Presented by THANT ZIN WIN Department of Mechanical Engineering Technological University (Kyaukse) Mandalay Division, Myanmar thantm7@gmail.com Presentation Outlines 1. 2. 3. 4. 5. 6. 7. 8. 9. 10. 11. 12. 13. Introduction Operating Principle of Coreless Induction Furnace Important Role of Water Cooling Types of Water Cooling System Layout Description Design Parameters of Cooling Pond Pond Design Model Consideration Equilibrium Temperature and Surface Heat Flux Pond Design Calculation Case Study Cooling Pond Performance Conclusion Further Suggestions 2 Introduction Electric Induction Furnace Core Type Coreless Type Fig 1 – Core and Coreless Type of Induction Furnace 3 Operating Principle of Coreless Induction Furnace Electromagnetic induction Connect to a source of AC Create thermal energy Melt the charge Stirring action caused by molten metal Fig 2 - Simplified Cross Section of Coreless Induction Furnace 4 Important Role of Water Cooling Water is vital to be success. Need high water quality. Flow velocity of all water circuit should be monitored. Fig 3 - A Sample Induction Coil with Cooling Water Cooling water supply temperature should not be below 25°C. Upper limit of leaving the coil should be no more than 70°C. If too cold water is allowed, condensation may be formed. Fig 4 - Sample of the Damaging Induction Coil 5 Types of Water Cooling System The types of water cooling system are as follow: Cooling Pond System Spray Pond System Evaporative Cooling Tower – Open-circuit System Fan-radiator Closed-circuit System Water/water Heat Exchanger Dual System Dual System with Closed-circuit Cooling Tower 6 Cooling Pond System Hot water inlet Cool water outlet Water surface Large ground area Small investment Pond Fig 5 – Sketch of Typical Cooling Pond System Process Description Hot water outlet Furnace 1 Capacitor bank Cooling pond (8,000 ft3) Furnace 2 Control panel Fig 6 – Schematic Diagram of Cooling Pond Model Pumps 24.33 ft3/min Cool water inlet 7 Layout Description of 0.16 ton Coreless Induction Furnace Suction Pipeline Discharge Pipeline Cooling Pond Furnace No. 1 Furnace No. 2 Control Panel Capacitor Bank Pump Fig 7 - Functional Layout of 0.16 ton Coreless Induction Furnace 8 Design Parameters of Cooling Pond The hot water or inlet temperature into the pond The cool water or outlet temperature from the pond The operating time occupied in melting The solar heat flux or solar energy identified as the main heating mechanisms The pond volume and size corresponding to the equilibrium temperature 9 Pond Design Model Consideration V = volume T = temperature A = area W R = inflow rate Q = Outflow rate Cooling Pond Interchange with Atmosphere Ta H Td Q, T Ti, R Ts TE V, T Tb Induction Furnaces Fig 8 - Illustrative Diagram of Cooling Pond Model d ( cˆTV ) cˆTi R QT cˆ H dt 10 Equilibrium Temperature and Surface Heat Flux Sun Ta sc Td a Wind W speed 2 s br e c ar sr R, To Q, Ti Tsw Hot water inlet sn Cool water outlet TE an T Tb Subsurface conduction Ground Fig 9 – Heat Transfer Mechanisms in Cooling Pond sc f (W )[ Td 0.255Ta ] 1600 TE 23 f (W )( 0.255) 11 Pond Design Calculation Known Data ◙ Relative humidity, RH = 62% ◙ Ambient air, Ta = 88ºF ◙ Dew point, Td = 72ºF ◙ Hot water, Ti = 91.4ºF ◙ Cold water, To = 82.4ºF ◙ Latitude of Yangon, = 16.45 N ◙ Wind speed, W = 4 mph ◙ Flow rate, Q = 24.37 ft3/min Assumptions ◙ Steady-state (Completely mixed Pond) ◙ Inflow rate is equal to outflow rate ◙ Ts = T (Completely well-mixed pond) ◙ No seepage into or from groundwater ◙ Neglect heat conduction between the surrounding soil ◙ Heat exchange occurs near the pond surface only ◙ Volume, V = constant ◙ Density, ρ = constant ◙ At time t = 0, T = 28ºC Pond volume V 6000 ft 3 50 ft 20 ft 6 ft Pond surface area A 50 ft 20 ft 1000ft 2 dT 91.4k r 62.59 kT (kr kT )T dt where, kr = water retention rate kT = thermal rate 12 Case Study Data for the Example Parameter Specified Value Capacity 0.16 ton Current frequency 1,000 Hz Metal overheating temperature 2.912°F Consumed power 16 kW Dry bulb temperature 88°F Relative humidity Wind speed 62% 4 mph Entering water temperature 82.4°F Leaving water temperature 91.4°F Latitude of Yangon 16.45 N 13 Cooling Pond Performance Allowable Operating Time (hr) 8 7 6 5 4 3 2 1 0 7000 8000 9000 10000 11000 Pond Area (ft2) (Fixed on 8 ft depth) The results corroborate the fact that the most important variable on cooling pond performance is pond surface area itself, but not is volume. 14 Conclusion Cooling system is the important part of coreless induction furnace. Cooling ponds are one of the economically competitive alternatives for removing of heat from induction furnaces. The most important influence factor on the cooling pond configurations is pond surface area. 15 Further Suggestions ◙ Extending the baffles in the pond. Highly baffled pond, longitudinal baffles, rectangular discharge Highly baffled pond, lateral baffles, rectangular discharge ◙ Using the heat exchangers. 16 17 Spray Pond System Fig - Sample Spray Pond System Use a number of nozzles Depend on relative humidity 18 Fan-radiator Closed-circuit System Fig - Fan-radiator (closed-circuit) System Completely enclosed Loss of water is slight 19 Water/water Heat Exchanger Dual System Fig - Dual System with Water/water Heat Exchanger More compact Easier to clean and maintain 20 Dual System with Closedcircuit Cooling Tower Fig - Dual System with Closed-circuit Cooling Tower Slightly more expensive Lower Piping and pumping costs 21 Types of Cooling Tower Fig - Mechanical Draft Cooling Towers Fig - Natural Draft Cooling Towers 22 Cooling Pond Area and Volume Calculation By using the following equations, T v 84.65 82.4 0.25 To 91.4 82.4 ( IP 0.3) The type of pond is shallow Declination angle, 360 23.45sin (264 74) 10.51 365 s cos1 ( tan16.45tan 10.51) 86.85 1.5159rad The hour angle, Maximum possible sunshine duration, S o 2 86 .85 11.58hr 15 The extraterrestrial solar radiation , 360 51411 0.033cos 75 365 (1.52sin(16.45) sin(10.51) cos(16.45) cos(10.51) sin(86.85)) 34233.62 kJ /(m 2 day) sc o 24 Ref: Magal, B. S. (1999), Solar Power Engineering, Fourth reprint, TATA McGraw Hill Publishing Company Limited, Bombay. 23 sc 9.5 0.18 0.62 34233.62 11 . 9 sc 23106.25 kJ /(m 2 day) 2034.62 Btu /(day ft 2 ) Clear sky solar radiation, Equilibrium temperature by using the iterative method, TE 62.5917 62.59 F sn an 1217 15 182 Btu /(day ft 2 ) 100 3386 15 508 Btu /(day ft 2 ) 100 br 3519Btu /(day ft 2 ) e 1060Btu /(day ft 2 ) c 73 Btu /(day ft 2 ) The net heat flux, n 182 508 3519 1060 73 3816Btu /(day ft 2 ) 24 The net heat exchange coefficient, Normalized intake temperature, K 3816 173 Btu /(day ft 2 F ) (84.65 62.59) 82.4 62.59 Ti 0.6876 91.4 62.59 Ti Pond cooling capacity, 1 1 r 1 0.6876 1 r r 0.4543 KA r cˆQ (173/ 1440) A (62.4 1.003 24.37) A 5768 ft 2 0.4543 Required cooling pond area, 25 By implementing to unit depth, the volume of cooling pond is V 5768 ft 3 49 ft 20 ft 6 ft Approximately, the volume 6000 ft 3 50 ft 20 ft 6 ft is used in the construction. A 50 ft 20 ft 1000ft 2 From the above volume and area, the relationship between the temperature and operating time is obtained as follows: dT 91.4k r 62.59k T (k r k T )T dt Where, kr = water retention rate kT = thermal rate 26 Solar Heat Flux Sun sc br Cloud s sr a e c ar Water surface sn an n sn an br e c Fig – Components of Surface Heat Transfer where, n = the net heat flux into the water surface sn = the net solar (short-wave) radiation into the water surface an = the net atmospheric (long-wave) radiation from the water surface br = the back (long-wave) radiation from the water surface e = the evaporative heat flux from the water surface c = the conductive heat flux from the water surface s = the solar radiation at water surface sr = the reflected solar radiation a = the atmospheric (long-wave) radiation ar = the reflected atmospheric radiation 27