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Heat Exchangers

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LAB SESSION # 1 HEAT EXCHANGER Heat exchangers are used to transfer heat from a fluid on a side of a barrier to a fluid on the other side without allowing the fluids to mix together. Heat exchangers maximize the surface area of a wall that is used between the two fluids while minimizing any resistance to the flow of a fluid through the exchanger. Example The most well-known type of heat exchanger is a car radiator, in a radiator, a solution of water and ethylene glycol, also known as antifreeze, transfers heat from the engine to the radiator and then from the radiator to the ambient air flowing through it. This process helps to keep a car's engine from overheating. PARALLEL-FLOW HEAT EXCHANGER Parallel-flow, a major type of heat exchangers, allows two fluids to enter the exchanger at the same end. The two fluids then travel in parallel to the other side of the exchanger. The hot fluid transfers heat to the wall via convection. Parallel-flow heat exchangers are often used when two fluids must be brought to close to the same temperature.
Transcript
Page 1: Heat Exchangers

LAB SESSION # 1

HEAT EXCHANGERHeat exchangers are used to transfer heat from a fluid on a side of a barrier to a fluid on the other side without allowing the fluids to mix together. Heat exchangers maximize the surface area of a wall that is used between the two fluids while minimizing any resistance to the flow of a fluid through the exchanger.

Example

The most well-known type of heat exchanger is a car radiator, in a radiator, a solution of water and ethylene glycol, also known as antifreeze, transfers heat from the engine to the radiator and then from the radiator to the ambient air flowing through it. This process helps to keep a car's engine from overheating.

PARALLEL-FLOW HEAT EXCHANGER

Parallel-flow, a major type of heat exchangers, allows two fluids to enter the exchanger at the same end. The two fluids then travel in parallel to the other side of the exchanger. The hot fluid transfers heat to the wall via convection. Parallel-flow heat exchangers are often used when two fluids must be brought to close to the same temperature.

LOGARITHMIC MEAN TEMPERATURE DIFFERENCE (LMTD) METHOD

The logarithmic mean temperature difference (also known as log mean temperature difference or simply by its initialism LMTD) is used to determine the temperature driving force for heat transfer in flow systems, most notably in heat exchangers. The LMTD is a logarithmic average of the temperature difference between the hot and cold streams at each end of the exchanger. The larger the LMTD, the more heat is transferred. The use of the LMTD arises straightforwardly from the analysis of a heat exchanger with constant flow rate and fluid thermal properties.

Page 2: Heat Exchangers

From Heat Transfer Eq. we get

Where, A is the total contact area and TΔ lm is the logarithmic mean temperature difference (LMTD)

LMTD=∆T lm=¿

Significance of the LMTD

The LMTD is the driven force for the heat exchange between the two fluids. As the LMTD value increases, the amounts of heat transfer between the two fluids also increase. The LMTD value is used for calculating the heat duty of the heat exchanger.

CONCENTRIC TUBE HEAT EXCHANGER

Page 3: Heat Exchangers

The purpose of this unit is to demonstrate the working principles of industrial heat exchangers in the most convenient way in the laboratory. Experiments show the practical importance of the temperature profiles, co- and counter flow, energy balances, log-mean temperature difference, and heat transfer coefficients.

The experimental setup consists of two concentric tubes in which fluids pass. The hot fluid is hot water, which is obtained from an electric geyser. Hot water flows through the inner tube, in one direction. Cold fluid is cold water, which flows through the annulus. Control valves are provided so that direction of cold water can be kept parallel or opposite to that of hot water. Thus, the heat exchanger can be operated either as paralle1 or counter flow heat exchanger. The temperatures are measured with thermometer. Thus, the heat transfer rate, heat transfer coefficient, LMTD and effectiveness of heat exchanger can be calculated for both parallel and counter flow.

EXPERIMENT # 01

Page 4: Heat Exchangers

DEMONSTRATE THE WORKING PRINCIPLE OF A DOUBLE PIPE CONCENTRIC TUBE HEAT EXCHANGER OPERATING UNDER

PARALLEL FLOW CONDITION.Apparatus

Double pipe heat exchanger Apparatus with both parallel and counter flow arrangement

Procedure

Start the water supply. Adjust the water supply on hot and cold sides. Keep the valves V2 & V3 closed and V1 & V4 opened so that arrangement is Parallel flow. Switch ON the geyser. Temperature of water will start rising. After temperatures become steady, note down the readings in the observation table.

Observations and Calculations

Length of pipe = L = 1.5 m

Tube outer diameter = do = (15x0.7) mm

Tube inner diameter = di = (22x0.9) mm

Set Temperature = 65°C

Transmission Area = A = 0.067 m2

Hot water Flow rate = Qh =2 ltr/min

Cold water Flow rate = Qc =1 ltr/min

Mass Flow rate of hot water,

mh=pQh=0.0333kg/ s

Mass Flow rate of cold water,

mc=pQc=0.01667 kg/s

Density of water= 1000kg/m3

Specific Heat of Water= Cp= 4.186 kJ/kg°C

Hot water Cold Water

Page 5: Heat Exchangers

Position Temperature (°C)

Temperature (°C)

Inlet 0m Thi=50 Tci=30Middle 0.75m 47 33.5Outlet 1.5m Tho=46 Tco=38.5

Temperature Difference at inlet = ∆T 1=T hi−T ci=20C

Temperature Difference at Outlet =∆T 2=T ho−T co=7.5C

Log mean Temperature Difference = LMTD = ∆Tm= 12.74 C

Amount of heat Given out by hot liquid=

qemit=mh .Cp .(T hi−T ho)=557.6Watts

Amount of heat Absorbed by Cold Water,

q|¿|=mc .C p .(Tci−T co)=592.3Watts¿

Losses,

qemitt−q|¿|=35.3Watts¿

Efficiency of Heat Exchanger,

Ƞ=¿

Overall Heat Transfer Coefficient,

U=q|¿|/(At x ∆Tm )=694Watt /m2C ¿

Efficiency of cold water,

Ƞcold water=42.5 %

Efficiency of hot water,

Ƞhot water=20 %

Temperature Profile:

Page 6: Heat Exchangers

0 0.2 0.4 0.6 0.8 1 1.2 1.4 1.620

22

24

26

28

30

32

34

36

38

40

Hot Water Temperature ProfileCold Water Temperature Profile

Distance along tube length X

(m)

Tem

pera

ture

T (C

)

Comments

Never switch ON the geyser unless there is water supply through it. If the red indicator on geyser goes off during operation, increase the water supply, because it

indicates that water temperature exceeds the set limit. Ensure steady water flow rate and temperatures before noting down the readings, as fluctuating

water supply can give erratic results.

LAB SESSON#02

Page 7: Heat Exchangers

COUNTER-FLOW

In counter-flow heat exchangers, the fluids enter the exchanger from opposite ends. As the two flows move toward each other from opposite directions, the system is able to maintain almost a constant gradient between the two liquid flows as they travel the length of the exchanger. This enables nearly all the heat properties from one flow to be transferred to the other flow.

CONCENTRIC TUBE HEAT EXCHANGER

EXPERIMENT#02

Page 8: Heat Exchangers

DEMONSTRATE THE WORKING PRINCIPLE OF A DOUBLE PIPE CONCENTRIC TUBE HEAT EXCHANGER OPERATING UNDER

COUNTER FLOW CONDITION.Apparatus

Double pipe heat exchanger Apparatus with both parallel and counter flow arrangement

Procedure

Start the water supply. Adjust the water supply on hot and cold sides. Open the valves V2 & V3 and then close the valves V1 & V4. The arrangement is now counter

flow. Switch ON the geyser. Temperature of water will start rising. Wait until the steady state is reached and note down the readings. After temperatures become steady, note down the readings in the observation table.

Observations and Calculations

Length of pipe=L= 1.5 m

Tube outer diameter=do= (15x0.7) mm

Tube inner diameter=di= (22x0.9) mm

Set Temperature= 65°C

Transmission Area=A=0.067 m2

Hot water Flow rate= Qh=2 ltr/min

Cold water Flow rate= Qc =1ltr/min

Mass Flow rate of hot water=mh= pQh=0.0333 (kg/s)

Mass Flow rate of cold water =mc= pQc= 0.01667(kg/s)

p = Density of water= 1000kg/m3

Specific Heat of Water= Cp= 4.186 kJ/kg°C

Position Hot water Temperature

(°C)

Cold Water Temperature

(°C)

Page 9: Heat Exchangers

Inlet 0m Thi=55 Tco=40Middle 0.75m 51 34Outlet 1.5m Tho=50 Tci=30

Temperature Difference at inlet= ∆T1=Thi-Tco= 15 C

Temperature Difference at Outlet=∆T2=Tho-Tci= 20 C

Log mean Temperature Difference=LMTD=∆Tm= 17.4 C

Amount of heat Given out by hot liquid=qemit=mh.Cp.(Thi-Tho)= 697.8 Watts

Amount of heat Absorbed by Cold Water= qabs=mc.Cp.(Tco-Tci)= 697 Watts

Losses= qemit - qabs= 0.8 Watts

Efficiency of Heat Exchanger=Ƞ= (qabs/ qemit)x100=99.88%

Overall Heat Transfer Co-efficient=U=qabs/(Atx∆Tm)=598.6 Watt/m2C

Efficiency of cold water= Ƞcold water =40%

Efficiency of cold water= Ƞhot water =20%

Temperature Profile:

Page 10: Heat Exchangers

0 0.2 0.4 0.6 0.8 1 1.2 1.4 1.620

22

24

26

28

30

32

34

36

38

40

Hot Water Temperature ProfileCold Water Temperature Profile

Distance along tube length X

(m)

Tem

pera

ture

T (C

)

Comments

If heat capacity rates of the cold and hot fluids are the same and the heat exchanger is operated in the counter-flow regime then T is independent of position in the heat exchanger.Δ

Page 11: Heat Exchangers

Lab Sesson#03

THEORYIn general with higher flow rates the overall heat transfer coefficient will increase a bit and with lower flow rates it will decrease. This is because the change in velocity will affect the film coefficient portion of the overall heat transfer coefficient.

So with a higher flow rate you will get slightly better heat transfer but you will also have a greater mass flowing through the exchanger. The net result will be the transfer of more heat but the actual temperature of the fluid exiting the exchanger will likely be lower because of the extra mass involved.

Other things that are affected by changes in flow rate are the pressure through the exchanger (Higher flow rates leads to higher pressure drops. Lower flow rates lead to lower pressure drops.) and in some cases possible fouling of the exchanger.

Experiment#03

DETERMINE THE EFFECT OF VOLUME FLOWRATE VARIATION OF

A) HOT FLUID

B) COLD FLUID

ON THE PERFORMANCE OF A GIVEN HEAT EXCHANGER (FOR BOTH PARALLEL AND COUNTER FLOW ARRANGEMENTS)Apparatus

Double pipe heat exchanger Apparatus with both parallel and counter flow arrangement

(a) For variation in Hot fluid Flowrate

1. For Parallel-Flow Arrangement

Procedure

1. Start the water supply. Adjust the water supply on hot and cold sides.2. Keep the valves V2 & V3 closed and V1 & V4 opened so that arrangement is Parallel flow.3. Switch ON the geyser. Temperature of water will start rising. 4. After temperatures become steady, note down the readings in the observation table.5. Vary the hot water flowrate and repeat the same procedure.

Page 12: Heat Exchangers

Observations and Calculations

Length of pipe = L = 1.5 m

Tube outer diameter = do = (15x0.7) mm

Tube inner diameter = di = (22x0.9) mm

Set Temperature = 60°C

Transmission Area = A = 0.067 m2

Cold water Flow rate = Qc =1 ltr/min

Mass Flow rate of cold water,

mc=pQc=0.01667 kg/s

Density of water= 1000kg/m3

Specific Heat of Water= Cp= 4.186 kJ/kg°C

No. of obs

Flowrate of hot water

Qh

Hot water Temperature (°C) Cold Water Temperature (°C)

(ltr/min) Inlet(Thi)

Mid Outlet (Tho)

Inlet(Tci)

Mid Outlet(Tco)

At x=0m

At x=0.75m At x=1.5m

Atx=0m

At x=0.75m At x=1.5m

1. 1 46 44 41 29 31 342. 2 53 52 49 29 35 393. 3 60 56 55 29 37 444. 4 55 52 50 29 35 42

Sample Calculations

For Observation Set #01

Temperature Difference at inlet = ∆T 1=T hi−T ci=17C

Temperature Difference at Outlet =∆T 2=T ho−T co=07C

Log mean Temperature Difference = LMTD = ∆Tm= 11.27 C

Amount of heat Given out by hot liquid=

qemit=mh .Cp .(T hi−T ho)=348.83Watts

Page 13: Heat Exchangers

Amount of heat Absorbed by Cold Water,

q|¿|=mc .C p .(Tci−T co)=348.83Watts¿

Losses,

qemitt−q|¿|=0Watts¿

Efficiency of Heat Exchanger,

Ƞ=¿

Overall Heat Transfer Coefficient,

U=q|¿|/(At x ∆Tm )=461.9Watt /m2C ¿

Efficiency of cold water,

Ƞcoldwater=29.4 %

Efficiency of hot water,

Ƞhot water=29.4 %

Results for the Given Data Set:

Flowrate of hot water

Qh

∆T1

Thi-Tci∆T2

Tho-Tco

LMTD∆Tm

qemit

mh.Cp.(Thi-Tho)

qabs

mc.Cp.(Tci-Tco)

Lossesqemit - qabs

U q

abs/(Atx∆Tm)

Ƞcold

water

Ƞhot water

(ltr/min) (C) (C) (C) Watts Watts Watts Watt/m2C % %

1 17 7 11.27 348.83 348.83 0 461.9 29.4 29.42 24 10 16 558.13 696.7 -138.5 650 41.7 16.673 31 11 19.3 1046.5 1044.5 2 807.75 48.4 16.124 26 8 15.27 1395.3 907 488.3 886.53 50% 19.23

Graphs

Scale : X-axis 1 big box=0.2 m Y-axis 1 big box=5 (C)

R1: for hot water Flow rate= Qh =1ltr/min R2: for hot water Flow rate= Qh =2ltr/min R3 :for hot water Flow rate= Qh =3ltr/min R4 :for hot water Flow rate= Qh =4ltr/min

Page 14: Heat Exchangers

0 0.2 0.4 0.6 0.8 1 1.2 1.4 1.620

25

30

35

40

45

50

55

60

65

29

35

42

5552

50

29

37

44

60

56 55

29

35

39

53 5249

2931

34

4644

41

R1 Hot FluidR1 Cold FluidR2 Hot FluidR2 Cold FluidR3 Hot FluidR3 Cold fluidR4 Hot FluidR4 Cold Fluid

Distance along Length X

(m)

Tem

pera

tture

T (C)

2. For Counter-flow Arrangement

Procedure

1. Start the water supply. Adjust the water supply on hot and cold sides.2. Open the valves V2 & V3 and then close the valves V1 & V4. The arrangement is now counter

flow. 3. Switch ON the geyser. Temperature of water will start rising. 4. Wait until the steady state is reached and note down the readings.5. After temperatures become steady, note down the readings in the observation table.

Observations and Calculations

Length of pipe = L = 1.5 m

Tube outer diameter = do = (15x0.7) mm

Tube inner diameter = di = (22x0.9) mm

Set Temperature = 60°C

Transmission Area = A = 0.067 m2

Page 15: Heat Exchangers

Cold water Flow rate = Qc =1 ltr/min

Mass Flow rate of cold water,

mc=pQc=0.01667 kg/s

Density of water= 1000kg/m3

Specific Heat of Water= Cp= 4.186 kJ/kg°C

No. of obs.

Flowrate of hot water

Qh

Hot water Temperature (°C) Cold Water Temperature (°C)

(ltr/min) Inlet(Thi)

Mid Outlet (Tho)

Outlet(Tco)

Mid Inlet(Tci)

Atx=0m

At x=0.75m

At x=1.5m

Atx=0m

At x=0.75m

At x=1.5m

1. 1 53 48 47 43 36 292. 2 49 47 46 42 35 293. 3 50 48.5 48 40 36 294. 4 52 50.5 49.5 40 34 29

Sample Calculations

For Observation Set #04

Temperature Difference at inlet = ∆T 1=T hi−T ci=12C

Temperature Difference at Outlet =∆T 2=T ho−T co=20.5C

Log mean Temperature Difference = LMTD = ∆Tm= 15.85 C

Amount of heat Given out by hot liquid=

qemit=mh .Cp .(T hi−T ho)=436.04Watts

Amount of heat Absorbed by Cold Water,

q|¿|=mc .C p . (Tci−T co )=767.43Watts¿

Losses,

qemitt−q|¿|=0Watts¿

Efficiency of Heat Exchanger,

Ƞ=¿

Page 16: Heat Exchangers

Overall Heat Transfer Coefficient,

U=q|¿|/(At x ∆Tm )=721.8Watt /m2C ¿

Efficiency of cold water,

Ƞcoldwater=47.8 %

Efficiency of hot water,

Ƞhot water=10.9 %

Results Summary for all Readings

Flowrate of hot water

Qh

∆T1 ∆T2

LMTD∆Tm

qemit qabs U Ƞcold water Ƞhot water

(ltr/min) (C) (C) (C) Watts Watts Watt/m2C % %

1 10 18 13.61 418.6 976.73 1071 58.3 252 7 17 11.27 313.95 907 1201 65 153 10 19 14.02 279.1 767.43 817 52.4 9.54 12 20.5 15.87 436.04 767.43 721.8 47.8 10.9

Graphs

Scale: X-axis 1 big box=0.2 m Y-axis 1 big box=5 (C)

R1: for hot water Flow rate= Qh =1ltr/min R2: for hot water Flow rate= Qh =2ltr/min R3 :for hot water Flow rate= Qh =3ltr/min R4 :for hot water Flow rate= Qh =4ltr/min

Page 17: Heat Exchangers

0 0.2 0.4 0.6 0.8 1 1.2 1.4 1.625

30

35

40

45

50

55

40

34

29

5250.5 49.5

40

36

29

5048.5 48

42

35

29

4947 46

43

36

29

53

48 47

R1 Hot FluidR1 Cold FluidR2 Hot FluidR2 Cold FluidR3 Hot FluidR3 Cold fluidR4 Hot FluidR4 Cold Fluid

Distance along Length X

(m)

Tem

pera

tture

T (C)

(B)For variation in Cold fluid Flowrate

1. for parallel-flow Arrangement

Procedure

1. Start the water supply. Adjust the water supply on hot and cold sides.2. Keep the valves V2 & V3 closed and V1 & V4 opened so that arrangement is Parallel flow.3. Switch ON the geyser. Temperature of water will start rising. 4. After temperatures become steady, note down the readings in the observation table.5. Vary the hot water flowrate and repeat the same procedure.

Observations and Calculations

Length of pipe = L = 1.5 m

Tube outer diameter = do = (15x0.7) mm

Tube inner diameter = di = (22x0.9) mm

Set Temperature = 60°C

Transmission Area = A = 0.067 m2

Hot water Flow rate = Qh =2 ltr/min

Page 18: Heat Exchangers

Mass Flow rate of hot water,

mh=pQh=0.0333kg/ s

Density of water= 1000kg/m3

Specific Heat of Water= Cp= 4.186 kJ/kg°C

No. of obs.

Flowrate of cold

waterQc

Hot water Temperature (°C) Cold Water Temperature (°C)

(ltr/min) Inlet(Thi)

Mid Outlet (Tho)

Inlet(Tci)

Mid Outlet(Tco)

At x=0m

At x=0.75m

At x=1.5m

Atx=0m

At x=0.75m

At x=1.5m

1. 1 50 48 45 29 36.5 382. 1.5 49 44.5 44 29 31.5 35.53. 2 47.5 44 43 29 31 354. 2.5 46 42.5 42 29 30 34

Sample Calculations

For Observation Set #01

Temperature Difference at inlet = ∆T 1=T hi−T ci=21C

Temperature Difference at Outlet =∆T 2=T ho−T co=07C

Log mean Temperature Difference = LMTD = ∆Tm= 12.74 C

Amount of heat Given out by hot liquid=

qemit=mh .Cp .(T hi−T ho)=697.67Watts

Amount of heat Absorbed by Cold Water,

q|¿|=mc .C p . (Tci−T co )=627.9Watts¿

Losses,

qemitt−q|¿|=69.77Watts¿

Efficiency of Heat Exchanger,

Ƞ=¿

Overall Heat Transfer Coefficient,

Page 19: Heat Exchangers

U=q|¿|/(At x ∆Tm )=735.43Watt /m2C ¿

Efficiency of cold water,

Ƞcoldwater=42.85 %

Efficiency of hot water,

Ƞhot water=23.8 %

Results Summary for all Readings

Flowrate of cold water

Qc

∆T1 ∆T2 LMTD∆Tm

qemit qabs Losses UȠcold

water

Ƞhot

water

(ltr/min) (C) (C) (C) Watts Watts Watts Watt/m2C

% %

1 21 7 12.743 697.67 627.9 69.77 735.43 42.85 23.8.1.5 20 8.5 13.44 697.67 678.93 18.74 753.96 32.5 252 18.5 8 12.53 627.9 835.6 207.7 995.3 32.43 24.32

2.5 17 8 11.94 558.13 870.41 312.7 1088 29.4 23.53

Graphs

Scale: X-axis 1 big box=0.2 m Y-axis 1 big box=5 (C)

R1: for cold water Flow rate= Qc =1ltr/min R2: for cold water Flow rate= Qc =1.5ltr/min R3 :for cold water Flow rate= Qc =2ltr/min R4 :for cold water Flow rate= Qc =2.5ltr/min

Page 20: Heat Exchangers

0 0.2 0.4 0.6 0.8 1 1.2 1.4 1.625

30

35

40

45

50

55

29 30

34

46

42.5 42

2931

35

47.5

44 43

2931.5

35.5

49

44.5 44

29

36.538

5048

45R1 Hot FluidR1 Cold FluidR2 Hot FluidR2 Cold FluidR3 Hot FluidR3 Cold fluidR4 Hot FluidR4 Cold Fluid

Distance along Length X

(m)

Tem

pera

tture

T (C)

(2) for Counter-flow Arrangement

Procedure

1. Start the water supply. Adjust the water supply on hot and cold sides.2. Open the valves V2 & V3 and then close the valves V1 & V4. The arrangement is now counter

flow. 3. Switch ON the geyser. Temperature of water will start rising. 4. Wait until the steady state is reached and note down the readings.5. After temperatures become steady, note down the readings in the observation table.

Observations and Calculations

Length of pipe = L = 1.5 m

Tube outer diameter = do = (15x0.7) mm

Tube inner diameter = di = (22x0.9) mm

Set Temperature = 60°C

Transmission Area = A = 0.067 m2

Hot water Flow rate = Qh =2 ltr/min

Page 21: Heat Exchangers

Mass Flow rate of hot water,

mh=pQh=0.0333kg/ s

Density of water= 1000kg/m3

Specific Heat of Water= Cp= 4.186 kJ/kg°C

No. of obs.

Flowrate of cold

waterQc

Hot water Temperature (°C) Cold Water Temperature (°C)

(ltr/min) Inlet(Thi)

Mid Outlet (Tho)

Outlet(Tco)

Mid Inlet(Tci)

At x=0m

At x=0.75m

At x=1.5m

Atx=0m

At x=0.75m

At x=1.5m

1. 1 49 47 46 40 36 292. 1.5 41 40 38.5 33 31.5 293. 2 43 41 40 30 28.5 294. 2.5 44 41 40 30.5 28 29

Sample Calculations

For Observation Set #04

Temperature Difference at inlet = ∆T 1=T hi−T ci=13.5C

Temperature Difference at Outlet =∆T 2=T ho−T co=11C

Log mean Temperature Difference = LMTD = ∆Tm= 12.21 C

Amount of heat Given out by hot liquid=

qemit=mh .Cp .(T hi−T ho)=558.13Watts

Amount of heat Absorbed by Cold Water,

q|¿|=mc .C p . (Tci−T co )=296.5Watts¿

Losses,

qemitt−q|¿|=261.8Watts¿

Efficiency of Heat Exchanger,

Ƞ=¿

Overall Heat Transfer Coefficient,

Page 22: Heat Exchangers

U=q|¿|/(At x ∆Tm )=319.8Watt /m2C ¿

Efficiency of cold water,

Ƞcoldwater=12.6 %

Efficiency of hot water,

Ƞhot water=26.67 %

Results Summary for all Readings

Flowrate of cold water

Qc

∆T1 ∆T2

LMTD∆Tm qemit qabs Losses U Ƞcold

water

Ƞhot

water

(ltr/min) (C) (C) (C) Watts Watts Watts Watt/m2C

% %

1 9 17 12.58 418.6 765.96 -- 908.76 55 151.5 8 9.5 8.73 348.83 417.8 -- 714.3 33.3 20.82 13 11 11.97 418.6 139.53 279.07 173.97 7.1 21.42

2.5 13.5 11 12.21 558.13 261.63 296.5 319.8 12.6 26.67

Graphs

Scale: X-axis 1 big box=0.2 m Y-axis 1 big box=5 (C)

R1: for cold water Flow rate= Qc =1ltr/min R2: for cold water Flow rate= Qc =1.5ltr/min R3 :for cold water Flow rate= Qc =2ltr/min R4 :for cold water Flow rate= Qc =2.5ltr/min

Page 23: Heat Exchangers

0 0.2 0.4 0.6 0.8 1 1.2 1.4 1.625

30

35

40

45

50

55

30.528 29

44

41 40

3028.5 29

4341 40

3331.5

29

41 4038.5

40

36

29

4947 46

R1 Hot FluidR1 Cold FluidR2 Hot FluidR2 Cold FluidR3 Hot FluidR3 Cold fluidR4 Hot FluidR4 Cold Fluid

Distance along Length X

(m)

Tem

pera

tture

T (C)

Conclusion

The higher the flow rate the higher heat transfer, the higher the efficiency, and greater the temp change.

The pay back is the higher the flow rate, the greater the pressure loss, the bigger pump you need.

Page 24: Heat Exchangers

Lab Sesson#04

THEORYHeat exchangers are typically employed in the process industries as a means of providing heat transfer between two streams of fluid across a medium. The heat exchanger ensures the conservation of heat energy otherwise known as heat economic operations.

Effects of heat exchanger operating temperature

The heat exchanger operating temperature affects heat exchange. For example in refineries, stream temperatures can vary due to changes in the operating procedures. Any alterations in the stream temperature will create a variation in the approaches; the exchanger duty and log mean temperature difference. Low approach difference will give a corresponding log mean temperature difference, and high load vice versa. When the operating temperature limits are exceeded, the material condenses as a result of deposits and coats the internals of heat exchangers, which produces a wall temperature that is lower than the bulk limit temperature. To maintain the operating temperature, the inlet and outlet temperature must be monitored

Experiment#04

DETERMINE THE EFFECT OF TEMPERATURE VARIATION OF HOT FLUID (SET) TEMPERATURE ON THE PERFORMANCE OF A GIVEN HEAT EXCHANGER. (FOR BOTH PARALLEL AND COUNTER FLOW

ARRANGEMENTS)Apparatus

Double pipe heat exchanger Apparatus with both parallel and counter flow arrangement

1. for parallel-flow ArrangementProcedure

1. Start the water supply. Adjust the water supply on hot and cold sides.2. Keep the valves V2 & V3 closed and V1 & V4 opened so that arrangement is Parallel flow.3. Switch ON the geyser. Temperature of water will start rising. 4. After temperatures become steady, note down the readings in the observation table.5. Vary the hot fluid set temperature and repeat the same procedure.

Page 25: Heat Exchangers

Observations and Calculations

Length of pipe = L = 1.5 m

Tube outer diameter = do = (15x0.7) mm

Tube inner diameter = di = (22x0.9) mm

Set Temperature = 65°C

Transmission Area = A = 0.067 m2

Hot water Flow rate = Qh =2 ltr/min

Cold water Flow rate = Qc =1 ltr/min

Mass Flow rate of hot water,

mh=pQh=0.0333kg/ s

Mass Flow rate of cold water,

mc=pQc=0.01667 kg/s

Density of water= 1000kg/m3

Specific Heat of Water= Cp= 4.186 kJ/kg°C

No. of obs.

Set temperature of Hot water

Hot water Temperature (°C) Cold Water Temperature (°C)

(C) Inlet(Thi)

Mid Outlet (Tho)

Inlet(Tci)

Mid Outlet(Tco)

At x=0m

At x=0.75m

At x=1.5m

Atx=0m

At x=0.75m

At x=1.5m

1. 60 53 52 49 29 35 392. 65 50 47 46 29 33.5 38.53. 70 60 56 55 29 37 44

Sample Calculations

For Observation Set #01

Temperature Difference at inlet = ∆T 1=T hi−T ci=13.5C

Temperature Difference at Outlet =∆T 2=T ho−T co=11C

Log mean Temperature Difference = LMTD = ∆Tm= 12.21 C

Amount of heat Given out by hot liquid=

Page 26: Heat Exchangers

qemit=mh .Cp .(T hi−T ho)=558.13Watts

Amount of heat Absorbed by Cold Water,

q|¿|=mc .C p . (Tci−T co )=296.5Watts¿

Losses,

qemitt−q|¿|=261.8Watts¿

Efficiency of Heat Exchanger,

Ƞ=¿

Overall Heat Transfer Coefficient,

U=q|¿|/(At x ∆Tm )=319.8Watt /m2C ¿

Efficiency of cold water,

Ƞcoldwater=12.6 %

Efficiency of hot water,

Ƞhot water=26.67 %

Results Summary for all Readings

Flowrate of hot water

Qh

∆T1 ∆T2 LMTD∆Tm

qemit qabs Losses U Ƞcold

water

Ƞhot water

(ltr/min) (C) (C) (C) Watts Watts Watts Watt/m2C % %

123

Graphs

Scale: X-axis 1 big box=0.2 m Y-axis 1 big box=5 (C)

R1: for hot water set temperature= 60 C R1: for hot water set temperature= 65 C R1: for hot water set temperature= 70 C

Page 27: Heat Exchangers

0 0.2 0.4 0.6 0.8 1 1.2 1.4 1.625

30

35

40

45

50

55

60

65

29

37

44

60

5655

29

33.5

38

50

4746

29

35

39

5352

49

R1 Hot FluidR1 Cold FluidR2 Hot FluidR2 Cold FluidR3 Hot FluidR3 Cold fluid

Distance along Length X

(m)

Tem

pera

ttur

eT (C

)

2. for Counter-flow Arrangement

Procedure

Start the water supply. Adjust the water supply on hot and cold sides. Open the valves V2 & V3 and then close the valves V1 & V4. The arrangement is now counter

flow. Switch ON the geyser. Temperature of water will start rising. Wait until the steady state is reached and note down the readings. After temperatures become steady, note down the readings in the observation table. Change the set temperature and repeat above procedure.

Observations and Calculations

Length of pipe = L = 1.5 m

Tube outer diameter = do = (15x0.7) mm

Tube inner diameter = di = (22x0.9) mm

Set Temperature = 65°C

Transmission Area = A = 0.067 m2

Page 28: Heat Exchangers

Hot water Flow rate = Qh =2 ltr/min

Cold water Flow rate = Qc =1 ltr/min

Mass Flow rate of hot water,

mh=pQh=0.0333kg/ s

Mass Flow rate of cold water,

mc=pQc=0.01667 kg/s

Density of water= 1000kg/m3

Specific Heat of Water= Cp= 4.186 kJ/kg°C

No. of obs.

Set temperature of Hot water

Hot water Temperature (°C) Cold Water Temperature (°C)

(C) Inlet(Thi)

Mid Outlet (Tho)

Outlet(Tco)

Mid Inlet(Tci)

At x=0m

At x=0.75m

At x=1.5m

Atx=0m

At x=0.75m

At x=1.5m

1. 60 49 47 46 41 36 292. 65 55 51 50 40 34 293. 70 50 48.5 48 43 36 29

Sample Calculations

For Reading#01

Temperature Difference at inlet = ∆T 1=T hi−T ci=13.5C

Temperature Difference at Outlet =∆T 2=T ho−T co=11C

Log mean Temperature Difference = LMTD = ∆Tm= 12.21 C

Amount of heat Given out by hot liquid=

qemit=mh .Cp .(T hi−T ho)=558.13Watts

Amount of heat Absorbed by Cold Water,

q|¿|=mc .C p . (Tci−T co )=296.5Watts¿

Losses,

qemitt−q|¿|=261.8Watts¿

Page 29: Heat Exchangers

Efficiency of Heat Exchanger,

Ƞ=¿

Overall Heat Transfer Coefficient,

U=q|¿|/(At x ∆Tm )=319.8Watt /m2C ¿

Efficiency of cold water,

Ƞcoldwater=12.6 %

Efficiency of hot water,

Ƞhot water=26.67 %

Results Summary for all Readings

Flowrate of hot water

Qh

∆T1 ∆T2 LMTD∆Tm

qemit qabs Losses U Ƞcold

water

Ƞhot water

(ltr/min) (C) (C) (C) Watts Watts Watts Watt/m2C % %

123

Graphs

Scale: X-axis 1 big box=0.2 m Y-axis 1 big box=5 (C)

R1: for hot water set temperature= 60 C R1: for hot water set temperature= 65 C R1: for hot water set temperature= 70 C

Page 30: Heat Exchangers

0 0.2 0.4 0.6 0.8 1 1.2 1.4 1.625

30

35

40

45

50

55

60

43

36

29

5048.5 48

40

34

29

55

5150

41

36

29

4947

46

R1 Hot FluidR1 Cold FluidR2 Hot FluidR2 Cold FluidR3 Hot FluidR3 Cold fluid

Distance along Length X

(m)

Tem

pera

ttur

eT (C

)


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