How can we use Fundamental Heat Transfer to understand real devices like heat exchangers?
|
|
- Linette Miller
- 6 years ago
- Views:
Transcription
1 Lectures CM30 /30/05 CM30 Transport I Part II: Heat Transfer Applied Heat Transfer: Heat Exchanger Modeling, Sizing, and Design Professor Faith Morrison Department of Chemical Engineering Michigan Technological University Before turning to radiation (last topic) we will discuss a few practical applications How can we use Fundamental Heat Transfer to understand real devices like heat exchangers?
2 Lectures CM30 /30/05 The Simplest Heat Exchanger: Double Pipe Heat exchanger counter current T less hot T T cold less cold The heat transfer from the outside to the inside is just heat flux in an annular shell T hot 3 Example 4: Heat flux in a cylindrical shell Assumptions: long pipe steady state k = thermal conductivity of wall h, h = heat transfer coefficients Maybe we can use heat transfer coefficient to understand forcedconvection heat exchangers... BUT... Cooler fluid at T b r R R Hot fluid at T b 4
3 Lectures CM30 /30/05 BUT: The temperature difference between the fluid and the wall varies along the length of the heat exchanger. The Simplest Heat Exchanger: Double Pipe Heat exchanger counter current T T T, outer bulk temperature, inner bulk temperature T T cold less hot less cold How can we adapt h so that we can use the concept to characterize heat exchangers? L x T hot 5 Let s look at the solution for radial conduction in an annulus Example 4: Heat flux in a cylindrical shell Solution: q r c A r c T ln r c k Not constant Boundary conditions? 6 3
4 Lectures CM30 /30/05 Example 4: Heat flux in a cylindrical shell, Newton s law of cooling boundary Conditions Results: Radial Heat Flux in an Annulus ln ln ln 7 Cooler Example 4: Heat flux in a cylindrical shell R Solution for Heat Flux: Hot fluid at T b r ln R fluid at T b Calculate Total Heat flow: ln Note that total heat flow is proportional to bulk Δ and (almost) area of heat transfer 8 4
5 Lectures CM30 /30/05 T = driving temperature difference 9 Q U A T Area must be specified when is reported Q U AT 0 5
6 Lectures CM30 /30/05 Heat flux in a cylindrical shell: But, in an actual heat exchanger, and vary along the length of the heat exchanger What kind of average do we use? T T T, outer bulk temperature, inner bulk temperature T T cold The Simplest Heat Exchanger: Double Pipe Heat exchanger counter current less hot less cold We will do an open system energy balance on a differential section to determine the correct average temperature difference to use. L x T hot 6
7 Lectures CM30 /30/05 The Simplest Heat Exchanger: Double Pipe Heat exchanger counter current Another way of looking at it: T less hot T T cold less cold T hot Inside System Outside System 3 The Simplest Heat Exchanger: Double Pipe Heat exchanger counter current Another way of looking at it: T less hot T T cold less cold Can do three balances: T hot. Balance on the inside system Inside System Outside System 4 7
8 Lectures CM30 /30/05 The Simplest Heat Exchanger: Double Pipe Heat exchanger counter current Another way of looking at it: T less hot T T cold less cold Can do three balances: T hot. Balance on the inside system. Balance on the outside system Inside System Outside System 5 The Simplest Heat Exchanger: Double Pipe Heat exchanger counter current Another way of looking at it: T less hot T T cold less cold Can do three balances: T hot. Balance on the inside system. Balance on the outside system 3. Overall balance Inside System Outside System 6 8
9 Lectures CM30 /30/05 The Simplest Heat Exchanger: Double Pipe Heat exchanger counter current Another way of looking at it: T less hot T T cold less cold T hot Inside System Outside System We can do: a macroscopic balances over the entire heat exchanger, or a pseudo microscopic balance over a slice of the heat exchanger 7 The Simplest Heat Exchanger: Double Pipe Heat exchanger counter current Another way of looking at it: T less hot T T cold less cold T hot Inside System Outside System We can do: a macroscopic balances over the entire heat exchanger, or a pseudo microscopic balance over a slice of the heat exchanger All the details of the algebra are here: 8 9
10 Lectures CM30 /30/05 Pseudo Microscopic Energy Balance on a slice of the heat exchanger 9 Pseudo Microscopic Energy Balance on a slice of the heat exchanger 0 0
11 Lectures CM30 /30/05 Pseudo Microscopic Energy Balance on a slice of the heat exchanger Adiabatic Heat Exchanger > Q in = 0 This expression characterizes the rate of change of heat transferred with respect to distance down the heat exchanger
12 Lectures CM30 /30/05 The Simplest Heat Exchanger: Double Pipe Heat exchanger counter current T less hot Result of inside balance: Result of outside balance: Result of overall balance: Solve for temperature derivatives, and subtract: This depends on T T cold less cold T hot All the details of the algebra are here: 3 Analysis of double pipe heat exchanger (continued) T (x) T T T T T L T Rate of change of heat transferred with respect to distance down the heat exchanger Driving force for heat transfer Question: dq How can we write in in terms of T ' T? dx Answer: Define an overall heat transfer coefficient, U 4
13 Lectures CM30 /30/05 Want to integrate to solve for, T (x) T T T T L T T but this is a function of For the differential slice of the heat exchanger that we are considering (modeling our ideas on Newton s law of cooling),? 5 For the differential slice of the heat exchanger that we are considering (modeling our ideas on Newton s law of cooling),? This is the missing piece that we needed. We can write in terms of if we define an overall heat transfer coefficient, 6 3
14 Lectures CM30 /30/05 7 Φ (we ll assume is constant) Φ Φ Φ Φ lnφ constant ΦΦ B.C: 0, 8 4
15 Lectures CM30 /30/05 T less hot Temperature profile in a double pipe heat exchanger: T T cold less cold T hot T TT T 0 e x 0 RU Cˆ m p Cˆ pm 9 T less hot T T cold T hot less cold x T T 0L L TT e T, T' ( o C) T T U 300 W / mk RL 5.4m ' mc p 6 kw / K mc 3 kw / K p Note that the temperature curves are not linear x/l Distance down the heat exchanger 30 5
16 Lectures CM30 /30/05 Temperature profile in a double pipe heat exchanger: T TT T 0 e x 0 RU Cˆ m p Cˆ pm Useful result, but what we REALLY want is an easy way to relate, to inlet and outlet temperatures. At the exit:, T T ln T T U RL Cˆ m p Cˆ pm 3 T T ln T T U RL Cˆ m p Cˆ pm The terms appear in the overall macroscopic energy balances. We can therefore rearrange this equation by replacing the terms with : total heat transferred in exchanger ln average temperature driving force 3 6
17 Lectures CM30 /30/05 T less hot FINAL RESULT: Q U T T T T RL T T ln T T A T T cold less cold T hot Q UA T lm T lm =log mean temperature difference T lm is the correct average temperature to use for the overall heattransfer coefficients in a double pipe heat exchanger. 33 T less hot FINAL RESULT: T T cold less cold Δ Δ ln Δ Δ T hot Q UA T lm T lm =log mean temperature difference T lm is the correct average temperature to use for the overall heattransfer coefficients in a double pipe heat exchanger. 34 7
18 Lectures CM30 /30/05 Example: Heat Transfer in a Double Pipe Heat Exchanger: Geankoplis 4 th ed Water flowing at a rate of 3.85 kg/s is to be heated from 54.5 to 87.8 o C in a double pipe heat exchanger by 54,430 kg/h of hot gas flowing counterflow and entering at 47 o C (.005 / ). The overall heat transfer coefficient based on the outer surface is U o =69. W/m K. Calculate the exit gas temperature and the heat transfer area needed. 35 Cp, water kj/kg K y = x R = T ( o C) 36 8
19 Lectures CM30 /30/05 Summary: Double Pipe Heat Exchanger the driving force for heat transfer changes along the length of the heat xchanger For example, T 300 o C o T T C T 340 xx8 T 50 o C T 90 0 C o T T C T 50 xx T(x) T 430 o C The correct average driving force for the whole xchanger is the log mean temperature difference T lm 37 Optimizing Heat Exchangers double-pipe: T T T T Q UA T lm To increase Q appreciably, we must increase A, i.e. R i But: only small increases possible increasing R i decreases h 38 9
20 Lectures CM30 /30/05 - Shell and Tube Heat Exchanger (Same as double pipe H.E.) shell tube - Shell and Tube Heat Exchanger Geankoplis 4 th ed., p9 shell tube 39 Cross Baffles in Shell-and-Tube Heat Exchangers 40 0
21 Lectures CM30 /30/05 And other more complex arrangements: shell 4 tube 4 For double-pipe heat exchanger: Q UA T lm For shell-and-tube heat exchangers: Q UA T lm F T calculated correction factor (obtain from experimentally determined charts) T m correct mean temperature difference for shell-and-tube heat exchangers 4
22 Lectures CM30 /30/05 - Shell and Tube H.E. F T Shell-and-Tube Heat Exchangers (- exchanger, F T = ) F T,min =0.75 Efficiency is low when is below, -4 Shell and Tube H.E. T hi = hot, in T ho = hot, out T ci = cold, in T co = cold, out F T,min =0.75 Geankoplis 4 th ed., p95 43 Heat Exchanger Design To calculate Q, we need both inlet and outlet temperatures: Q UAT T m UA F T T lm T T Δ Δ ln Δ Δ T What if the outlet temperatures are unknown? i.e. the design/spec problem. 44
23 Lectures CM30 /30/05 Example Problem: How will this heat exchanger perform? Water flowing at a rate of 0.73 / enters the inside of a countercurrent, double-pipe heat exchanger at 300.K and is heated by an oil stream that enters at 385 at a rate of 3. /. The heat capacity of the oil is.89 /, and the average heat capacity of the water of the temperature range of interest is 4.9 /. The overall heattransfer coefficient of the exchanger is 300. /, and the area for heat transfer is 5.4. What is the total amount of heat transferred? 45 T Example Problem: How will this heat exchanger perform? T T T Water flowing at a rate of enters the inside of a countercurrent, double-pipe heat exchanger at 300.K and is heated by an oil stream that enters at at a rate of. The heat capacity of the oil is, and the average heat capacity of the water of the temperature range of interest is. The overall heattransfer coefficient of the exchanger is, and the area for heat transfer is. What is the total amount of heat transferred? You try. 46 3
24 Lectures CM30 /30/05 Example Problem: How will this heat exchanger perform? To calculate unknown outlet temperatures: Procedure:. Guess Q. Calculate outlet temperatures 3. Calculate Δ 4. Calculate Q 5. Compare, adjust, repeat 47 Example Problem: How will this heat exchanger perform? U A T_ Tprime_ m_water m'_oil cp_water cp_oil 0.3 kw/m^k 5.4 m^ 300 K 385 K 0.73 kg/s 3. kg/s 4.9 kj/kgk.89 kg/kgk Guess Q 00 kj/s Guess Q 00 kj/s 3 Guess Q 50 kj/s T_ 333 K T_ 366 K T_ 349 K Tprime_ 368 K Tprime_ 35 K Tprime_ 360 K Delta left 68 K Delta left 5 K Delta left 60 K Delta Right 5 K Delta Right 9 K Delta Right 36 K DeltaTlm 60 K DeltaTlm 33 K DeltaTlm 47 K Q_new 76.5 kw Q_new 5.4 kw Q_new 6. kw 4 Guess Q 70 kj/s 5 Guess Q 80 kj/s 6 Guess Q 78.6 kj/s T_ 356 K T_ 359 K T_ 359 K Tprime_ 357 K Tprime_ 355 K Tprime_ 355 K Delta left 57 K Delta left 55 K Delta left 55 K Delta Right 9 K Delta Right 6 K Delta Right 6 K DeltaTlm 4 K DeltaTlm 39 K DeltaTlm 39 K Q_new 9.0 kw Q_new 78. kw Q_new 79.9 kw 03HeatExchEffecExample.xlsx 48 4
25 Lectures CM30 /30/05 Example Problem: How will this heat exchanger perform? U A T_ Tprime_ m_water m'_oil cp_water cp_oil 0.3 kw/m^k 5.4 m^ 300 K 385 K 0.73 kg/s 3. kg/s 4.9 kj/kgk.89 kg/kgk This procedure can be sped up considerably by the use of the concept of Heat-Exchanger Effectiveness, Guess Q 00 kj/s Guess Q 00 kj/s 3 Guess Q 50 kj/s T_ 333 K T_ 366 K T_ 349 K Tprime_ 368 K Tprime_ 35 K Tprime_ 360 K Delta left 68 K Delta left 5 K Delta left 60 K Delta Right 5 K Delta Right 9 K Delta Right 36 K DeltaTlm 60 K DeltaTlm 33 K DeltaTlm 47 K Q_new 76.5 kw Q_new 5.4 kw Q_new 6. kw 4 Guess Q 70 kj/s 5 Guess Q 80 kj/s 6 Guess Q 78.6 kj/s T_ 356 K T_ 359 K T_ 359 K Tprime_ 357 K Tprime_ 355 K Tprime_ 355 K Delta left 57 K Delta left 55 K Delta left 55 K Delta Right 9 K Delta Right 6 K Delta Right 6 K DeltaTlm 4 K DeltaTlm 39 K DeltaTlm 39 K Q_new 9.0 kw Q_new 78. kw Q_new 79.9 kw 03HeatExchEffecExample.xlsx 49 Heat Exchanger Effectiveness Consider a counter-current double-pipe heat exchanger: T co T hi T ho T hi T co T ho T ci distance along the exchanger T ci 50 5
26 Lectures CM30 /30/05 Energy balance cold side: Q in, cold Q mc T T p cold co ci Equate: Energy balance hot side: Q Q mc T T in, hot p hot ho hi mc mc p hot p cold T co Tci Tc T ho Thi Th 5 Case : mc mc c p hot T T h T hi p cold cold fluid = minimum fluid Δ Δ T co T h We want to compare the amount of heat transferred in this case to the amount of heat transferred in a PERFECT heat exchanger. T c distance along the exchanger T ho T ci 5 6
27 Lectures CM30 /30/05 If the heat exchanger were perfect, (no heat left un-transferred) cold side: Thi T co A T ho T ci this temperature difference only depends on inlet temperatures distance along the exchanger 53 Heat Exchanger Effectiveness, Q Q A Q mc T T p cold hi ci cold fluid = minimum fluid if is known, we can calculate Q without iterations 54 7
28 Lectures CM30 /30/05 Case : mc mc c p hot T T h p cold hot fluid = minimum fluid Δ Δ T hi T h T co T c T ho T ci distance along the exchanger 55 If the heat exchanger were perfect, (no heat left un-transferred) hot side: T hi T co A Tho T ci The same temperature difference as before (inlets) distance along the exchanger 56 8
29 Lectures CM30 /30/05 Heat Exchanger Effectiveness Q mc T T p hot hi ci Q Q A hot fluid = minimum fluid in general, Q mc T T p min hi if is known, we can calculate without iterations ci 57 But where do we get? The same equations we use in the trial-and-error solution can be combined algebraically to give as a function of (mc p ) min, (mc p ) max. countercurrent flow: e mc mc UA mc p min p max This relation is plotted in Geankoplis, as is the relation for co-current flow. p min e mc mc UA mc p min p min p max mc mc p min p min 58 9
30 Lectures CM30 /30/05 Heat Exchanger Effectiveness for Double-pipe or - Shell-and-Tube Heat Exchangers counter-current co-current note: Geankoplis C min =(mc p ) min Geankoplis 4 th ed., p99 59 T Example Problem: How will this heat exchanger perform? T T T Water flowing at a rate of enters the inside of a countercurrent, double-pipe heat exchanger at 300.K and is heated by an oil stream that enters at at a rate of. The heat capacity of the oil is, and the average heat capacity of the water of the temperature range of interest is. The overall heattransfer coefficient of the exchanger is, and the area for heat transfer is. What is the total amount of heat transferred? You try
31 Lectures CM30 /30/05 Heat Exchanger Fouling material deposits on hot surfaces rust, impurities strong effect when boiling occurs clean scale adds an additional resistance to heat transfer fouled scale 6 Heat transfer resistances add effect of fouling U i oro U i oro resistance due to interface Ri or o Ro ln hi Ri k Ri hor o resistance due to limited thermal conductivity Ri or o Ro ln hi Ri hdiri k Ri hdoro hor o see Perry s Handbook, or Geankoplis 4 th ed. Table 4.9-, page 300 for values of h d 6 3
32 Lectures CM30 /30/05 Heat Exchanger Fouling fouled scale Geankoplis, 4 th edition, p Next: Heat transfer with phase change Evaporators Radiation DONE 64 3
Applied Heat Transfer:
Lectures 7+8 CM30 /6/06 CM30 Transport I Part II: Heat Transfer Applied Heat Transfer: Heat Exchanger Modeling, Sizing, and Design Professor Faith Morrison Department of Chemical Engineering Michigan Technological
More informationHow can we use Fundamental Heat Transfer to understand real devices like heat exchangers?
Lecture 7 03 CM30 /0/03 CM30 Transort I Part II: Heat Transfer Alied Heat Transfer: Heat Exchanger Modeling, Sizing, and Design Professor Faith Morrison Deartment of Chemical Engineering Michigan Technological
More informationIntroduction to Heat and Mass Transfer
Introduction to Heat and Mass Transfer Week 16 Merry X mas! Happy New Year 2019! Final Exam When? Thursday, January 10th What time? 3:10-5 pm Where? 91203 What? Lecture materials from Week 1 to 16 (before
More informationOverall Heat Transfer Coefficient
Overall Heat Transfer Coefficient A heat exchanger typically involves two flowing fluids separated by a solid wall. Heat is first transferred from the hot fluid to the wall by convection, through the wall
More informationc Dr. Md. Zahurul Haq (BUET) Heat Exchangers: Rating & Sizing - I ME 307 (2017) 2 / 32 T666
Heat Exchanger: Rating & Sizing Heat Exchangers: Rating & Sizing - I Dr. Md. Zahurul Haq Professor Department of Mechanical Engineering Bangladesh University of Engineering & Technology (BUET) Dhaka-000,
More informationT718. c Dr. Md. Zahurul Haq (BUET) HX: Energy Balance and LMTD ME 307 (2018) 2/ 21 T793
HX: Energy Balance and LMTD Dr. Md. Zahurul Haq Professor Department of Mechanical Engineering Bangladesh University of Engineering & Technology (BUET) Dhaka-000, Bangladesh http://zahurul.buet.ac.bd/
More informationChapter 11: Heat Exchangers. Dr Ali Jawarneh Department of Mechanical Engineering Hashemite University
Chapter 11: Heat Exchangers Dr Ali Jawarneh Department of Mechanical Engineering Hashemite University Objectives When you finish studying this chapter, you should be able to: Recognize numerous types of
More information1. Nusselt number and Biot number are computed in a similar manner (=hd/k). What are the differences between them? When and why are each of them used?
1. Nusselt number and Biot number are computed in a similar manner (=hd/k). What are the differences between them? When and why are each of them used?. During unsteady state heat transfer, can the temperature
More informationHeat Exchangers: Rating & Performance Parameters. Maximum Heat Transfer Rate, q max
Heat Exchangers: Rating & Performance Parameters Dr. Md. Zahurul Haq HTX Rating is concerned with the determination of the heat transfer rate, fluid outlet temperatures, and the pressure drop for an existing
More informationThermal Unit Operation (ChEg3113)
Thermal Unit Operation (ChEg3113) Lecture 3- Examples on problems having different heat transfer modes Instructor: Mr. Tedla Yeshitila (M.Sc.) Today Review Examples Multimode heat transfer Heat exchanger
More informationINSTRUCTOR: PM DR MAZLAN ABDUL WAHID
SMJ 4463: HEAT TRANSFER INSTRUCTOR: PM DR MAZLAN ABDUL WAHID http://www.fkm.utm.my/~mazlan TEXT: Introduction to Heat Transfer by Incropera, DeWitt, Bergman, Lavine 5 th Edition, John Wiley and Sons DR
More informationPROBLEM The heat rate, q, can be evaluated from an energy balance on the cold fluid, 225 kg/h J. 3600s/h
PROBLEM 11.41 KNOWN: Concentric tube heat exchanger. FIND: Length of the exchanger. SCHEMATIC: ASSUMPTIONS: (1) Negligible heat loss to surroundings, () Negligible kinetic and potential energy changes,
More informationINTRODUCTION: Shell and tube heat exchangers are one of the most common equipment found in all plants. How it works?
HEAT EXCHANGERS 1 INTRODUCTION: Shell and tube heat exchangers are one of the most common equipment found in all plants How it works? 2 WHAT ARE THEY USED FOR? Classification according to service. Heat
More informationDESIGN AND COST ANALYSIS OF HEAT TRANSFER EQUIPMENTS
DESIGN AND COST ANALYSIS OF HEAT TRANSFER EQUIPMENTS Md. Khairul Islam Lecturer Department of Applied Chemistry and Chemical Engineering. University of Rajshahi. What is design? Design includes all the
More informationطراحی مبدل های حرارتی مهدي کریمی ترم بهار HEAT TRANSFER CALCULATIONS
طراحی مبدل های حرارتی مهدي کریمی ترم بهار 96-97 HEAT TRANSFER CALCULATIONS ١ TEMPERATURE DIFFERENCE For any transfer the driving force is needed General heat transfer equation : Q = U.A. T What T should
More informationMultiple pass and cross flow heat exchangers
Multiple pass and cross flow heat exchangers Parag Chaware Department of Mechanical Engineering of Engineering, Pune Multiple pass and cross flow heat exchangers Parag Chaware 1 / 13 Introduction In order
More informationAnalyzing Mass and Heat Transfer Equipment
Analyzing Mass and Heat Transfer Equipment (MHE) Analyzing Mass and Heat Transfer Equipment Scaling up to solving problems using process equipment requires both continuum and macroscopic knowledge of transport,
More informationS.E. (Chemical) (Second Semester) EXAMINATION, 2011 HEAT TRANSFER (2008 PATTERN) Time : Three Hours Maximum Marks : 100
Total No. of Questions 12] [Total No. of Printed Pages 7 [4062]-186 S.E. (Chemical) (Second Semester) EXAMINATION, 2011 HEAT TRANSFER (2008 PATTERN) Time : Three Hours Maximum Marks : 100 N.B. : (i) Answers
More information23 1 TYPES OF HEAT EXCHANGERS
cen5426_ch23.qxd /26/04 9:42 AM Page 032 032 FUNDAMENTALS OF THERMAL-FLUID SCIENCES 23 TYPES OF HEAT EXCHANGERS Different heat transfer applications require different types of hardware different configurations
More informationPrinciples of Food and Bioprocess Engineering (FS 231) Problems on Heat Transfer
Principles of Food and Bioprocess Engineering (FS 1) Problems on Heat Transfer 1. What is the thermal conductivity of a material 8 cm thick if the temperature at one end of the product is 0 C and the temperature
More information8.1 Technically Feasible Design of a Heat Exchanger
328 Technically Feasible Design Case Studies T 2 q 2 ρ 2 C p2 T F q ρ C p T q ρ C p T 2F q 2 ρ 2 C p2 Figure 3.5. Countercurrent double-pipe exchanger. 8. Technically Feasible Design of a Heat Exchanger
More informationHEAT EXCHANGER. Objectives
HEAT EXCHANGER Heat exchange is an important unit operation that contributes to efficiency and safety of many processes. In this project you will evaluate performance of three different types of heat exchangers
More informationDesigning Steps for a Heat Exchanger ABSTRACT
Designing Steps for a Heat Exchanger Reetika Saxena M.Tech. Student in I.F.T.M. University, Moradabad Sanjay Yadav 2 Asst. Prof. in I.F.T.M. University, Moradabad ABSTRACT Distillation is a common method
More informationThermal Analysis of Shell and Tube Heat Ex-Changer Using C and Ansys
Thermal Analysis of Shell and Tube Heat Ex-Changer Using C and Ansys A v.hari Haran,*, B g.ravindra Reddy and C b.sreehari a) PG Student Mechanical Engineering Department Siddharth Institute Of Engineering
More informationHeat processes. Heat exchange
Heat processes Heat exchange Heat energy transported across a surface from higher temperature side to lower temperature side; it is a macroscopic measure of transported energies of molecular motions Temperature
More informationCircle one: School of Mechanical Engineering Purdue University ME315 Heat and Mass Transfer. Exam #2. April 3, 2014
Circle one: Div. 1 (12:30 pm, Prof. Choi) Div. 2 (9:30 am, Prof. Xu) School of Mechanical Engineering Purdue University ME315 Heat and Mass Transfer Exam #2 April 3, 2014 Instructions: Write your name
More informationHeat Transfer Performance in Double-Pass Flat-Plate Heat Exchangers with External Recycle
Journal of Applied Science and Engineering, Vol. 17, No. 3, pp. 293 304 (2014) DOI: 10.6180/jase.2014.17.3.10 Heat Transfer Performance in Double-Pass Flat-Plate Heat Exchangers with External Recycle Ho-Ming
More informationRadiation Heat Transfer
Heat Lectures 0- CM30 /5/06 CM30 ransport I Part II: Heat ransfer Radiation Heat ransfer In Unit Operations Heat Shields Professor Faith Morrison Department of Chemical Engineering Michigan echnological
More informationHeat Transfer with Phase Change
CM3110 Transport I Part II: Heat Transfer Heat Transfer with Phase Change Evaporators and Condensers Professor Faith Morrison Department of Chemical Engineering Michigan Technological University 1 Heat
More informationNumerical Analysis of Plate Heat Exchanger Performance in Co-Current Fluid Flow Configuration
Numerical Analysis of Plate Heat Exchanger Performance in Co-Current Fluid Flow Configuration H. Dardour, S. Mazouz, and A. Bellagi Abstract For many industrial applications plate heat exchangers are demonstrating
More informationMemorial University of Newfoundland Faculty of Engineering and Applied Science
Memorial University of Newfoundl Faculty of Engineering Applied Science ENGI-7903, Mechanical Equipment, Spring 20 Assignment 2 Vad Talimi Attempt all questions. The assignment may be done individually
More informationHeat and Mass Transfer Unit-1 Conduction
1. State Fourier s Law of conduction. Heat and Mass Transfer Unit-1 Conduction Part-A The rate of heat conduction is proportional to the area measured normal to the direction of heat flow and to the temperature
More informationSpecific heat capacity. Convective heat transfer coefficient. Thermal diffusivity. Lc ft, m Characteristic length (r for cylinder or sphere; for slab)
Important Heat Transfer Parameters CBE 150A Midterm #3 Review Sheet General Parameters: q or or Heat transfer rate Heat flux (per unit area) Cp Specific heat capacity k Thermal conductivity h Convective
More informationPLATE & FRAME HEAT EXCHANGER
PLATE & FRAME HEAT EXCHANGER By Farhan Ahmad Department of Chemical Engineering, University of Engineering & Technology Lahore Introduction The plate heat exchanger (PHE) was first introduced by Dr Richard
More informationCHAPTER FOUR HEAT TRANSFER
CHAPTER FOUR HEAT TRANSFER 4.1. Determination of Overall Heat Transfer Coefficient in a Tubular Heat Exchanger 4.2. Determination of Overall Heat Transfer Coefficient in a Plate Type Heat Exchanger 4.3.
More informationThe average velocity of water in the tube and the Reynolds number are Hot R-134a
hater 0:, 8, 4, 47, 50, 5, 55, 7, 75, 77, 8 and 85. 0- Refrigerant-4a is cooled by water a double-ie heat exchanger. he overall heat transfer coefficient is to be determed. Assumtions he thermal resistance
More informationS.E. (Chemical) (Second Semester) EXAMINATION, 2012 HEAT TRANSFER (2008 PATTERN) Time : Three Hours Maximum Marks : 100
Total No. of Questions 12] [Total No. of Printed Pages 7 Seat No. [4162]-187 S.E. (Chemical) (Second Semester) EXAMINATION, 2012 HEAT TRANSFER (2008 PATTERN) Time : Three Hours Maximum Marks : 100 N.B.
More informationChapter 3: Steady Heat Conduction
3-1 Steady Heat Conduction in Plane Walls 3-2 Thermal Resistance 3-3 Steady Heat Conduction in Cylinders 3-4 Steady Heat Conduction in Spherical Shell 3-5 Steady Heat Conduction with Energy Generation
More informationPROBLEM and from Eq. 3.28, The convection coefficients can be estimated from appropriate correlations. Continued...
PROBLEM 11. KNOWN: Type-30 stainless tube with prescribed inner and outer diameters used in a cross-flow heat exchanger. Prescribed fouling factors and internal water flow conditions. FIND: (a) Overall
More informationPrinciples of Food and Bioprocess Engineering (FS 231) Exam 2 Part A -- Closed Book (50 points)
Principles of Food and Bioprocess Engineering (FS 231) Exam 2 Part A -- Closed Book (50 points) 1. Are the following statements true or false? (20 points) a. Thermal conductivity of a substance is a measure
More informationGiven: Hot fluid oil, Cold fluid - water (T 1, T 2 ) (t 1, t 2 ) Water
. In a counter flow double pipe eat excanger, oil is cooled fro 85 to 55 by water entering at 5. Te ass flow rate of oil is 9,800 kg/ and specific eat f oil is 000 J/kg K. Te ass flow rate of water is
More informationPROBLEM 8.3 ( ) p = kg m 1m s m 1000 m = kg s m = bar < P = N m 0.25 m 4 1m s = 1418 N m s = 1.
PROBLEM 8.3 KNOWN: Temperature and velocity of water flow in a pipe of prescribed dimensions. FIND: Pressure drop and pump power requirement for (a) a smooth pipe, (b) a cast iron pipe with a clean surface,
More informationDesign and Temperature Analysis on Heat Exchanger with TEMA Standard Codes
Design and Temperature Analysis on Heat Exchanger with TEMA Standard Codes Adesh Dhope 1, Omkar Desai 2, Prof. V. Verma 3 1 Student, Department of Mechanical Engineering,Smt. KashibaiNavale college of
More informationDESIGN OF A SHELL AND TUBE HEAT EXCHANGER
DESIGN OF A SHELL AND TUBE HEAT EXCHANGER Swarnotpal Kashyap Department of Chemical Engineering, IIT Guwahati, Assam, India 781039 ABSTRACT Often, in process industries the feed stream has to be preheated
More informationHEAT TRANSFER. Mechanisms of Heat Transfer: (1) Conduction
HEAT TRANSFER Mechanisms of Heat Transfer: (1) Conduction where Q is the amount of heat, Btu, transferred in time t, h k is the thermal conductivity, Btu/[h ft 2 ( o F/ft)] A is the area of heat transfer
More informationUniversity of Rome Tor Vergata
University of Rome Tor Vergata Faculty of Engineering Department of Industrial Engineering THERMODYNAMIC AND HEAT TRANSFER HEAT TRANSFER dr. G. Bovesecchi gianluigi.bovesecchi@gmail.com 06-7259-727 (7249)
More informationHEAT TRANSFER 1 INTRODUCTION AND BASIC CONCEPTS 5 2 CONDUCTION
HEAT TRANSFER 1 INTRODUCTION AND BASIC CONCEPTS 5 2 CONDUCTION 11 Fourier s Law of Heat Conduction, General Conduction Equation Based on Cartesian Coordinates, Heat Transfer Through a Wall, Composite Wall
More informationExperimental Analysis of Double Pipe Heat Exchanger
206 IJEDR Volume 4, Issue 2 ISSN: 232-9939 Experimental Analysis of Double Pipe Heat Exchanger Urvin R. Patel, 2 Manish S. Maisuria, 3 Dhaval R. Patel, 4 Krunal P. Parmar,2,3,4 Assistant Professor,2,3,4
More informationExamination Heat Transfer
Examination Heat Transfer code: 4B680 date: June 13, 2008 time: 14.00-17.00 Note: There are 4 questions in total. The first one consists of independent subquestions. If possible and necessary, guide numbers
More informationHeat Transfer Predictions for Carbon Dioxide in Boiling Through Fundamental Modelling Implementing a Combination of Nusselt Number Correlations
Heat Transfer Predictions for Carbon Dioxide in Boiling Through Fundamental Modelling Implementing a Combination of Nusselt Number Correlations L. Makaum, P.v.Z. Venter and M. van Eldik Abstract Refrigerants
More information10 minutes reading time is allowed for this paper.
EGT1 ENGINEERING TRIPOS PART IB Tuesday 31 May 2016 2 to 4 Paper 4 THERMOFLUID MECHANICS Answer not more than four questions. Answer not more than two questions from each section. All questions carry the
More informationME 315 Exam 3 8:00-9:00 PM Thursday, April 16, 2009 CIRCLE YOUR DIVISION
ME 315 Exam 3 8:00-9:00 PM Thurday, Aril 16, 009 Thi i a cloed-book, cloed-note examination. There i a formula heet at the back. You mut turn off all communication device before tarting thi exam, and leave
More informationHEAT TRANSFER AND EXCHANGERS
HEAT TRANSFER AND EXCHANGERS Although heat-transfer rates can be computed with reasonable accuracy for clean or new pipe, the effect of dirty or corroded pipe surfaces cannot he satisfactorily estimated.
More informationSHELL-AND-TUBE TEST PROBLEMS
SHELL-AND-TUBE TEST PROBLEMS The problems that have been used to validate some of the capabilities in INSTED for the analysis of shell-and-tube heat exchanger are discussed in this chapter. You should
More informationHeat Exchanger Design
Heat Exchanger Design Heat Exchanger Design Methodology Design is an activity aimed at providing complete descriptions of an engineering system, part of a system, or just a single system component. These
More informationPFR with inter stage cooling: Example 8.6, with some modifications
PFR with inter stage cooling: Example 8.6, with some modifications Consider the following liquid phase elementary reaction: A B. It is an exothermic reaction with H = -2 kcal/mol. The feed is pure A, at
More informationESRL Module 8. Heat Transfer - Heat Recovery Steam Generator Numerical Analysis
ESRL Module 8. Heat Transfer - Heat Recovery Steam Generator Numerical Analysis Prepared by F. Carl Knopf, Chemical Engineering Department, Louisiana State University Documentation Module Use Expected
More informationME 331 Homework Assignment #6
ME 33 Homework Assignment #6 Problem Statement: ater at 30 o C flows through a long.85 cm diameter tube at a mass flow rate of 0.020 kg/s. Find: The mean velocity (u m ), maximum velocity (u MAX ), and
More informationCountercurrent heat exchanger
Countercurrent heat exchanger 1. Theoretical summary The basic operating principles and the simplified calculations regarding the counter current heat exchanger were discussed in the subject Chemical Unit
More informationSEM-2017(03HI MECHANICAL ENGINEERING. Paper II. Please read each of the following instructions carefully before attempting questions.
We RoU No. 700095 Candidate should write his/her Roll No. here. Total No. of Questions : 7 No. of Printed Pages : 7 SEM-2017(03HI MECHANICAL ENGINEERING Paper II Time ; 3 Hours ] [ Total Marks : 0 Instructions
More informationTOPIC 2 [A] STEADY STATE HEAT CONDUCTION
TOPIC 2 [A] STEADY STATE HEAT CONDUCTION CLASS TUTORIAL 1. The walls of a refrigerated truck consist of 1.2 mm thick steel sheet (k=18 W/m-K) at the outer surface, 22 mm thick cork (k=0.04 W/m-K) on the
More informationEffect of External Recycle on the Performance in Parallel-Flow Rectangular Heat-Exchangers
Tamkang Journal of Science and Engineering, Vol. 13, No. 4, pp. 405 412 (2010) 405 Effect of External Recycle on the Performance in Parallel-Flow Rectangular Heat-Exchangers Ho-Ming Yeh Energy and Opto-Electronic
More informationThermal Unit Operation (ChEg3113)
Thermal Unit Operation (ChEg3113) Lecture 6- Double Pipe Heat Exchanger Design Instructor: Mr. Tedla Yeshitila (M.Sc.) Today Review Double pipe heat exchanger design procedure Example Review Deign of heat
More informationLevel 7 Post Graduate Diploma in Engineering Heat and mass transfer
9210-221 Level 7 Post Graduate Diploma in Engineering Heat and mass transfer 0 You should have the following for this examination one answer book non programmable calculator pen, pencil, drawing instruments
More informationSHRI RAMSWAROOP MEMORIAL COLLEGE OF ENGG. & MANAGEMENT B.Tech. [SEM V (ME-51, 52, 53, 54)] QUIZ TEST-1 (Session: )
QUIZ TEST-1 Time: 1 Hour HEAT AND MASS TRANSFER Note: All questions are compulsory. Q1) The inside temperature of a furnace wall ( k=1.35w/m.k), 200mm thick, is 1400 0 C. The heat transfer coefficient
More informationDESIGN AND EXPERIMENTAL ANALYSIS OF SHELL AND TUBE HEAT EXCHANGER (U-TUBE)
DESIGN AND EXPERIMENTAL ANALYSIS OF SHELL AND TUBE HEAT EXCHANGER (U-TUBE) Divyesh B. Patel 1, Jayesh R. Parekh 2 Assistant professor, Mechanical Department, SNPIT&RC, Umrakh, Gujarat, India 1 Assistant
More informationSUMMER-18 EXAMINATION Model Answer. Subject: Heat Transfer Operation Subject code: Page 1 of 23
(ISO/IEC - 700-005 Certified) SUMMER-8 EXAMINATION Subject: Heat Transfer Operation Subject code: 7560 Page of 3 Important Instructions to examiners: ) The answers should be examined by key words and not
More informationTransfer processes: direct contact or indirect contact. Geometry of construction: tubes, plates, and extended surfaces
Chapter 5 Heat Exchangers 5.1 Introduction Heat exchangers are devices used to transfer heat between two or more fluid streams at different temperatures. Heat exchangers find widespread use in power generation,
More informationECH 4224L Unit Operations Lab I Thin Film Evaporator. Introduction. Objective
Introduction In this experiment, you will use thin-film evaporator (TFE) to separate a mixture of water and ethylene glycol (EG). In a TFE a mixture of two fluids runs down a heated inner wall of a cylindrical
More informationMaking Decisions with Insulation
More on Heat Transfer from Cheresources.com: FREE Resources Making Decisions with Insulation Article: Basics of Vaporization Questions and Answers: Heat Transfer Experienced-Based Rules for Heat Exchangers
More informationPROPOSED SOLUTION - ASSIGNMENT 4
Norwegian University of Science and Technology Course: Process Integration Department of Energy and Process Engineering Number: TEP 4215 Trondheim, 30.12.07, T. Gundersen Part: Heat Exchanger Networks
More informationBen Wolfe 11/3/14. Figure 1: Theoretical diagram showing the each step of heat loss.
Condenser Analysis Water Cooled Model: For this condenser design there will be a coil of stainless steel tubing suspended in a bath of cold water. The cold water will be stationary and begin at an ambient
More informationCHAPTER 5 MASS AND ENERGY ANALYSIS OF CONTROL VOLUMES
Thermodynamics: An Engineering Approach 8th Edition in SI Units Yunus A. Çengel, Michael A. Boles McGraw-Hill, 2015 CHAPTER 5 MASS AND ENERGY ANALYSIS OF CONTROL VOLUMES Lecture slides by Dr. Fawzi Elfghi
More informationLectures on Applied Reactor Technology and Nuclear Power Safety. Lecture No 6
Lectures on Nuclear Power Safety Lecture No 6 Title: Introduction to Thermal-Hydraulic Analysis of Nuclear Reactor Cores Department of Energy Technology KTH Spring 2005 Slide No 1 Outline of the Lecture
More informationEVAPORATION YUSRON SUGIARTO
EVAPORATION YUSRON SUGIARTO Evaporation: - Factors affecting evaporation - Evaporators - Film evaporators - Single effect and multiple effect evaporators - Mathematical problems on evaporation Principal
More informationAttempt ALL QUESTIONS IN SECTION A and ANY TWO QUESTIONS IN SECTION B Graph paper will be provided.
UNIVERSITY OF EAST ANGLIA School of Mathematics Main Series UG Examination 2017-2018 ENGINEERING PRINCIPLES AND LAWS ENG-4002Y Time allowed: 3 Hours Attempt ALL QUESTIONS IN SECTION A and ANY TWO QUESTIONS
More informationCoolant. Circuits Chip
1) A square isothermal chip is of width w=5 mm on a side and is mounted in a subtrate such that its side and back surfaces are well insulated, while the front surface is exposed to the flow of a coolant
More informationLecture 3: DESIGN CONSIDERATION OF DRIERS
Lecture 3: DESIGN CONSIDERATION OF DRIERS 8. DESIGN OF DRYER Design of a rotary dryer only on the basis of fundamental principle is very difficult. Few of correlations that are available for design may
More informationPhysics 2B Chapter 17 Notes - Conduction Spring 2018
Heat as a Fluid Scientists in the 1700 s had no idea what was going on. They were figuring things out for the first time and they didn t have much to work with because the scientific method was still relatively
More informationTwo mark questions and answers UNIT I BASIC CONCEPT AND FIRST LAW SVCET
Two mark questions and answers UNIT I BASIC CONCEPT AND FIRST LAW 1. What do you understand by pure substance? A pure substance is defined as one that is homogeneous and invariable in chemical composition
More informationHeat exchangers: Heat exchanger types:
Heat exhangers: he proess of heat exhange between two fluids that are at different temperatures and separated by a solid wall ours in many engineering appliations. he devie used to implement this exhange
More informationBME-A PREVIOUS YEAR QUESTIONS
BME-A PREVIOUS YEAR QUESTIONS CREDITS CHANGE ACCHA HAI TEAM UNIT-1 Introduction: Introduction to Thermodynamics, Concepts of systems, control volume, state, properties, equilibrium, quasi-static process,
More informationEstimating number of shells and determining the log mean temperature difference correction factor of shell and tube heat exchangers
Advanced Computational Methods in Heat Transfer IX 33 Estimating number of shells and determining the log mean temperature difference correction factor of shell and tube heat exchangers 3 4 S. K. Bhatti,
More informationProblem 1: Microscopic Momentum Balance
Problem 1: Microscopic Momentum Balance A rectangular block of wood of size 2λ (where 2λ < 1) is present in a rectangular channel of width 1 unit. The length of the block is denoted as L and the width
More informationTHE FIRST LAW APPLIED TO STEADY FLOW PROCESSES
Chapter 10 THE FIRST LAW APPLIED TO STEADY FLOW PROCESSES It is not the sun to overtake the moon, nor doth the night outstrip theday.theyfloateachinanorbit. The Holy Qur-ān In many engineering applications,
More informationIntroduction to Heat and Mass Transfer. Week 5
Introduction to Heat and Mass Transfer Week 5 Critical Resistance Thermal resistances due to conduction and convection in radial systems behave differently Depending on application, we want to either maximize
More informationEXPERIMENTAL AND THEORETICAL ANALYSIS OF TRIPLE CONCENTRIC TUBE HEAT EXCHANGER
EXPERIMENTAL AND THEORETICAL ANALYSIS OF TRIPLE CONCENTRIC TUBE HEAT EXCHANGER 1 Pravin M. Shinde, 2 Ganesh S. Yeole, 3 Abhijeet B. Mohite, 4 Bhagyashree H. Mahajan. 5 Prof. D. K. Sharma. 6 Prof. A. K.
More informationCooling of Electronics Lecture 2
Cooling of Electronics Lecture 2 Hans Jonsson Agenda Lecture 2 Introduction to Cooling of Electronics Cooling at different levels Cooling demand calculations Introduction to Cooling of Electronics Both
More informationMaking Decisions with Insulation
PDHonline Course K115 (3 PDH) Making Decisions with Insulation Instructor: Christopher Haslego, B.S. ChE 2012 PDH Online PDH Center 5272 Meadow Estates Drive Fairfax, VA 22030-6658 Phone & Fax: 703-988-0088
More informationFind: a) Mass of the air, in kg, b) final temperature of the air, in K, and c) amount of entropy produced, in kj/k.
PROBLEM 6.25 Three m 3 of air in a rigid, insulated container fitted with a paddle wheel is initially at 295 K, 200 kpa. The air receives 1546 kj of work from the paddle wheel. Assuming the ideal gas model,
More informationA First Course on Kinetics and Reaction Engineering Unit 30.Thermal Back-Mixing in a PFR
Unit 30.Thermal Back-Mixing in a PFR Overview One advantage offered by a CSTR when running an exothermic reaction is that the cool feed gets heated by mixing with the contents of the reactor. As a consequence
More informationPERFORMANCE ANALYSIS OF SHELL AND TUBE HEAT EXCHANGERS USING AN EDUCATIONAL APPLICATION
Fundamental J. Thermal Science and Engineering, Vol. 2, Issue 1, 2012, Pages 37-52 Published online at http://www.frdint.com/ PERFORMANCE ANALYSIS OF SHELL AND TUBE HEAT EXCHANGERS USING AN EDUCATIONAL
More informationIf there is convective heat transfer from outer surface to fluid maintained at T W.
Heat Transfer 1. What are the different modes of heat transfer? Explain with examples. 2. State Fourier s Law of heat conduction? Write some of their applications. 3. State the effect of variation of temperature
More informationRelationship to Thermodynamics. Chapter One Section 1.3
Relationship to Thermodynamics Chapter One Section 1.3 Alternative Formulations Alternative Formulations Time Basis: CONSERVATION OF ENERGY (FIRST LAW OF THERMODYNAMICS) An important tool in heat transfer
More informationCHAPTER 5 CONVECTIVE HEAT TRANSFER COEFFICIENT
62 CHAPTER 5 CONVECTIVE HEAT TRANSFER COEFFICIENT 5.1 INTRODUCTION The primary objective of this work is to investigate the convective heat transfer characteristics of silver/water nanofluid. In order
More informationOne-Dimensional, Steady-State. State Conduction without Thermal Energy Generation
One-Dimensional, Steady-State State Conduction without Thermal Energy Generation Methodology of a Conduction Analysis Specify appropriate form of the heat equation. Solve for the temperature distribution.
More informationThermodynamics 1. Lecture 7: Heat transfer Open systems. Bendiks Jan Boersma Thijs Vlugt Theo Woudstra. March 1, 2010.
hermodynamics Lecture 7: Heat transfer Open systems Bendiks Jan Boersma hijs Vlugt heo Woudstra March, 00 Energy echnology Summary lecture 6 Poisson relation efficiency of a two-stroke IC engine (Otto
More informationLecture 16 : Fully Developed Pipe flow with Constant Wall temperature and Heat Flux
Module 2 : Convection Lecture 16 : Fully Developed Pipe flow with Constant Wall temperature and Heat Flux Objectives In this class: The fully developed temperature profile for uniform circumferential heating
More informationDesign, Fabrication and Testing Of Helical Tube in Tube Coil Heat Exchanger
International Journal of Engineering and Technical Research (IJETR) ISSN: 2321-0869, Volume-2, Issue-12, December 2014 Design, Fabrication and Testing Of Helical Tube in Tube Coil Heat Exchanger Sagar
More informationMathematical Modelling for Refrigerant Flow in Diabatic Capillary Tube
Mathematical Modelling for Refrigerant Flow in Diabatic Capillary Tube Jayant Deshmukh Department of Mechanical Engineering Sagar Institute of Research and Technology, Bhopal, M.P., India D.K. Mudaiya
More information