Introduction The objectives of the experiment conducted were to determine air outlet velocities & flow rates, air inlet velocities and flow rates, and water inlet and outlet data and to compare of data at different water inlet flow rates. Cooling towers are used in water treatment processes, sewage systems, and heating and cooling systems. The type of cooling tower that was used for the experiment was a counter-flow tower. The air stream and water stream flow opposite of each other. Theory The calculations for this experiment were based on the following two equations. Assuming Steady State Operation [IN = OUT], the following balances can be used: Overall Mass Balance MAO + MWO = MAI + MWI Overall Energy Balance hAO*MAO + hWO*MWO = hAI*MAI+ hWI*MWI Where M=Mass, h=enthalpy, AO=Air Outlet, AI=Air Inlet, WO=Water Outlet, and WI=Water Inlet. Wet bulb and dry bulb temperatures of the air inlets and outlets were and used to look up enthalpy data on the psychometric chart. Also, software to calculate psychometric chart information was used. In order to calculate air outlet velocities, the profile is needed. The profile can be found by plotting velocity (y-axis) versus radius (xaxis) at which the velocity was measured. A curve fit was performed to obtain the 1 equation for the profile. The following equation was used to calculate the average velocity: 2 R Vave V (r )rdrd V (r )dA dA rdrd 0 0 2 R 0 0 Where V(r) is the velocity profile and r is the radius. The volumetric flow rate is determined by: (Volumetric flow rate) = Vave*Area Using the volumetric flow rate, the mass flow rate of the air outlet can be calculated by the following equation: (Mass flow rate) = (density)*(volumetric flow rate) 2 Equipment Figure 1 is a schematic drawing of the cooling tower used in the experiment. Figures 2, 3, 4, 5, and 6 are pictures the Water cooling tower located in EMCS 120 that was Outlet Air offor Inlet ) Flow Rate = 10.1 used for the experiment. At the water inlet, there is(l/min a mechanism that evenly distributes the incoming water=throughout Area 0.312 m2the system. On the side of the tower, a fan is responsible Volumetric Flow Rate= 1.6 m3/s for inputting air, i.e. the air inlet. Temp. Dry Bulb= 23 °C= Wet Bulb Temp. Enthalpy = 86 kJ/kg Dry Air Air Outlet 2 Warm Water Inlet 3 Air Inlet 1 Cool Water Outlet 4 Make-Up Water Portable Cooling Tower Figure 1 Schematic of Cooling Tower Figure 2 Cooling Tower 3 Air Inlet Figure 3 Air Inlet Air Outlet and Water Inlet Figure 4 Water Inlet and Air Outlet 4 Portable Cooling Tower Figure 5 Cooling tower Water Spraying Upward Figure 6 Air Outlet and Water Inlet 5 Procedure The experiment began by filling the bottom of the cooling tower with water in order to prevent splashing. Once the bottom was filled, the tower was plugged into a power supply. Temperature measurements are taken for the water inlet first. Next, air inlet wet bulb and dry bulb temperatures are taken at the 3 regions of the inlet location. They were averaged together. As the system is running, air outlet temperatures are taken at the same 3 radii with the 3 sections at the outlet region as shown in Figure 6. Finally, the water outlet temperature is taken at the bottom of the cooling tower. 6 Results Figure 7 is a graph of the outlet velocity as a function of radius Velocity for water inlet flowOutlet fate = 5.1 (l/min) as a Function of Radius for Water Inlet Flow Rate = 5.1 (l/min) Velocity (m/s) Air Outlet Velocities V(r) = -438.81r3 - 111.83r2 + 78.86r + 0.0789 R2 = 0.9876 9 8 7 6 5 4 3 2 1 0 0 0.05 0.1 0.15 0.2 0.25 0.3 0.35 Radius (m) Figure 7 Outlet Air Velocity Profile @ 5.1 (l/min) Figure 8 shows the graph of the outlet velocity as a function of radius Outlet for water inlet flow fate = Velocity 10.1 (l/min)as a Function of Radius for Water Inlet Flow Rate = 10.1 (l/min) Air Outlet Velocities 3 2 Velocity (m/s) V(r)= -395.28r - 118.74r + 76.678r + 0.0452 9 8 7 6 5 4 3 2 1 0 2 R = 0.9955 0 0.1 0.2 0.3 0.4 Radius (m) Figure 8 Outlet Air Velocity Profile @ 10.1 (l/min) 7 Figure 9 shows the graph of the outlet velocity as a function of radius Outlet Velocity for water inlet flow fate = 40.3 (l/min) as a Function of Radius for Water Inlet Flow Rate = 40.3 (l/min) Air Outlet Velocities 3 2 V(r) = -318.78r - 32.419r + 41.871r + 0.0242 2 5 R = 0.9965 4.5 Velocity (m/s) 4 3.5 3 2.5 2 1.5 1 0.5 0 0 0.05 0.1 0.15 0.2 0.25 0.3 0.35 Radius (m) Figure 9 Outlet Air Velocity Profile @ 40.3 (l/min) Table 1 shows a comparison of data from calculations and measurements at different water inlet flow rates Water Inlet Flow Rates Inlet Temp Outlet Temp. Temp. Change Mass Flow Rate Tons of Cooling at 5.1 l/min at 10.1 l/min at 40.3 l/min 52.5 oC 56.3 oC 52 oC 27.7 oC 31 oC 30.4 oC 24.8 oC 25.3 oC 21.6 oC 0.085 kg/s 0.168 kg/s 0.671 kg/s 2.5 5.1 17 Figure 10 Comparison Table 8 Discussion of Results There were different velocity profiles found at each inlet water flow rate. The profiles were all of a third order polynomial. The Tons of Cooling increased as the inlet water flow rate increased. The greatest change in temperature occurred when the water inlet flow rate was at 10.1 (l/min). Conclusions Through the conduction of this experiment, a cooling tower analysis was able to be completed. Measurements for inlet and out data for air and water were made with relative ease… allowing for calculations of data for the system a success. All data reported was an average of at least 3 data points in order to provide better accuracy as opposed to using a relative measurement (at just one point). 9 Appendix Sample Calculation (Volumetric flow rate) = Vave*Area (Volumetric flow rate) = (8.56 m/s) * (0.0380 m2) (Volumetric flow rate) = 0.325 m3/s 10