Single-shell, two-tube pass heat exchanger with surface area 0.4 m? andoverall heat transfer coefficient of 1800 W/m2-K; saturated steam at 110°Ccondenses on one side while water at a flow rate of 0.35 kg/s enters at 17°C.Calculate (a) Outlet temperature of the water (b) Rate of condensation of steam.cp(water)=4179 J/kg. K.916 IThermodynamicsTABLE A-4Saturated water-Temperature tableInternal energy,Specific volume,m/kgEnthalpy.KJ/kgEntropy,kJ/kg - Kk/kgSa.SatSat.Sat.Sat.Sat.Sat.Sat.liquid, Evap., vapor,Sat.Temp.,liquid,liquid,Evap..liquid,Evap.,press.Pst kPavapor,vapor,vapor,T°CUphe0.0010000.0010000.00021.01942.0202374.92374.90.00121.02042.0220.0000 9.1556 9.15560.07630.1511 8.7488 8.89990.2245 8.5559 8.78030.2965 8.3696 8.66610.015100.61170.87251.2281206.00147.03106.322360.82346.62381.82388.72500.92489.12477.22500.92510.12519.28.9487 9.024915200.0010000.0010012.3392 0.0010022332.52318.42395.52402.32465.42453.51.705777.88562.98083.91362.98283.9152528.32537.457.762104.83125.73146.63167.53188.4325300.3672 8.1895 8.55670.4368 8.0152 8.45200.5051 7.8466 8.35170.5724 7.6832 8.25560.6386 7.5247 8.16333.16980.00100343.34032.8792304.32290.22276.02409.12415.92422.7104.83125.742441.72429.82546.54.24690.0010042555.62564.62573.53540455.6291 0.0010067.3851 0.0010089.595325.20519.51515.2512261.92247.72429.42436.1146.64167.53188.442417.92406.0-2394.00.0010102582.4209.332233.42219.12204.72190.35012.3522382.00.0010120.0010150.00101712.0269.56397.66706.19352442.72449.3209.342591.30.7038 7.3710 8.074815.7635560650.7680 7.2218 7.98980.83130.8937 6.9360 7.82960.9551 6.7989 7.754O230.24251.16230.26251.18272.122369.82357.72600.12608.819.9477.0769 7.90820.0010200.0010232455.92462.42468.925.043272.09293.042345.42333.02617.52626.17031.2025.03962175.8293.07313.9975802161.32146.62131.92475.32481.638.5970.0010260.0010290.0010324.12913.40532.8261314.032320.62308.02295.32282.52269.61.0158 6.6655 7.68121.0756 6.5355 7.61111.1346 6.4089 7.54351.19291.2504 6.1647 7.41512634.62643.047.41657.86870.183334.97355.96335.02356.0285902487.82117.02102.02494.02500.12651.42659.62667.66.2853 7.47820.0010360.0010402.35931.9808376.97398.00377.04398.099584.609101.42120.90143.38169.182087.02071.82056.42040.91000.0010430.0010470.0010521.67201.4186419.062506.0419.172675.62683.42691.12698.62706.02256.41.3072 6.0470 7.35422511.92517.7105440.15461.27440.28461.422243.11101150.0010560.0010601.20941.03600.891332229.72216.02202.11.3634 5.9319 7.29521.4188 5.8193 7.23821.4737 5.7092 7.18292523.32528.9482.42482.59503.81120198.67503.602025.31.5279 5.6013 7.1292125130135232.23270.28313.220.0010650.0010700.0010750.0010800.0010850.770120.668080.58179524.83546.10567.412009.51993.41977.32534.32539.52544.7525.07546.38567.752713.12720.12726.92188.12173.71.5816 5.4956 7.07711.6346 5.3919 7.0265140145361.53415.680.508500.446002549.62554.42159,12144.32129.21.6872 5.2901 6.97731.7392 5.1901 6.92941.7908 5.0919 6.8827588.771960.91944.2589.16610.642733.5610.192739.8150155476.16543.490.0010910.0010960.392480.34648631.66653.19674.791927.41910.31893.02113.82098.01.8418 4.9953 6.83711.89241.94262559.1632.18653.792745.92563.52567.82571.92575.72751.82757.52762.84.9002 6.79274.8066 6.7492160165170618.23700.93792.180.0011020.0011080.0011140.306800.272440.24260696.46718.201875.41857.5675.47697.24719.082082.02065.61.9923 4.7143 6.70672.04172048.82767.94.6233 6.6650175892.601002.81123.51255.20.0011210.21659740.021839.42579.4741.022031.72772.72.0906 4.5335 6.62420.0011270.0011340.0011410.0011490.001157761.92783.91763.05785.19807.434.4448 6.58411801851900.193841820.91802.11783.02582.82586.02589.02014.21996.21977.92777.22781.42.13922.1875 4.3572 6.54472.2355 4.2705 6.50592.28310.173902785.32788.82792.00.15636806.00828.18850.461954.1847 6.46781398.81554.90.140890.127211763.61743.72591.72594.2829.78852.261959.01939.82002.3305 4.0997 6.4302

TS=110°CT1=17°CT2 =?m˙=0.35kg/secCp=4179j/kg-kU= 1800w/m2-k∆T= log mean temp difference

Single-shell, two-tube pass heat exchanger with surface area 0.4 m2 and overall heat transfer coefficient of 1800 W/m2.K; saturated steam at 110°C condenses on one side while water at a flow rate of 0.35 kg/s enters at 17°C. Calculate (a) Outlet temperature of the water (b) Rate of condensation of steam. cp(water)=4179 J/kg. K. 016 Thermodynamics

Single-shell, two-tube pass heat exchanger with surface area 0.4 m2 and overall heat transfer coefficient of 1800 W/m2.K; saturated steam at 110°C condenses on one side while water at a flow rate of 0.35 kg/s enters at 17°C. Calculate (a) Outlet temperature of the water (b) Rate of condensation of steam. cp(water)=4179 J/kg. K. 016 Thermodynamics

Elements Of Electromagnetics

7th Edition

ISBN:9780190698614

Author:Sadiku, Matthew N. O.

Publisher:Sadiku, Matthew N. O.

ChapterMA: Math Assessment

Section: Chapter Questions

Problem 1.1MA

See similar textbooks

Related questions

Q: Heat transfer problem.In a counter flow heat exchanger, water, flow rate 0.05kg/s, enters at 400K…

Q: A doube pipe heat exchangeris to be designed to heat 1 kg/s of cold fluid from 30 degree celusis to…

A: Heat Exchanger is a steady flow adiabatic device(open system) in which two flowing fluids exchange…

Q: QUESTION 8 A concentric-tube, counter-flow heat exchanger, as shown below, is used to cool mercury…

Q: Nanofluids are at the spot of consideration for new generation of heat exchangers. As a process…

A: Nanofluid is the suspension of nanoparticles made up of metal oxide and carbon tube etc. it is used…

Q: I have exam tomorrow and need to practice and I’m stuck ! Help

A: 1.Advantages and Disadvantages of Flat Plate Heat Exchangers Advantages:Compactness: Flat plate…

Q: Don't use chatgpt will upvote

A: 1. Vertical Position EquationY(t)=V0t−21gt2V0 is the initial speed of the ball,g is the…

Q: (1) In a double tube heat exchanger in which hot and cold fluids flow into a countercurrent flow,…

A: We will answer the first question since the exact one is not specified. Please resubmit the question…

Q: A vegetable soup, with specific heat capacity 4000 J/(kg. K), is being heated from 21 to 97 °C…

A: Given:For vegetable soup:For steam:The overall heat transfer coefficient = To find:The rate of heat…

Q: i) ii) State the assumptions used to arrive at the above equation. Explain why the "log-mean"…

A: This question is based on the concept of Heat exchanger.

Q: derive Hagen-poiseuille equation from the friction factor given.

A: Derivation of the Hagen-Poiseuille equation: A cylindrical liquid element (liquid package) of radius…

Q: 1. Calculate the (UA) of 3771k12 model at McMaster Carr? With more than three times the pressure…

A: The main basic Heat Exchanger equation is: Q = U x A x ΔTm ΔTm =…

Q: concentric-pipe heat exchanger, one of the fluids is a condensing vapour and the other is the…

A: This question is based on the concept of concentric-pipe heat exchanger.

Q: Required information Consider operation of a single-pass cross-flow heat exchanger with water…

Concept explainers

Heat Exchangers

Heat exchangers are the types of equipment that are primarily employed to transfer the thermal energy from one fluid to another, provided that one of the fluids should be at a higher thermal energy content than the other fluid.

Heat Exchanger

The heat exchanger is a combination of two words ''Heat'' and ''Exchanger''. It is a mechanical device that is used to exchange heat energy between two fluids.

Question

100%

Single-shell, two-tube pass heat exchanger with surface area 0.4 m? and
overall heat transfer coefficient of 1800 W/m2-K; saturated steam at 110°C
condenses on one side while water at a flow rate of 0.35 kg/s enters at 17°C.
Calculate (a) Outlet temperature of the water (b) Rate of condensation of steam.
cp(water)=4179 J/kg. K.
916 I
Thermodynamics
TABLE A-4
Saturated water-Temperature table
Internal energy,
Specific volume,
m/kg
Enthalpy.
KJ/kg
Entropy,
kJ/kg - K
k/kg
Sa.
Sat
Sat.
Sat.
Sat.
Sat.
Sat.
Sat.
liquid, Evap., vapor,
Sat.
Temp.,
liquid,
liquid,
Evap..
liquid,
Evap.,
press.
Pst kPa
vapor,
vapor,
vapor,
T°C
Up
he
0.001000
0.001000
0.000
21.019
42.020
2374.9
2374.9
0.001
21.020
42.022
0.0000 9.1556 9.1556
0.0763
0.1511 8.7488 8.8999
0.2245 8.5559 8.7803
0.2965 8.3696 8.6661
0.01
5
10
0.6117
0.8725
1.2281
206.00
147.03
106.32
2360.8
2346.6
2381.8
2388.7
2500.9
2489.1
2477.2
2500.9
2510.1
2519.2
8.9487 9.0249
15
20
0.001000
0.001001
2.3392 0.001002
2332.5
2318.4
2395.5
2402.3
2465.4
2453.5
1.7057
77.885
62.980
83.913
62.982
83.915
2528.3
2537.4
57.762
104.83
125.73
146.63
167.53
188.43
25
30
0.3672 8.1895 8.5567
0.4368 8.0152 8.4520
0.5051 7.8466 8.3517
0.5724 7.6832 8.2556
0.6386 7.5247 8.1633
3.1698
0.001003
43.340
32.879
2304.3
2290.2
2276.0
2409.1
2415.9
2422.7
104.83
125.74
2441.7
2429.8
2546.5
4.2469
0.001004
2555.6
2564.6
2573.5
35
40
45
5.6291 0.001006
7.3851 0.001008
9.5953
25.205
19.515
15.251
2261.9
2247.7
2429.4
2436.1
146.64
167.53
188.44
2417.9
2406.0
-2394.0
0.001010
2582.4
209.33
2233.4
2219.1
2204.7
2190.3
50
12.352
2382.0
0.001012
0.001015
0.001017
12.026
9.5639
7.6670
6.1935
2442.7
2449.3
209.34
2591.3
0.7038 7.3710 8.0748
15.763
55
60
65
0.7680 7.2218 7.9898
0.8313
0.8937 6.9360 7.8296
0.9551 6.7989 7.754O
230.24
251.16
230.26
251.18
272.12
2369.8
2357.7
2600.1
2608.8
19.947
7.0769 7.9082
0.001020
0.001023
2455.9
2462.4
2468.9
25.043
272.09
293.04
2345.4
2333.0
2617.5
2626.1
70
31.202
5.0396
2175.8
293.07
313.99
75
80
2161.3
2146.6
2131.9
2475.3
2481.6
38.597
0.001026
0.001029
0.001032
4.1291
3.4053
2.8261
314.03
2320.6
2308.0
2295.3
2282.5
2269.6
1.0158 6.6655 7.6812
1.0756 6.5355 7.6111
1.1346 6.4089 7.5435
1.1929
1.2504 6.1647 7.4151
2634.6
2643.0
47.416
57.868
70.183
334.97
355.96
335.02
356.02
85
90
2487.8
2117.0
2102.0
2494.0
2500.1
2651.4
2659.6
2667.6
6.2853 7.4782
0.001036
0.001040
2.3593
1.9808
376.97
398.00
377.04
398.09
95
84.609
101.42
120.90
143.38
169.18
2087.0
2071.8
2056.4
2040.9
100
0.001043
0.001047
0.001052
1.6720
1.4186
419.06
2506.0
419.17
2675.6
2683.4
2691.1
2698.6
2706.0
2256.4
1.3072 6.0470 7.3542
2511.9
2517.7
105
440.15
461.27
440.28
461.42
2243.1
110
115
0.001056
0.001060
1.2094
1.0360
0.89133
2229.7
2216.0
2202.1
1.3634 5.9319 7.2952
1.4188 5.8193 7.2382
1.4737 5.7092 7.1829
2523.3
2528.9
482.42
482.59
503.81
120
198.67
503.60
2025.3
1.5279 5.6013 7.1292
125
130
135
232.23
270.28
313.22
0.001065
0.001070
0.001075
0.001080
0.001085
0.77012
0.66808
0.58179
524.83
546.10
567.41
2009.5
1993.4
1977.3
2534.3
2539.5
2544.7
525.07
546.38
567.75
2713.1
2720.1
2726.9
2188.1
2173.7
1.5816 5.4956 7.0771
1.6346 5.3919 7.0265
140
145
361.53
415.68
0.50850
0.44600
2549.6
2554.4
2159,1
2144.3
2129.2
1.6872 5.2901 6.9773
1.7392 5.1901 6.9294
1.7908 5.0919 6.8827
588.77
1960.9
1944.2
589.16
610.64
2733.5
610.19
2739.8
150
155
476.16
543.49
0.001091
0.001096
0.39248
0.34648
631.66
653.19
674.79
1927.4
1910.3
1893.0
2113.8
2098.0
1.8418 4.9953 6.8371
1.8924
1.9426
2559.1
632.18
653.79
2745.9
2563.5
2567.8
2571.9
2575.7
2751.8
2757.5
2762.8
4.9002 6.7927
4.8066 6.7492
160
165
170
618.23
700.93
792.18
0.001102
0.001108
0.001114
0.30680
0.27244
0.24260
696.46
718.20
1875.4
1857.5
675.47
697.24
719.08
2082.0
2065.6
1.9923 4.7143 6.7067
2.0417
2048.8
2767.9
4.6233 6.6650
175
892.60
1002.8
1123.5
1255.2
0.001121
0.21659
740.02
1839.4
2579.4
741.02
2031.7
2772.7
2.0906 4.5335 6.6242
0.001127
0.001134
0.001141
0.001149
0.001157
761.92
783.91
763.05
785.19
807.43
4.4448 6.5841
180
185
190
0.19384
1820.9
1802.1
1783.0
2582.8
2586.0
2589.0
2014.2
1996.2
1977.9
2777.2
2781.4
2.1392
2.1875 4.3572 6.5447
2.2355 4.2705 6.5059
2.2831
0.17390
2785.3
2788.8
2792.0
0.15636
806.00
828.18
850.46
195
4.1847 6.4678
1398.8
1554.9
0.14089
0.12721
1763.6
1743.7
2591.7
2594.2
829.78
852.26
1959.0
1939.8
200
2.3305 4.0997 6.4302

Expert Solution

This question has been solved!

Explore an expertly crafted, step-by-step solution for a thorough understanding of key concepts.

SEE SOLUTION Check out a sample Q&A here

Step 1

Step 2

Step 3

Step 4

Step by step

Solved in 4 steps

SEE SOLUTION Check out a sample Q&A here

Knowledge Booster

Learn more about

Need a deep-dive on the concept behind this application? Look no further. Learn more about this topic, mechanical-engineering and related others by exploring similar questions and additional content below.

Similar questions

Question about heat exchanger
Below data was obtained from an experimental activity for a parallel pipe heat exchanger. Arrangement: counterflow (cold fluid in annular and hot fluid in tube). Mass flow rate: - Hot fluid: 1.03 kg/s - Cold fluid: 0.91 kg/s Temperatures: - Hot fluid inlet (Th.1): 80.5 +/- 10% °C - Hot fluid outlet (Th2): 64.0 +/- 10% °C - Cold fluid inlet (Te1): 20.0 +/- 10% °C - Cold fluid outlet (Tc2): 41.0 +/- 10% °C Assume cp constant and equal to 4.2 kJ/kg-K. 1. State assumptions (at least 9 unique ones) and include references. 2. What is the log mean temperature difference in °C? 3. What is the heat transfer rate on the cold side in kW? Heat added or lost on cold side? 4. What is the heat transfer rate on the hot side in kW? Heat added or lost on hot side? 5. What is the effectiveness of the heat exchanger for the given conditions? 6. Calculate the propagation of uncertaintv in kW for part 3 (heat transfer rate on the cold side) and part 4 (heat transfer rate on the hot side).
i just need F, G, H answered!
The condenser of a large thermal power plant consists of a single body with two passes each and 30000 pipes.It is a shell and tube type heat exchanger. Pipes are 25 mm inner diameter, thin-walled and steam,11000 W / m2With a convection coefficient of .K, it condenses on the outer surfaces of the pipe. HeatThe transfer required by the exchanger is 2000 MW, and 30000 kg / h of water will be transferred from the pipes.as with flowing flow rate. Water enters at a temperature of 20 ° C, steam at 50 ° C.is condensing. Calculation temperature of the cooling water from the condenser? Required per passdetermine the pipe length? The properties of water at Tort = 300 K; Cp = 4180 j / kgK, μ = 855 × 10--6 Ns / m2,k = 0.613 W / mK, Pr = 5.83.