Parametric Studies of a Hybrid Desiccant Cooling System

With the drastically change in climatic conditions in recent years, demand for air conditioning is spreading all over the world. Th is causes a primary consumption of energy in high quantity. In order to provide the best indoor air quality and thermal comfort with min imum consumption of energy, the hybrid desiccant cooling system is one of the options in our daily life. In this paper, an experimental performance study has been done on the hybrid desiccant cooling system. The effects of various parameters on performance of the system have also been observed. It is found that the influence of the parameters studied on the dehumid ification rate is similar to those reported earlier.


Introduction
The liquid desiccant air-conditioning system utilizes low grade heat energy and is env iron mentally friend ly . The dehumidifier and regenerator are the key co mponents of the hybrid desiccant cooling system. The hybrid cooling system cons ists o f a vapou r co mp ress ion system, efficient in sensible cooling, and desiccant dehumidifiers, efficient in removing latent heat load. On combin ing the two systems we get a hybrid system. This concept has been proposed by several investigators including Meckler [13] and Schlepp and Schultz [12]. Meckler [13] has designed and installed several air conditioning systems that integrate solid or liquid desiccant dehumidifiers with conventional vapour compression systems for air conditioning of co mmercial and institutional buildings. Integration of commercially availab le dehumidifiers for latent heat removal and conventional vapour compression systems for sensible heat removal for supermarket applications is economical today.
Alizadeh et al. [11] designed, optimized and constructed a prototype of a forced flow solar collector/Regenerator. They emp loyed an aqueous solution of calciu m chloride as desiccant and studied the influence of parameters, such as air and desiccant solution flow rates as well as the climat ic conditions on the regenerator's performance. The performance of a regenerator was measured by the rate at which it removed water vapour fro m the weak desiccant solution. The conclusion reached in that study was that the performance of the regenerator increased as the air flow-rate increased. The solar co llector efficiency generally increased with the increase of the air mass flow-rate. The existence of an optimu m value of the air flow-rate at which the efficiency is maximal was also predicted. A strong influence of the solar insolation on the collector/regenerator thermal performance was noticed. Yadav [2] simulated a hybrid desiccant cooling system comp rising the tradit ional vapour compression air conditioning system coupled with a liquid desiccant dehumidifier which was regenerated by solar energy. The study suggested that, when the latent load constitutes 90% of the total cooling load, the system can generate up to 80% of energy savings. Dai et al. [4] conducted a comparative study of a standalone VCS, the desiccant-associated VCS, and the desiccant and evaporative cooling associated VCS. The authors found an increase of cold production by 38.8-76% and that of COP by 20-30%. Mazzei et al. [8] co mpared the operating costs of the desiccant and traditional systems using the computer simu lation tool and predicted operating cost savings of about 35% and a reduction of thermal power up to 52%. In the case were the desiccant would be regenerated by waste heat, the authors projected operating costs savings reaching up to 87%.
Sanjeev et al. [10] studied theoretically and experimentally a liquid desiccant cooling system made of a falling film tubular absorber and a falling film regenerator. For the purpose of performance evaluation, the authors defined wetness factors to characterise the uniformity of wetting of the surface of the contactors (dehumid ifier and regenerator) by the desiccant solution. Their study is of g reat interest for designing viewpoint, as it can help calculate more accurately the size of the contactors. Kadoma et al. [7] investigated the impact of the desiccant wheel speed, air velocity and regeneration temperature on the COP. The authors showed the existence of an optimal speed and established that the COP decreased when the airflow rate increased and, on the contrary, the temperature of regeneration and the cooling capacity had the same evolution tendency.
Various authors have done parametric study and optimized the performance o f the hybrid desiccant cooling systems. Giovanni Angrisani and Francesco Minichiello [14] optimized a desiccant HVA C system coupled to a small size co-generator where they concluded that the performances of the two systems are strongly influenced by outdoor therma l-hygro metric conditions and guaranteed a primary energy saving when outdoor air hu midity ratio is lo wer than a certain value (11.5 g/kg) and outdoor air temperature is in the range 25 -36 ℃. Later in 2011, Avadhesh Yadav and V.K.Bajpai [15] founded that the 10RPH and 20RPH are the optimu m parameter of desiccant wheel for the rotation speed. This study was carried out to evaluate the dehumid ification rate of air in a dehumidifier packed tower structure using the liquid desiccant H2O/CaCl 2 and by varying the liquid desiccant, airflo w rates, in let air and desiccant conditions. In the present study, the performance as well as parametric study for a hybrid desiccant cooling system has been done. The experiments were performed at Renewab le Energy Lab of Mechanical Eng ineering Depart ment, Institute of Technology, Banaras Hindu University, Varanasi, India.

System Description
The Hybrid desiccant cooling system basically consists of two packed towers (Figure1). One is for absorption and another one is for regeneration. Both towers are in cylindrical in shape and of similar size. The towers are made of up of fibre rein forced plastic (FRP) o f thickness 4 mm and it has a constant height of 100cm .Packing is done using polypropylene cascade ring of specific surface area 205 2 3 � for a height of 30 cm .Beneath both the towers, a collection tank made up o f alu miniu m, fo r storage of the liquid desiccant has been provided. The arrangement fo r the tanks is such that heated desiccant is sprayed on to the regenerator and cool desiccant is sprayed on to the absorber.

Figure 1. Photograph of Experiment Setup
In the absorber, moisture is absorbed from the inco ming air stream, due to the vapour pressure difference between the air and solution. Thereby, the dehumid ification takes place. Fro m the absorber, the desiccant falls into a collection tank where it is heated to an elevated temperature so as to increase its vapour pressure and this heated desiccant is sprayed on to the regenerator where the mo isture is transferred into the air stream. A PT100 sensor is used to sense the temperature of the heated desiccant. The other tank is cooled using an ice which is covered with thermocoal to avoid any heat exchange with surrounding. In the towers, the desiccant and air flo w in a counter current manner. Desiccant is sprayed on to the packing and air moves upward through the packing. For obtaining the airflow, two centrifugal fans of capacity of 10 m 3 / min each, are installed at the entry of the two towers.
Two centrifugal pu mps each with a maximu m discharge of 800 litre /hour are used for pumping the desiccant into the two towers. Desiccant is distributed into the towers by means of multi point distributor made of PVC p ipes and it trickles down through the packing to the outlet, which is situated at the bottom. Demister pads are placed at the top of the two towers to eliminate desiccant carry over through the air stream. The specifications of the measuring devices used are given in Table 1. Once steady state conditions have been attained, the different measurements viz inlet and outlet temperature of the desiccant and air , using calibrated T type thermocouples, inlet and outlet air relat ive hu mid ity using digital capacit ive probe hygrometer in let and outlet desiccant concentration, are measured. In the measurement of concentration of desiccant, weight of a known quantity (100ml) of the desiccant is taken whereby its density is calculated and the concentration is calculated using the correlation developed by Manuel R. Conde [1]. Once these readings are obtained for the dehumidifier, the moisture removal rate is calculated and the effect of the different variables namely air inlet temperature, desiccant inlet temperature solution to air flow ratio is studied. For studying their effect, one variable is changed keeping all others at their mean values and their effects are studied for both absorber and regenerator.

Mathematical Modelling
The performance of desiccant cooling system can be evaluated using the hereafter mathematical exp ressions. These expressions were derived by the author Gandhidasan P et al., [5]. The air moisture removal effect iveness is defined by = , − , where Pa,i, Pa,o, Ps,i, designate respectively the air in let water vapour pressure, air outlet water vapour pressure, and the solution vapour pressure.
The vapour pressure of inside as well as outside air is obtained by The vapour pressure of CaCl 2 is calculated by P CaCl2 = A 25 f(ξ,θ) + f(water) f (water) is the vapour pressure above the normal water surface at different temperature. Table 2 show the values of parameters used in the vapour pressure calculations below. Vapour pressure on the water surface is calculated byln( � ) = ( 1 τ + 2 1.5 + 3 3 + 4 3 .5 + 5 4 + where Ts,o, Ts,i, Tc,i, designate, respectively, the desiccant solution outlet temperature, the desiccant solution inlet temperature, the cooling mediu m in let temperature.
The outlet temperature of the desiccant solution is derived fro m the above expression and represented by the expression The relation linking the concentrations of inlet and outlet desiccant solution is given by Finally the mass rate of mo isture removal is obtained fro m above equation.
Fro m the previous studies on the traditional packed bed dehumidifiers, the values of Ga/ Gs were slightly more.  Table 3 and given by-

Result and Discussion
The equations 2-9 have been used to calculate the performance data varying the air temperature fro m 30.1ºC to 33.1ºC. Figure 2 shows the variation of mo isture removal effectiveness with the inlet air temperature. It is clear fro m the figure that by increasing inlet air temperature, the mo isture removal effectiveness of air also goes on increasing. Here, when air temperature is lo wer than desiccant solution temperature, then air is heated up by desiccant solution and sensible heat is t ransferred fro m air to desiccant solution. But on increasing air temperature, air temperature dominates over desiccant temperature and able to transfer both sensible heat as well as latent heat. Under the constant desiccant flow rate and desiccant in let concentration, the outlet desiccant concentration is calculated and thereby moisture removal rate (m ͦ ) by using equation 12. In the measurement of concentration of desiccant, weight of a known quantity (100ml) of the desiccant is taken whereby its density is calculated along with its temperature and the concentration is calcu lated using the correlation developed by Manuel R. Conde [1]. Figure 3 shows the variat ion of moisture removal rate with outlet desiccant concentration. It reveals that varying outlet concentration fro m 4.37 to 5.2 gives rise to mo isture removal rate. This shows that by increasing outlet concentration, the absorption capacity of desiccant goes on decreasing and thus mo isture removal rate also goes on decreasing.  Figure 4, as shown below, the variation of moisture removal rate with hu midity change under the same air temperature has been depicted. Th is shows that by increasing humid ity change, moisture removal rate also goes on increasing. It means that when increasing mo isture inside air, latent heat also increases due to more condensation of mo isture. This extra amount of latent heat increases the temperature of air and thus it increases the moisture removal rate. also goes on increasing under the constant desiccant flow rate. It is due to the fact that by increasing air flo w rate, mo re amount of moisture co mes in contact with desiccant. This led to greater amount of condensation of moisture in a solution which overall increases moisture removal rate.

Parametric Studies
The following input parameters have been used to study the effect of various parameters on the performance of the system.
Inlet  Figure 6 shows the variat ion of moisture removal rate with inlet air temperature. It is clear fro m the figure that if the air temperature is less than the desiccant temperature, the air exchanges only sensible heat but when air temperature becomes more than desiccant temperatures, then latent heat also add significantly and thus there is a sudden increment in curve.  Figure 7 shows the variat ion of moisture removal rate with outlet desiccant concentration. Now, on varying outlet concentration fro m 0.10 to 0.45, mo isture removal rate goes on decreasing. This means that on increasing outlet concentration, the absorption capacity of desiccant goes on decreasing and thus mo isture removal rate also goes on decreasing.  Figure 8 shows the variation of mo isture removal effectiveness with the outlet air temperature. The reason behind it is that on increasing the air temperature, the air goes on losing its capability to exchange its sensible heat due to closeness of temperature difference.

Conclusions
The following are the conclusions drawn fro m the present study: •Increased inlet air temperature helps the desiccant solution to easily trap the moisture fro m hu mid fresh air and thus increases the effectiveness.
•Increased air flow rate enhances the condensation of mo isture and thus overall increases mo isture removal rate.
•Similarly, increased humid ity also enhances condensation and thereby moisture removal rate.
•The optimu m inlet temperature should be more than 17℃ when the desiccant inlet temperature is 17℃ and desiccant concentration is 35 %.
•The optimu m desiccant outlet concentration should be between 0.2 to 0.9. Th is range has been found to be the most effective fo r mo isture removal if the inlet desiccant concentration is 35 % and desiccant flow rate to be 0.2685 kg/s.
•The optimu m air flo w rate should be between 1.5 m/s to 2.5 m/s if the desiccant flo w rate assumed to be 0.2685 kg/s and inlet humidity ratio to be 14 g/kg.
The influence of the parameters studied on the dehumidification rate can be assumed to be linear. Further research work with other desiccant solutions and different cascade ring for efficient mixing o f air and desiccant solution can be undertaken to analyse the system performance.