlet is moisturized. The more humid the collector air, the higher the exergy, but is accompanied by a decrease of the overall theoretical efficiency. 3. Theoretical efficiency can be increased by use of saturated air at the collector inlet temperature along with a drying process in the collector by solar heat. The addition of water into a collector would decrease its theoretical efficiency, but could contribute to a certain gain, e.g. from the simultaneous greenhouse production in the peripheral parts of the collector. In this case the collector peripherals would act as a greenhouse with intensive irrigation, where tall green vegetation act as a filling for air humidification. At the same time, there would be neither need for any chemical water treatment, nor would there be any kind of water cleansing having some adverse ecological impact. Such SC plants could use some surface water bodies like lakes and rivers in order to compensate for the evaporated water. POSSIBILITY OF GROUND-LEVEL CONCENTRATION OF THE HEIGHT POTENTIAL According to the results described above, a solid structure chimney can reach only a small part of an overall height potential of the collector air. Consequently, such a type of construction cannot be considered satisfactory from the thermodynamic point of view. At the same time, the solid structure SC plant is rather demanding when taking into account the construction engineering, materials, safety measures and high investment costs. Chapters 2, 5, and 6 have dealt with a technically feasible height potential. In this chapter we are going to deal with an idea how to use that potential. In order to exploit it, the potential should be available at the ground level, which is the only place where turbines can be placed. If we exclude option of building very high and robust chimneys, another possibility of achieving the height potential ground level concentration could be by creating a special velocity field above the ground-level plant. The velocity field would have to keep the turbine back pressure lower than the pressure of the surrounding atmosphere, which as a result enables the net turbine work. One could imagine a kind of inertial bottle for whose maintenance one part of the height potential would be consumed, whereas the remaining part of the available potential could be utilized in the turbine. A type of such a bottle, characterized by a substantial impact of air friction with ground, was suggested by Michaud (1999) under the name of vortex. However, he did not take into account the full thermodynamic aspect of the process. The type of plant in which the collector process would be a part of the Brayton cycle in the gravitational field has been suggested by Ninic (2000). In such a plant the role of friction with the ground is not essential. According to the latter variant an inertial bottle is represented by the vertical vortex column in the gravitation field in whose axis the pressure would be lower than in the surrounding atmosphere at the same elevation. The structure of the bottle wall in the vertical cross-section would be quite complex. The radial pressure difference existing between an external and internal circular wall would be brought into equilibrium by a centrifugal force that affects the corresponding ringlike mass in accordance to the relation  EMBED Equation.DSMT4 . In the gravitation field the pressure difference would rise when going downwards from the vortex top and it will be concentrated at the ground level, where the turbines are situated in the ringlike base of such a gravitation vortex column (GVC). The GVC height should be much greater than the height of any solid structure chimney, possibly up to the upper level of the troposphere (confer the point D and E in Fig.3.). The crucial evaluation of the Ninic GVC concept runs like a question: if it is generally possible to generate and maintain such a circular flow motion of air having as small as possible energy dissipation along the vertical boundary layer, due to a turbulent friction, which could destroy such a vortex motion much sooner than it could reach the upper layers of the troposphere. In the physical GVC model which was developed the following was of utmost importance: The process going on in GVC is a primary thermodynamic phenomenon, and thermodynamic premises of somewhat wider scope than those dealt within the Chapter 2 are necessary for designing a physical and mathematical GVC model. Dissipation intensity of the angular momentum into the surrounding atmosphere shall be relatively small, either due to flow stability (laminary) on the GVC periphery or due to the induced low inward radial velocity component on the periphery, or due to both. In any case there are observations regarding the tornado vortex, which indicate the existence of angular momentum radial conservation mechanisms. There is a close analogy between the above described gravitational vortex column and the tornado phenomenon in certain atmospheric conditions. Describing the atmospheric circumstances that correspond to the first of the above quoted prerequisites, the concept of convective available potential energy (CAPE) has been introduced in meteorology. The definition of CAPE is identical with the net technically feasible part of exergy. The range of the CAPE criteria calculated on the basis of atmospheric measurements as the first prerequisite for occurrence of a tornado is very broad. Thus Renno (1996) quotes the CAPE mean value for the tropical belt amounting to 1000J/kg, and Garner (2002) quotes that in the operating zone of the developed tornado CAPE amounts from 966 to 6142J/kg. According to these measurements and the calculations in Chapter 2, dry air heated to 45C would have CAPE (3735J/kg), which according to the basic criteria would be sufficient for the maintenance of a tornado-like vortex, even with dry air in a standard atmosphere. CONCLUSION The article is based on the published theoretical tenets and on the key results regarding the evaluation of SC power plants with solid structure chimneys. For maximally available work output, defined as the operating potential of the collector air in the standard atmosphere, it was shown to be considerably larger than that one theoretically obtained in SC designs with solid chimneys. The impact of air humidity on the increase of the operating potential and efficiency of the whole plant has also been analyzed. Finally, the technical possibility of utilizing the total operating potential was suggested partly for generation of the turbine work, and partly for the maintenance of the GVC air flow structure above the ground-level of the SC power plant. Basic assumptions preceding GVC physical modeling were provided. A considerable analogy existing between GVC - flow structure and natural tornados thereby plays the role of an almost experimental confirmation of the effect that the implementation of the proposed GVC structure is also technically feasible. NOMENCLATURE A m2 irradiated collector surface Cp J/kgK specific heat air capacity ecoll J/kg exergy (maximum technically work output, availability) of air at the collector outlet ecoll tech J/kg technically feasible part of exergy  EMBED Equation.DSMT4  J/kg net technically feasible ( part of ) exergy  EMBED Equation.DSMT4  J/kg maximal net work output for solid chimney g m/s2 gravitation acceleration G W/m2 density of overall sun radiation h J/kg specific enthalpy hcoll J/kg air enthalpy with the collector outlet h0 J/kg specific enthalpy of the collector air in thermodynamic equilibrium with atmosphere Hmax m maximum height reached by the collector air HC m chimney height  EMBED Equation.DSMT4  kg/s mass air flow pa Pa atmospheric pressure pcoll Pa pressure at the collector outlet p0 Pa collector air pressure in equilibrium with the atmosphere (at H = Hmax) P W turbine power R m mean radius of GVC shell s0 J/kgK air entropy in equilibrium with the environment T0 K environment temperature u m/s mean circular velocity of GVC - shell uC m/s air speed at the turbine outlet va m3/kg air volume in the atmosphere vcoll m3/kg volume of the collector air z m height  effective absorption coefficient of the collector b W/m2K convective heat transfer coefficient ( m thickness of GVC shell DpC Pa pressure differences at the bottom of the chimney of the height H Dpr Pa radial pressure difference  EMBED Equation.DSMT4  Pa pressure drop equivalent to kinetic energy at the chimney inlet Dtcoll C increase of air temperature in the collector hbuoy efficiency of buoyancy energy conversion  EMBED Equation.DSMT4  theoretical efficiency of buoyancy energy conversion  EMBED Equation.DSMT4  relative efficiency of the chimney hc theoretical efficiency of the chimney (i.e. of the Brayton cycle implemented by the chimney) hcoll collector efficiency ht turbine efficiency (coll % relative humidity collector outlet ( kg/m3 mean density of GVC shell ra kg/m3 density of atmospheric air rc kg/m3 air density at chimney inlet Acknowledgements: The author wishes to thank the Ministry of Science and Technology of the Republic of Croatia for support in this work. REFERENCES Boanjakovi, F. (1965): Technical thermodynamics, pp.326-331. Holt, Reinhart and Winston, New York. Gannon, A.J, Backstrom, Th.W.V.: Solar tower cycle analysis with system loss and solar collector performance. Proceedings of the ASME International solar energy conference Solar 2000: Solar Powers Life Share in Energy, June 16-21, 2000, Madison Wisconsin Garner, J.M., Thalken, B.W. (2002): Evaluation of an experimental tornado index.  HYPERLINK "http://www.garnerchase.net/tornado index.html" http://www.garnerchase.net/tornado index.html. Haaf, W., Fiedrich K., Mayr, G. and Schlaich J. (1983) Solar towers Part I: Principle and construction of the pilot plant Manzanares : Solar Energy 2. 3 20. Haaf, W., (1983) Solar towers, part II: Preliminary test results form the Manzanares pilot plant Solar Energy 2 141-161 Michaud, L.M. (1999): Vortex process for capturing mechanical energy during upward heat convection in the atmosphere, Applied energy 62, 241-251 Ninic, N. (2000): Solar power plant including a gravitational air vortex, P-20000385 A, Croatian intellectual property gazette, No 1, 2002. 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