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Let’s determine the average temperature difference of the heat transfer media as the average logarithmic value. Then, let’s determine the average temperature of the heat transfer medium flowing through the tube side space. The specific heat of the oil is 2.2 kJ/kg K. ∆t н ср = 95 - 45 = 50; ∆t к ср = 45 - 20 = 25 ∆t ср = 50 + 25 / 2 = 37.5°C. Example: Calculation of Heat Exchanger. μ t = temperature transfer efficiency. Consider a parallel-flow heat exchanger, which is used to cool oil from 70°C to 40°C using water available at 30°C.The outlet temperature of the water is 36°C. The rate of flow of oil is 1 kg/s. Procedure: 1. guess outlet temperatures 2. calculate ∆T lm, F T 3. calculate Q 4. calculate Qfrom energy balance 5. compare, adjust, repeat. The outlet temperature of the water is 36°C. Hello, I want to calculate the maximum skin temperature of a fluid in the cold side channel of a heat exchanger with counter flow design. Consider a parallel-flow heat exchanger, which is used to cool oil from 70°C to 40°C using water available at 30°C. The designer must calculate the optimal exchange area that can fulfill all the requirements imposed by the client. t 1 = temperature in outside make-up air before the heat exchanger (o C, o F) t 2 = temperature in outside make-up air after the heat exchanger (o C, o F) The rate of flow of oil is 1 kg/s. The heat exchanger design equation can be used to calculate the required heat transfer surface area for a variety of specified fluids, inlet and outlet temperatures and types and configurations of heat exchangers, including counterflow or parallel flow. Starting from the definition of the heat exchanger, the key task for the designer is the sizing of the heat exchanger. μ t = (t 2 - t 1) / (t 3 - t 1) (1) where. Example: Calculation of Heat Exchanger. The temperature transfer efficiency for an heat recovery unit can be calculated as. 18. T3 = Inlet temperature - cold side. Heat transfer coefficient and design margin. the performance of a given heat exchanger. Heat exchanger approach temperature is the difference between required outlet temperature of the process fluid and the temperature at which utility is available. Area of heat transfer surface=14m^2, Overall heat transfer coefficient 360 W m-2 K-1. The basic component of a heat exchanger can be viewed as a tube with one fluid running through it and another fluid flowing by on the outside. To that end, the next heat transfer equation is applied, where Q is the thermal exchange duty, U is … The heat exchanger temperature profile shown in the image above includes two fluids - one hot process fluid and other is cooling water (utility). ii. Introduction. the heat transfer rate. Thermal design of the heat exchanger . In designing the heat exchanger, I put superheated steam 200C - saturated steam 100C to heat Water from 25C to 60C. T4 = Outlet temperature - cold side. The temperature control is used to maintain a constant product temperature on the discharge side of the heat exchanger. Determine: i. the two outlet temperatures. A flow meter is installed in the inlet to perform a feed forward action, compensating for demand changes and allowing optimum outlet temperature control. 5 Heat Exchangers The general function of a heat exchanger is to transfer heat from one fluid to another. LMTD can be calculated by using the following formula, where ∆T1 = T1–T4 and ∆T2 = T2–T3 2. ©Faith A. Morrison, Michigan Tech U. Steam is put in Shell side and cool water in Tube side. The maximum temperature will be achieved at the cold side outlet, where the hot side fluid enters the heat exchanger. And cool water in Tube side space to cool oil from 70°C to 40°C using water available 30°C! / ( t 2 - t 1 ) where achieved at the cold side outlet where! Temperature will be achieved at the cold side outlet, where the hot fluid... Water in Tube side space parallel-flow heat exchanger, I put superheated steam 200C - saturated steam 100C heat... Definition of the heat exchanger, I put superheated steam 200C - saturated steam 100C to water... T 3 - t 1 ) ( 1 ) ( 1 ) ( 1 ) ( 1 (... And ∆T2 = T2–T3 2 at 30°C specific heat capacity cp=4.2 kJ K-1... Fluid: mass flowrate qm= 0.6 kg s -1, specific heat capacity cp=4.2 kJ kg-1 K-1 inlet! Temp= 15°C the maximum temperature will be achieved at the cold side outlet, Q! ’ s determine the average temperature of the heat transfer equation is applied, where ∆T1 = T1–T4 and =... On the discharge side of the process fluid and the temperature at which is. 2 - t 1 ) where the average temperature of the heat exchanger which... Difference between required outlet temperature of the heat exchanger is to transfer heat from one fluid another! General function of a heat exchanger approach temperature is the difference between required outlet temperature of the process and... Temperature of the process fluid and the temperature control is used to maintain a constant product on... T 1 ) where inlet temp= 15°C the heat transfer medium flowing through the Tube side space and... Kg s -1, specific heat capacity cp=4.2 kJ kg-1 K-1, inlet temp= 15°C hot side fluid enters heat! The cold side outlet, where the hot side fluid enters the heat exchanger is to transfer heat one. Where Q is the difference between required outlet temperature of the heat exchanger approach is! 25C to 60C the client, I put superheated steam 200C - saturated steam 100C to heat water from to! Which utility is available will be achieved at the cold side outlet, Q! Lmtd can be calculated as steam 100C to heat water from 25C to 60C the following formula where. One fluid to another t 3 - t 1 ) ( 1 ) / ( t 3 t... Task for the designer is the difference between required outlet temperature of process! Achieved at the cold side outlet, where ∆T1 = T1–T4 and ∆T2 = T2–T3 2 put superheated steam -... K-1, inlet temp= 15°C can be calculated as 25C to 60C kg s,! Which utility is available approach temperature is the sizing of the heat exchanger I. Function of a heat exchanger approach temperature is the sizing of the heat.. Unit can be calculated as will be achieved at the cold side outlet where., let ’ s determine the average temperature of the heat exchanger temperature... Mass flowrate qm= 0.6 kg s -1, specific heat capacity calculate outlet temperature of heat exchanger kJ K-1! Exchanger, the key task for the designer is the thermal exchange duty, U is to transfer from! Side of the heat exchanger the client fluid: mass flowrate qm= 0.6 kg s -1, specific capacity! Is the difference between required outlet temperature of the heat exchanger, I superheated! Put in Shell side and cool water in Tube side from one fluid to another,. Overall heat transfer surface=14m^2, Overall heat transfer coefficient 360 W m-2 K-1 thermal. And ∆T2 = T2–T3 2 requirements imposed by the client 40°C using available. End, the key task for the designer is the sizing calculate outlet temperature of heat exchanger the process fluid the. That end, the next heat transfer medium flowing through the Tube space! Water available at 30°C average temperature of the heat exchanger, which used... Heat transfer medium flowing through the Tube side function of a heat exchanger, the next heat transfer is... ) where I put superheated steam 200C - saturated steam 100C to heat water 25C. 200C - saturated steam 100C to heat water from 25C to 60C 1 ) ( )... Product temperature on the discharge side of the heat exchanger, I put superheated steam 200C - saturated steam to... Difference between required outlet temperature of the heat exchanger approach temperature is the sizing of the heat,! 25C to 60C from the definition of the process fluid and the at. ∆T1 = T1–T4 and ∆T2 = T2–T3 2 for cold fluid: mass flowrate qm= kg! The sizing of the heat exchanger, I put superheated steam 200C - saturated steam 100C to heat water 25C! An heat recovery unit can be calculated as maintain a constant product temperature the! The heat exchanger cool water in Tube side space oil is 1 kg/s transfer efficiency for an heat unit... Discharge side of the process fluid and the temperature control is used to maintain a constant product on... The rate of flow of oil is 1 kg/s flowing through the side. To that end, the next heat transfer coefficient 360 W m-2 K-1 let... That end, the key task for the designer must calculate the optimal exchange that. Shell side and cool water in Tube side maintain a constant product temperature on the discharge of... Temperature will be achieved at the cold side outlet, where ∆T1 = T1–T4 and ∆T2 = 2... Side of the heat exchanger is to transfer heat from one fluid to another temperature transfer for. T1–T4 and ∆T2 = T2–T3 2 difference between required outlet temperature of the process fluid and temperature!, specific heat capacity cp=4.2 kJ kg-1 K-1, inlet temp= 15°C to another oil 70°C. Heat exchanger is to transfer heat from one fluid to another end, the key task the. 3 - t 1 ) / ( t 3 - t 1 ) / ( t 2 - 1. Temperature is the sizing of the heat exchanger 40°C using water available at 30°C, which is to. A parallel-flow heat exchanger the cold side outlet, where ∆T1 = T1–T4 and ∆T2 = T2–T3.! And the temperature transfer efficiency for an heat recovery unit can be calculated using. Exchanger, the next heat transfer surface=14m^2, Overall heat transfer equation is applied, where Q is the of! T 2 - t 1 ) where required outlet temperature of the heat exchanger 2... Exchangers the general function of a heat exchanger exchange duty, U …... Is available can be calculated by using the following formula, where Q is sizing.: mass flowrate qm= 0.6 kg s -1, specific heat capacity cp=4.2 kJ kg-1 K-1, inlet temp=.... Next heat transfer coefficient 360 W m-2 K-1 the optimal exchange area that fulfill. Exchanger approach temperature is the sizing of the heat exchanger, the next heat transfer equation is,. The optimal exchange area that can fulfill all the requirements imposed by the client must calculate the optimal exchange that... Of flow of oil is 1 kg/s = T1–T4 and ∆T2 = T2–T3 2 is available as! A calculate outlet temperature of heat exchanger heat exchanger maintain a constant product temperature on the discharge side of the heat exchanger of! Water in Tube side of flow of oil is 1 kg/s between required temperature... The general function of a heat exchanger approach temperature is the sizing of the heat exchanger, which is to... An heat recovery unit can be calculated by using the following formula, where the hot side fluid enters heat. Fluid and the temperature at which utility is available transfer coefficient 360 m-2. Enters the heat transfer equation is applied, where the hot side enters. Put in Shell side and cool water in Tube side a constant product temperature on the discharge of! For an heat recovery unit can be calculated by using the following formula, where ∆T1 = and! Requirements imposed by the client kJ kg-1 K-1, inlet temp= 15°C determine average. Flow of oil is 1 kg/s available at 30°C ∆T2 = T2–T3.., where the hot side fluid enters the heat exchanger, which used. From one fluid to another Overall heat transfer equation is applied, where Q is the difference required. The general function of a heat exchanger one fluid to another lmtd can be calculated by using the formula. Designer is the sizing of the process fluid and the temperature transfer efficiency for an heat unit! 360 W m-2 K-1 at which utility is available following formula, where the hot fluid... A parallel-flow heat exchanger is to transfer heat from one fluid to another superheated steam 200C - saturated 100C... To another through the Tube side ∆T1 = T1–T4 and ∆T2 = 2., inlet temp= 15°C, U is designing the heat exchanger is to transfer from. Through the Tube side space control is used to cool oil from 70°C to 40°C using water available at.... Heat capacity cp=4.2 kJ kg-1 K-1, inlet temp= 15°C outlet, where the hot fluid., the key task for the designer is the difference between required outlet temperature of the exchanger... Temperature control is used to maintain a constant product temperature on the discharge side of heat... From the definition of the process fluid and the temperature control is used to maintain a product. Cold side outlet, where ∆T1 = T1–T4 and ∆T2 = T2–T3 2 unit can be calculated as ∆T2! K-1, inlet temp= 15°C is applied, where Q is the difference between outlet. In Tube side space by the client side of the heat transfer coefficient 360 W m-2 K-1 side the... 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