tutorial heat transfer.pptx

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Water flows through a shower head steadily at a rate of 10 L/min. An electric resistance heater placed in the water pipe heats the water from 16°C to 43°C. Taking the density of water to be 1 kg/L, determine the electric power input to the heater, in kW. In an effort to conserve energy, it is proposed to pass the drained warm water at a temperature of 39°C through a heat exchanger to preheat the incoming cold water. If the heat exchanger has an effectiveness of 0.50 (that is, it recovers only half of the energy that can possibly be transferred from the Properties The density and specific heat of water at room temperature are ρ = 1 kg/L and C = 4.18 kJ/kg·°C Answers: 18.8 kW, 10.8 kW, 11.3 Rs

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Waterflowsthroughashowerheadsteadily atarateof10L/min.Anelectricresistance heaterplacedinthewaterpipeheatsthe water from 16Cto4C. !a"ing the density ofwaterto#e1"g/L$determinetheelectric power input to the heater$ in "W. %n an effort toconser&eenergy$itisproposedtopassthe drained warm water at a temperature of 'C throughaheate(changertopreheatthe incomingcoldwater.%ftheheate(changer hasaneffecti&enessof0.)0*thatis$it reco&ersonlyhalfoftheenergythatcan possi#ly#etransferredfromthedrained water toincomingcold water+$ determinethe electricpowerinputre,uiredinthiscase.%f the price of the electric energy is -.) .s/"Wh$ determine how much money is sa&ed during a 10/minute shower as a result of installing this heat e(changer.Properties !he density and specific heat of water at room temperature are 0 1 1 "g/L and C 1 4.1- "2/"g3CAnswers: 18.8 kW, 10.8 kW, 11.3 Rs%t is well "nown that wind ma"es the cold air feel much colder as a result of the wind-chill effect that is due to the increase in the con&ection heat transfer coefficientwithincreasingair&elocity.!hewind/chilleffectisusually e(pressedintermsofthewind-chillfactor,whichisthedifference#etween theactualairtemperatureandthee,ui&alentcalm/airtemperature.4or e(ample$awind/chillfactorof50Cforanactualairtemperatureof)C means that the windy air at )C feels as cold as the still air at 1)C. %n other words$ a person will lose as much heat to air at )C with a wind/chill factor of 50C as he or she would in calm air at 1)C. 4or heat transfer purposes$ a standingmancan#emodeledasa0/cm/diameter$160/cm/long&ertical cylinderwith#oththetopand#ottomsurfacesinsulatedandwiththeside surfaceatana&eragetemperatureof4C.4oracon&ectionheattransfer coefficient of 1) W/m5 3 C$ determine the rate of heat loss from this man #y con&ection in still air at 50C. What would your answer #e if the con&ection heattransfercoefficientisincreasedto)0W/m53Casaresultofwinds7 What is the wind/chill factor in this case7 Answers: 336 W, 1120 W, 32.7CA 0.5/L glass of water at 50C is to #e cooled with ice to )C. 8etermine how much ice needs to #e added to the water$ in grams$ if the ice is at 0C. Also$ determine how much water would #e needed if the cooling is to #e done with cold water at 0C. !he meltingtemperatureandtheheatoffusionoficeatatmosphericpressureare0C and .6 "2/"g$ respecti&ely$ and the density of water is 1 "g/L.9lot the amount of ice that needs to #e added to the water as a function of the ice temperature in the range of 54C to 0C.Answers: 35.4 gms, 600 gmsAsphericalmetal#allofradiusr0isheatedinano&entoatemperatureofTi throughout and is then ta"en out of the o&en and dropped into a large #ody of water at Twhereitiscooled#ycon&ectionwithana&eragecon&ectionheattransfer coefficientofh.Assumingconstantthermalconducti&ityandtransientone/dimensionalheattransfer$e(pressthemathematicalformulation*thedifferential e,uation and the #oundary and initial conditions+ of this heat conduction pro#lem. 8o not sol&e.Waterflowsthroughapipeatana&eragetemperatureofT1)0C.!heinnerand outer radii of the pipe are r1 1 6 cm and r5 1 6.) cm$ respecti&ely. !he outer surface of the pipe is wrapped with a thin electric heater that consumes 00 W per m length of the pipe. !he e(posed surface of the heater is hea&ily insulated so that the entire heat generatedintheheateristransferredtothepipe.:eatistransferredfromtheinner surface of the pipe to the water #y con&ection with a heat transfer coefficient ofh = ))W/m53C.Assumingconstantthermalconducti&ityandone/dimensionalheat transfer$e(pressthemathematicalformulation*thedifferentiale,uationandthe #oundaryconditions+oftheheatconductioninthepipeduringsteadyoperation.8o not sol&e.%nafoodprocessingfacility$asphericalcontainerofinnerradiusr140cm$outer radius r541 cm$ and thermal conducti&ity k1.) W/m 3 C is used to store hot water andto"eepitat100Catalltimes.!oaccomplishthis$theoutersurfaceofthe containeriswrappedwitha)00/Welectricstripheaterandtheninsulated.!he temperature of the inner surface of the container is o#ser&ed to #e nearly 100C at all times.Assuming10percentoftheheatgeneratedintheheaterislostthroughthe insulation$ *a+ e(press the differential e,uation and the #oundary conditions for steady one/dimensionalheatconductionthroughthecontainer$*b+o#tainarelationforthe &ariation of temperature in the container material #y sol&ing the differential e,uation$ and*c+e&aluatetheoutersurfacetemperatureofthecontainer. Alsodeterminehow much water at 100C this tan" can supply steadily if the cold water enters at 50C..ate of water heated from 50 to 100C50d dTrdr dr _ ,( )( )51 11$ 5 100 $osdT rBC T r T C k qdr ( )55111 1sq rT r Tr r k _ + ,( )1100 5.-6 5.) T rr _ + ,( )5101.)oT r C 4.-4 /ppQQ mC T m kg hC T Consider a long solid cylinder of radius r0 1 4 cm and thermal conducti&ity k =5) W/m 3 C. :eat is generated in the cylinder uniformly at a rate of g0 1 ) W/cm. !he side surface of the cylinder is maintained at a constant temperature of Ts = -0C. !he &ariation of temperature in the cylinder is gi&en #y;ased on this relation$ determine *a+ heat conduction is steady or transient$ *#+ if it is 1$ 5 or8*c+ the &alue of heat flu( on the side surface of the cylinder at r = r0( )5555oosoor rodT rq kdrq r rkk rq r 1 _ 1 , ]55-0 /sq W cm 8oes heat generation in a solid &iolate the first law of thermodynamics$ which states that energy cannot #e created or destroyed7