CHAPTER 2 STEADY STATE HEAT CONDUCTION
|
|
- Julianna Gordon
- 7 years ago
- Views:
Transcription
1 CHAPTER 2 STEADY STATE HEAT CONDUCTION 1. A storage chamber of interior dimensions high has its inside maintained at a temperature of whilst the outside is at. The walls and ceiling of the chamber have three layers made of 60 mm thick board ( ) on the inside 90 mm thick insulation ( ) at the mid 240 mm thick concrete ( ) on the outside Neglecting flow of heat through the floor, determine the rate at which heat can flow towards inside of the chamber. (D.S. Kumar, Example 3.13) 2. A 8 mm thick metal plate, having thermal conductivity is exposed to vapor at 100 on one side and cooling water at 30 on another side. The heat transfer coefficients are on vapor side and on water side. Determine the rate of heat transfer and drop in temperature on each side of the plate. Assume area of the plate as unity. (Summer 2014) (Similar to D.S. Kumar, Example 3.40) 3. A composite wall has three layers of material held together by 3 cm diameter aluminium rivet per 0.1m2 of surface. The layer of material consists of 10 cm thick brick with hot surface at, 1cm thick wood with cold surface at. These two layers are interposed by third layer of insulating material 25cm thick. The conductivity of the material are: Assuming one dimensional heat flow, calculate the percentage change in heat transfer rate due to rivets. (Summer 2015) 4. A steel tube of 5 cm inner diameter and 8 cm outer diameter ( ), is covered with an insulation of 3 cm thickness ( ). A hot gas at, flows. Calculate the heat loss from the tube for 20 meter length. Also calculate the temperature at the interface of insulation and steel. Outside air Darshan Institute of Engineering and Technology, Rajkot 1
2 temperature is at,. (May-2012) (Similar to Mahesh Rathod, Example 3.29) 5. A steam pipe 8 cm in diameter is covered with 3 cm thick layer of insulation which has a surface emissivity of 0.9. The surface temperature of the insulation is and the pipe is placed in atmospheric air at. Considering heat loss by both radiation and natural convection calculate: (Dec-2011) I. The heat loss from the 7 m length of pipe. II. The overall heat transfer coefficient and the heat transfer coefficient due to radiation alone. The thermo physical properties of air at mean film temperature of 52 are as following: (where the notations have their usual meaning.) use empirical correlation for horizontal cylinders as ( ). 6. A refrigeration suction line having outer diameter 30 mm is required to be thermally insulated. The outside air convective heat transfer coefficient is. The thermal conductivity of the insulating material is. Determine: I. Whether the insulation will be effective II. Estimate the maximum value of thermal conductivity of insulating material to reduce heat transfer III. The thickness of cork insulation to reduce the heat transfer to 20% (k=0.04 W/m o C) (Summer 2013) Darshan Institute of Engineering and Technology, Rajkot 2
3 CHAPTER 3 FIN HEAT TRANSFER ( ) 1. Two long rods of the same diameter, one made of brass (k = 85 W/m-deg) and the other of copper (k = 375 W/m-deg), having one of their ends inserted into a furnace. At a section 10.5 cm away from the furnace, the temperature of the brass rod is 120. At what distance from the furnace end, the same temperature would be reached in the copper rod. Both rods are exposed to the same environment. (D.S. Kumar, Example 5.1) 2. A rod of 10 mm square section and 160 mm length with thermal conductivity of 50 W/m-deg protrudes from a furnace wall at 200, and is exposed to air at 30 Darshan Institute of Engineering and Technology, Rajkot 1 with convection coefficient 20 W/m 2 -deg. Make calculations for the heat convected upto 80 mm and 158 mm lengths and comment on the result. Adopt a long fin model for the arrangement. (D.S. Kumar, Example 5.4) 3. A rod of 10 mm diameter and 80 mm length with thermal conductivity 16 W/m-deg protrudes from a surface at 160. The rod is exposed to air at 30 with a convection coefficient of 25 W/m 2 -deg. How does the heat flow from this rod get affected if the same material volume is used for two fins of the same length? Assume short fin with end insulated. (D.S. Kumar, Example 5.11) 4. A 5 cm diameter rod, 90 cm long is having its lower face grinded smooth. The remainder of the rod is exposed to the 32 room air and a surface coefficient heat transfer equal to 6.5 W/m 2 -deg exists between the rod surface and the room air. The grinder dissipates mechanical energy at the rate of 35 W. If thermal conductivity of rod material is 41.5 W/m-deg, find the temperature of the rod at the point where the grinding is taking place. (D.S. Kumar, Example 5.21) 5. A thermometric pocket is a hollow brass tube (k = 75 W/m-deg) having outer and inner diameter of 15 mm of 10 mm respectively. The pocket extends to 5 cm depth from the wall of a 15 cm diameter pipe which carries hot air. The heat transfer coefficient between the pocket and air is prescribed by the relation: Nusselt number Nu = (Re) Make calculation for the error in temperature measurement. Presume the following data: (D.S. Kumar, Example 5.31)
4 Air temperature 160 and pipe wall temperature 40 HEAT TRANSFER ( ) Reynolds number and thermal conductivity of air W/m-deg Darshan Institute of Engineering and Technology, Rajkot 2
5 CHAPTER 4 TRNASIENT HEAT CONDUCTION 1. A potato with mean diameter of 4 cm is initially at. It is placed in boiling water for 5 minute and 30 seconds and found to be boiled perfectly. For how long should be a similar potato for the same consumer be boiled when taken from cold storage at. (Summer-2015) (Similar to D.S. Kumar, Example 6.7) Use lumped system analysis and take thermophysical properties of potato as 2. A solid sphere of 1 cm made up of steel is at initially at temperature. Properties of steel:, Density =, Sp. Heat = Calculate the time required for cooling it up to I. cooling medium is air at with in the following two cases II. cooling medium is water at with (Winter-2013) (Similar to D.S. Kumar, Example 6.7) Darshan Institute of Engineering and Technology, Rajkot 1
6
7 CHAPTER 5 & 6 RADIATION HEAT TRANSFER ( ) 1. Determine the view factor from any one side to any other side of the infinitely long triangular duct whose cross section is given in figure 1. (Cengel; Example 13.4) Figure 1 Infinitely long triangular duct 2. A furnace is shaped like a long equilateral triangular duct, as shown in Figure 2. The width of each side is 1 m. The base surface has an emissivity of 0.7 and is maintained at a uniform temperature of 600 K. The heated left-side surface closely approximates a blackbody at 1000 K. The right-side surface is well insulated. Determine the rate at which heat must be supplied to the heated side externally per unit length of the duct in order to maintain these operating conditions. (Cengel; Example 13.9) Figure 2 The triangular furnace 3. Determine the rate of heat loss by radiation from a steel tube of outside diameter 7 cm and length 3 m at a temperature of 227 brick conduit of 0.3 m side and at 27 if the tube is located within a square. Take emissivity of steel and brick as 0.79 and 0.93 respectively. (Summer 2014) )(Similar to D.S. Kumar; Example 8.30) 4. Two large parallel plates with emissivity (ε) = 0.5 each, are maintained at different temperatures and are exchanging heat only by radiation. Two equally large radiation Darshan Institute of Engineering and Technology, Rajkot 1
8 shields with surface emissivity 0.05 are introduced in parallel to the plates. Find percentage reduction in net radiative heat transfer. (May 2011) (Similar to D.S. Kumar; Example 8.38) 5. Calculate the net radiation heat transfer per m 2 area of two large plates placed parallel to each other at temperatures of and respectively. ( ) and ( ). If a polished aluminum shield is placed between them, find the % reduction in heat transfer, ( ). (Summer 2015) (Similar to D.S. Kumar; Example 8.38) Darshan Institute of Engineering and Technology, Rajkot 2
9 CHAPTER 7 CONVECTION HEAT TRANSFER ( ) 1. A hot square plate 40cm x 40cm at 100 C is exposed to atmospheric air at 20 C. Make calculations for the heat loss from both surfaces of the plate, if (a) plate is kept vertical (b) plate is kept horizontal. The following empirical correlations have been suggested: Nu = (Gr Pr) 0.33 for vertical position of plate, and Nu = 0.72 (Gr Pr) 0.25 for upper surface Nu = 0.35 (Gr Pr) 0.25 for lower surface [Ans: W] [D.S. Kumar 11.9, GTU - JAN 2013] 2. Calculate the rate of heat loss from a human body which may be considered as vertical cylinder 30 cm in diameter and 175 cm high in still air at 15 C.The skin temperature is 35 C and emissivity at the skin surface is 0.4. Neglect sweating and effect of clothing. Use Nu = 0.13 (Gr Pr) [Ans: W] [D.S. Kumar 11.15] 3. Estimate the heat transfer from a 40W incandescent bulb at 120 C to 20 C quiescent air. Approximate the bulb as a 50 mm dia. Sphere. What percentage of power is lost by free convection? The approximate co-relation is, ( ). [Ans: W; 19.62%] 4. A steam pipe 8 cm in diameter is covered with 3 cm thick layer of insulation which has a surface emissivity of 0.9.The surface temperature of the insulation is 80 C and the pipe is placed in atmospheric air at 24 C. Considering heat loss by both radiation and natural convection calculate: (1) The heat loss from the 7 m length of pipe. (2) The overall heat transfer coefficient & heat transfer co-efficient due to radiation alone. Use empirical correlation for horizontal cylinders as, ( ) [Ans: W; W/m 2 - C; W/m 2 - C][GTU DEC 2011] 5. Water at 10 C, flows over a flat plate (at 90 C) measuring 1 m X 1 m, with a velocity of 2 m/s. Determine, (a) The length of plate over which the flow is laminar (b) The rate of heat transfer up to the above length (c) The rate of heat transfer from the entire plate. Useful correlation: ( ) ( ) [ ( ) ]( ) [Ans: 0.139m; KW; 471KW][GTU MAY 2013] 6. Air at 20 C is flowing over a flat plate which is 200mm wide and 500mm long. The plate is maintained at 100 C. Find the heat loss from the plate if the air is flowing Darshan Institute of Engineering and Technology, Rajkot 1
10 parallel to 500mm side with 2m/s velocity. What will be the effect on heat transfer if the flow is parallel to 200mm side? For laminar flow over flat plate, use following correlation: ( ) ( ) [Ans: W, 85.6 W] [R. K. Rajput; 7.15] 7. Air at 20 C and at a pressure of 1 bar is flowing over a flat plate at a velocity of 3m/sec. If the plate is 280 mm wide and at 56 C, calculate the following quantities at x = 280 mm. a. Hydrodynamic boundary layer thickness b. Local and average friction coefficient c. Shearing stress due to friction d. Thickness of thermal boundary layer e. Local and average convective heat transfer coefficient f. Rate of heat transfer by convection g. Total drag force on the plate and h. Total mass flow rate through the boundary [Ans: Using Blasius Solution:-6.26mm; ; ; N/m 2 ; 6.88mm; 6.43W/m 2 K; 12.86W/m 2 K; 36.29W; N; kg/s] [4.6; P. K. NAG] 8. A plate of length 750mm has been placed longitudinally in a stream of crude oil which flows with a velocity of 5 m/sec. If the oil has a specific gravity of 0.8 and kinematic viscosity of 1 x 10-4 m 2 /sec, calculate, a. Boundary layer thickness at the middle of plate b. Shear stress at the middle of plate and c. Friction drag on one side of the plate. [Ans: m; N/m 2 ; N] 9. Air at 20 C and at atmospheric pressure flows at a velocity 4.5 m/s past a flat plate with a sharp leading edge. The entire plate surface is maintained at a temperature of 60 C. Assuming that the transition occurs at a critical Reynolds number of , find the distance from the leading edge at which the boundary layer changes from laminar to turbulent. At the location calculate: (1) thickness of hydrodynamic and thermal boundary layer, (2) Local and average heat transfer coefficients, (3) Heat transfer rate from both sides per unit width of plate. Use ( ) ( ) Assume cubic velocity profile and approximate method. [Ans: 12.34mm; 13.55mm; 3.05W/m 2 K; 6.1W/m 2 K; 917.4W] [GTU MAY 2012] [4.7; P. K. NAG] 10. The air at atmospheric pressure and temperature of 30 C flows over one side of plate of a velocity of 90 m/min. This plate is heated and maintained at 100 C over its entire length. Find out the following at 0.3 and 0.6 m from its leading edge. (1) Thickness of velocity boundary layer and thermal boundary layer. (2) Mass flow rate Darshan Institute of Engineering and Technology, Rajkot 2
11 which enters the boundary layer between 0.3 m and 0.6 m per metre depth of plate. Assume unit width of plate. [Ans: 8.30mm; 9.119mm; 11.73mm; 12.88mm; kg/s] [GTU MAY 2012] Use following properties of fluid at required temperature, Example Temp ρ Cp ν x 10 Fluid K µ Pr No. C kg/m 3 KJ/kg-deg m 2 /sec W/m-deg kg/m-hr 1 Air Air Air Air Water Air Air Air Air Darshan Institute of Engineering and Technology, Rajkot 3
12
13 CHAPTER 9 HEAT EXCHANGERS HEAT TRANSFER ( ) 1. Exhaust gases (Cp = 1.12 kj/kg-deg) flowing through a tubular heat exchanger at the rate of 1200 kg/hr are cooled from 400 C to 120 C. The cooling is affected by water (Cp = 4.18 kj/kg-deg) that enters the system at 10 C at the rate of 1500 kg/hr. If the overall heat transfer co-efficient is 500 kj/m 2 -hr-deg, what heat exchanger area is required to handle the load for (a) Parallel flow and (b) Counter flow arrangement? [Ans: m 2, m 2 ] [14.9, D. S. Kumar] 2. A counter flow concentric tube heat exchanger is used to cool the lubricating oil of a large industrial gas turbine engine. The oil flows through the tube at 0.19 kg/s (Cp = 2.18 kj/kg-k), and the coolant water flows in the annulus in the opposite direction at a rate of 0.15 kg/sec (Cp = 4.18 kj/kg-k). the oil enters the coolant at 425 K and leaves at 345 K while the coolant enters at 285 K. how long must the tube be made to perform this duty if the heat transfer co-efficient from oil to tube surface is 2250 W/m 2 K and from tube surface to water is 5650 W/m 2 K? The tube has a mean diameter of 12.5 mm and its wall presents negligible resistance to heat transfer. [Ans: 7.21 m] [14.17, D. S. Kumar] 3. A one-shell two-tube pass heat exchanger having 3000 thin wall brass tubes of 20 mm diameter has been installed in a steam power plant with a heat load of 2.3X10 8 W. the steam condenses at 50 C and the cooling water enters the tubes at 20 C at the rate of 3000 kg/s. Calculate the overall heat transfer co-efficient, the tube length per pass, and the rate of condensation of steam. Take the heat transfer co-efficient for condensation on the outer surfaces of the tubes as W/m 2 K and the latent heat of steam as 2380 kj/kg. further presume the following fluid properties: c = 4180 J/kg-K, μ = 855 X 10-6 Ns/m 2, k = W/m-k and Pr = 5.83 [Ans: 6524 W/m 2 K, 4.82 m, kg/s] [14.18, D. S. Kumar] 4. A heat exchanger is to be designed to condense 8 kg/s of an organic liquid (tsat = 80 C; hfg = 600 kj/kg) with cooling water available at 15 C and at a flow rate of 60 kg/s. The overall heat transfer co-efficient is 480 W/m 2 -deg. Calculate: Darshan Institute of Engineering and Technology, Rajkot 1
14 a. The number of tubes required. The tubes are to be of 25 mm outer diameter, 2 mm thickness and 4.85 m length. b. The number of tube passes. The velocity of the cooling water is not to exceed 2 m/s. [Ans: 478 tubes, 6 passes] [14.19, D. S. Kumar] 5. A surface condenser used in a steam power plant deals with kg of steam per hour at a pressure of 4.15 kn/m 2 and 0.9 dryness fraction. The cooling medium will be water that enters the condenser at 15 C and leaves at 25 C. From previous experience, a water velocity of 1.5 m/s is maintained through the tubes and the overall co-efficient of heat transfer is estimated at 3500 W/m 2 -K. Calculate : a. Mass flow rate of water, b. Surface area required for the given duty and c. Passes and number of tubes. The tubes used in condenser are 20 mm outside diameter, 1.5 mm thick and the space limitation restricts the condenser length to 4 meters. At the condensing pressure, steam has saturation temperature ts = 29.5 C and latent heat of vaporization hfg = 2435 kj/kg. Presume that the condensate coming out of the condenser is saturated water at the condenser pressure, i.e., there is no under cooling and the steam losses only latent part of its heat. [Ans: X 10 6 kg/hr, m 2, 1158 tubes, 2 passes] [14.22, D. S. Kumar] 6. Calculate the surface area required for a heat exchanger which is required to cool 3600 kg/hr of benzene (Cp = 1.74 kj/kg-k) from 75 C to 45 C. The cooling water (Cp = 4.18 kj/kg-deg) at 15 C has a flow rate of 2500 kg/hr. consider the following arrangements: a. Single pass counter flow b. 1-4 exchanger (one shell pass and four tube passes) c. Cross flow single pass with water mixed and benzene unmixed. The overall heat transfer co-efficient for each configuration is approximated to be 0.3kW/m 2 -K. [Ans: 4.87 m 2, 5.29 m 2, 5.18 m 2 ] [14.35, D. S. Kumar] Darshan Institute of Engineering and Technology, Rajkot 2
15 7. A counter flow heat exchanger is used to cool 2000 kg/hr of oil (cp = 2.5 kj/kg-k) from 105 C to 30 C by the use of water entering at 15 C. If the overall heat transfer co-efficient is expected to be 1.5 kw/m 2 K, make calculations for the water flow rate, the surface area required and the effectiveness of heat exchanger. Presume that the exit temperature of the water is not to be exceed 80 C. Use NTU-effectiveness approach. [Ans: kg/hr, 3.55 m 2, 0.833] [14.41, D. S. Kumar] 8. In a surface condenser, the water flowing through a series of tubes at the rate of 200 kg/hr is heated from 15 C to 75 C. The steam condenses on the outside surface of tubes at atmospheric pressure and the overall co-efficient of heat transfer is estimated at 860 kj/m 2 -hr-deg. Use NTU method to work out the length of tube and the steam condensation rate. Presume that the tube is 25 mm in diameter. At the condensing pressure, steam has saturation temperature ts = 100 C and the latent heat of vaporization hfg = 2160 kj/kg. Further, the steam is initially just saturated and the condensate leaves the exchanger without sub-cooling, i.e., only the latent heat of condensing steam is transferred to water. Take specific heat of water as 4 kj/kg-k. [Ans: 14.5 m, kg/hr] [14.45, D. S. Kumar] 9. A tube type heat exchanger is used to cool hot water from 80 C to 60 C. The task is accomplished by transferring heat to cold water that enters the heat exchanger at 20 C and leaves at 40 C. Should this heat exchanger operate under counter flow or parallel flow conditions? Also determine the exit temperatures if the flow rates of fluids are doubled. [Ans: C, C] [14.47, D. S. Kumar] Darshan Institute of Engineering and Technology, Rajkot 3
Natural Convection. Buoyancy force
Natural Convection In natural convection, the fluid motion occurs by natural means such as buoyancy. Since the fluid velocity associated with natural convection is relatively low, the heat transfer coefficient
More informationFREESTUDY HEAT TRANSFER TUTORIAL 3 ADVANCED STUDIES
FREESTUDY HEAT TRANSFER TUTORIAL ADVANCED STUDIES This is the third tutorial in the series on heat transfer and covers some of the advanced theory of convection. The tutorials are designed to bring the
More informationXI / PHYSICS FLUIDS IN MOTION 11/PA
Viscosity It is the property of a liquid due to which it flows in the form of layers and each layer opposes the motion of its adjacent layer. Cause of viscosity Consider two neighboring liquid layers A
More informationPractice Problems on Boundary Layers. Answer(s): D = 107 N D = 152 N. C. Wassgren, Purdue University Page 1 of 17 Last Updated: 2010 Nov 22
BL_01 A thin flat plate 55 by 110 cm is immersed in a 6 m/s stream of SAE 10 oil at 20 C. Compute the total skin friction drag if the stream is parallel to (a) the long side and (b) the short side. D =
More informationModule 1 : Conduction. Lecture 5 : 1D conduction example problems. 2D conduction
Module 1 : Conduction Lecture 5 : 1D conduction example problems. 2D conduction Objectives In this class: An example of optimization for insulation thickness is solved. The 1D conduction is considered
More informationExperimental Study of Free Convection Heat Transfer From Array Of Vertical Tubes At Different Inclinations
Experimental Study of Free Convection Heat Transfer From Array Of Vertical Tubes At Different Inclinations A.Satyanarayana.Reddy 1, Suresh Akella 2, AMK. Prasad 3 1 Associate professor, Mechanical Engineering
More informationEnergy Efficient Process Heating: Insulation and Thermal Mass
Energy Efficient Process Heating: Insulation and Thermal Mass Kevin Carpenter and Kelly Kissock Department of Mechanical and Aerospace Engineering University of Dayton 300 College Park Dayton, OH 45469-0210
More informationRusty Walker, Corporate Trainer Hill PHOENIX
Refrigeration 101 Rusty Walker, Corporate Trainer Hill PHOENIX Compressor Basic Refrigeration Cycle Evaporator Condenser / Receiver Expansion Device Vapor Compression Cycle Cooling by the removal of heat
More informationHeat Transfer Prof. Dr. Ale Kumar Ghosal Department of Chemical Engineering Indian Institute of Technology, Guwahati
Heat Transfer Prof. Dr. Ale Kumar Ghosal Department of Chemical Engineering Indian Institute of Technology, Guwahati Module No. # 04 Convective Heat Transfer Lecture No. # 03 Heat Transfer Correlation
More informationHeat Transfer Enhancement in a Heat Exchanger using Punched and V-cut Twisted Tape Inserts
Heat Transfer Enhancement in a Heat Exchanger using Punched and V-cut Twisted Tape Inserts Imran Quazi#1, Prof. V.R.Mohite#2 #1DPCOE-Mechanical Department, SPP University Pune, India imranqu azi198 7@gmail.com
More informationThe soot and scale problems
Dr. Albrecht Kaupp Page 1 The soot and scale problems Issue Soot and scale do not only increase energy consumption but are as well a major cause of tube failure. Learning Objectives Understanding the implications
More informationHeat Exchangers. Heat Exchanger Types. Heat Exchanger Types. Applied Heat Transfer Part Two. Topics of This chapter
Applied Heat Transfer Part Two Heat Excangers Dr. Amad RAMAZANI S.A. Associate Professor Sarif University of Tecnology انتقال حرارت کاربردی احمد رمضانی سعادت ا بادی Autumn, 1385 (2006) Ramazani, Heat Excangers
More informationHEAT TRANSFER IM0245 3 LECTURE HOURS PER WEEK THERMODYNAMICS - IM0237 2014_1
COURSE CODE INTENSITY PRE-REQUISITE CO-REQUISITE CREDITS ACTUALIZATION DATE HEAT TRANSFER IM05 LECTURE HOURS PER WEEK 8 HOURS CLASSROOM ON 6 WEEKS, HOURS LABORATORY, HOURS OF INDEPENDENT WORK THERMODYNAMICS
More informationFundamentals of THERMAL-FLUID SCIENCES
Fundamentals of THERMAL-FLUID SCIENCES THIRD EDITION YUNUS A. CENGEL ROBERT H. TURNER Department of Mechanical JOHN M. CIMBALA Me Graw Hill Higher Education Boston Burr Ridge, IL Dubuque, IA Madison, Wl
More informationCorrelations for Convective Heat Transfer
In many cases it's convenient to have simple equations for estimation of heat transfer coefficients. Below is a collection of recommended correlations for single-phase convective flow in different geometries
More informationBasic Equations, Boundary Conditions and Dimensionless Parameters
Chapter 2 Basic Equations, Boundary Conditions and Dimensionless Parameters In the foregoing chapter, many basic concepts related to the present investigation and the associated literature survey were
More informationAN EXPERIMENTAL STUDY OF EXERGY IN A CORRUGATED PLATE HEAT EXCHANGER
International Journal of Mechanical Engineering and Technology (IJMET) Volume 6, Issue 11, Nov 2015, pp. 16-22, Article ID: IJMET_06_11_002 Available online at http://www.iaeme.com/ijmet/issues.asp?jtype=ijmet&vtype=6&itype=11
More informationCE 6303 MECHANICS OF FLUIDS L T P C QUESTION BANK PART - A
CE 6303 MECHANICS OF FLUIDS L T P C QUESTION BANK 3 0 0 3 UNIT I FLUID PROPERTIES AND FLUID STATICS PART - A 1. Define fluid and fluid mechanics. 2. Define real and ideal fluids. 3. Define mass density
More informationEXPERIMENTAL ANALYSIS OF HEAT TRANSFER ENHANCEMENT IN A CIRCULAR TUBE WITH DIFFERENT TWIST RATIO OF TWISTED TAPE INSERTS
INTERNATIONAL JOURNAL OF HEAT AND TECHNOLOGY Vol.33 (2015), No.3, pp.158-162 http://dx.doi.org/10.18280/ijht.330324 EXPERIMENTAL ANALYSIS OF HEAT TRANSFER ENHANCEMENT IN A CIRCULAR TUBE WITH DIFFERENT
More informationFluids and Solids: Fundamentals
Fluids and Solids: Fundamentals We normally recognize three states of matter: solid; liquid and gas. However, liquid and gas are both fluids: in contrast to solids they lack the ability to resist deformation.
More informationHeat Transfer From A Heated Vertical Plate
Heat Transfer From A Heated Vertical Plate Mechanical and Environmental Engineering Laboratory Department of Mechanical and Aerospace Engineering University of California at San Diego La Jolla, California
More informationCorrugated Tubular Heat Exchangers
Corrugated Tubular Heat Exchangers HEAT EXCHANGERS for the 21st CENTURY Corrugated Tubular Heat Exchangers (CTHE) Corrugated Tube Heat Exchangers are shell and tube heat exchangers which use corrugated
More informationHEAT TRANSFER ANALYSIS IN A 3D SQUARE CHANNEL LAMINAR FLOW WITH USING BAFFLES 1 Vikram Bishnoi
HEAT TRANSFER ANALYSIS IN A 3D SQUARE CHANNEL LAMINAR FLOW WITH USING BAFFLES 1 Vikram Bishnoi 2 Rajesh Dudi 1 Scholar and 2 Assistant Professor,Department of Mechanical Engineering, OITM, Hisar (Haryana)
More informationHeat Exchangers - Introduction
Heat Exchangers - Introduction Concentric Pipe Heat Exchange T h1 T c1 T c2 T h1 Energy Balance on Cold Stream (differential) dq C = wc p C dt C = C C dt C Energy Balance on Hot Stream (differential) dq
More informationSteady Heat Conduction
Steady Heat Conduction In thermodynamics, we considered the amount of heat transfer as a system undergoes a process from one equilibrium state to another. hermodynamics gives no indication of how long
More informationNumerical Investigation of Heat Transfer Characteristics in A Square Duct with Internal RIBS
merical Investigation of Heat Transfer Characteristics in A Square Duct with Internal RIBS Abhilash Kumar 1, R. SaravanaSathiyaPrabhahar 2 Mepco Schlenk Engineering College, Sivakasi, Tamilnadu India 1,
More informationSizing of triple concentric pipe heat exchanger
Sizing of triple concentric pipe heat exchanger 1 Tejas M. Ghiwala, 2 Dr. V.K. Matawala 1 Post Graduate Student, 2 Head of Department 1 Thermal Engineering, SVMIT, Bharuch-392001, Gujarat, INDIA, 2 Department
More informationTHE PSEUDO SINGLE ROW RADIATOR DESIGN
International Journal of Mechanical Engineering and Technology (IJMET) Volume 7, Issue 1, Jan-Feb 2016, pp. 146-153, Article ID: IJMET_07_01_015 Available online at http://www.iaeme.com/ijmet/issues.asp?jtype=ijmet&vtype=7&itype=1
More informationHeat exchangers are devices that facilitate the exchange of heat between
cen5426_ch23.qxd /26/04 9:42 AM Page 03 HEAT EXCHANGERS CHAPTER 23 Heat exchangers are devices that facilitate the exchange of heat between two fluids that are at different temperatures while keeping them
More informationExperimental Study On Heat Transfer Enhancement In A Circular Tube Fitted With U -Cut And V -Cut Twisted Tape Insert
Experimental Study On Heat Transfer Enhancement In A Circular Tube Fitted With U -Cut And V -Cut Twisted Tape Insert Premkumar M Abstract Experimental investigation of heat transfer and Reynolds number
More informationIntegration of a fin experiment into the undergraduate heat transfer laboratory
Integration of a fin experiment into the undergraduate heat transfer laboratory H. I. Abu-Mulaweh Mechanical Engineering Department, Purdue University at Fort Wayne, Fort Wayne, IN 46805, USA E-mail: mulaweh@engr.ipfw.edu
More informationNatural convection in a room with two opposite heated vertical walls
INTERNATIONAL JOURNAL OF ENERGY AND ENVIRONMENT Volume 6, Issue 1, 2015 pp.81-86 Journal homepage: www.ijee.ieefoundation.org Natural convection in a room with two opposite heated vertical walls Ameer
More informationSheet 5:Chapter 5 5 1C Name four physical quantities that are conserved and two quantities that are not conserved during a process.
Thermo 1 (MEP 261) Thermodynamics An Engineering Approach Yunus A. Cengel & Michael A. Boles 7 th Edition, McGraw-Hill Companies, ISBN-978-0-07-352932-5, 2008 Sheet 5:Chapter 5 5 1C Name four physical
More informationWaste Heat Recovery through Air Conditioning System
International Journal of Engineering Research and Development e-issn: 2278-067X, p-issn : 2278-800X, www.ijerd.com Volume 5, Issue 3 (December 2012), PP. 87-92 Waste Heat Recovery through Air Conditioning
More informationTheoretical and Numerical Analysis of Heat Transfer in Pipeline System
APCOM & ISCM -4 th December, 20, Singapore Theoretical and Numerical Analysis of Heat Transfer in Pipeline System Xiaowei Zhu, Hui Tang, *Hua Li, Jiahua Hong, Songyuan Yang School of Mechanical & Aerospace
More informationIterative calculation of the heat transfer coefficient
Iterative calculation of the heat transfer coefficient D.Roncati Progettazione Ottica Roncati, via Panfilio, 17 44121 Ferrara Aim The plate temperature of a cooling heat sink is an important parameter
More informationInvestigation on Enhancement of Heat Transfer Using Different Type of Nanofluids Review
Review Paper Investigation on Enhancement of Heat Transfer Using Different Type of Nanofluids Review Authors 1 Ramesh Bhoi *, 2 Dinesh Dabhi, 3 Chetan Jaiswal Address for Correspondence: 1, 2 Mechanical
More informationEVERYDAY ENGINEERING EXAMPLES FOR SIMPLE CONCEPTS
EVERYDAY ENGINEERING EXAMPLES FOR SIMPLE CONCEPTS Thermal Properties ENGR 3350 - Materials Science Dr. Nedim Vardar Copyright 2015 Thermal Properties of Materials Engage: MSEIP Engineering Everyday Engineering
More informationInternational Journal of Latest Research in Science and Technology Volume 4, Issue 2: Page No.161-166, March-April 2015
International Journal of Latest Research in Science and Technology Volume 4, Issue 2: Page No.161-166, March-April 2015 http://www.mnkjournals.com/ijlrst.htm ISSN (Online):2278-5299 EXPERIMENTAL STUDY
More informationEngine Heat Transfer. Engine Heat Transfer
Engine Heat Transfer 1. Impact of heat transfer on engine operation 2. Heat transfer environment 3. Energy flow in an engine 4. Engine heat transfer Fundamentals Spark-ignition engine heat transfer Diesel
More informationKeywords: Heat transfer enhancement; staggered arrangement; Triangular Prism, Reynolds Number. 1. Introduction
Heat transfer augmentation in rectangular channel using four triangular prisms arrange in staggered manner Manoj Kumar 1, Sunil Dhingra 2, Gurjeet Singh 3 1 Student, 2,3 Assistant Professor 1.2 Department
More informationVapor Chambers. Figure 1: Example of vapor chamber. Benefits of Using Vapor Chambers
Vapor Chambers A vapor chamber is a high-end thermal management device that can evenly dissipate heat from a small source to a large platform of area (see Figure 1). It has a similar construction and mechanism
More informationDepartment of Chemical Engineering, National Institute of Technology, Tiruchirappalli 620 015, Tamil Nadu, India
Experimental Thermal and Fluid Science 32 (2007) 92 97 www.elsevier.com/locate/etfs Studies on heat transfer and friction factor characteristics of laminar flow through a circular tube fitted with right
More informationInternational Journal of ChemTech Research CODEN (USA): IJCRGG ISSN: 0974-4290 Vol.7, No.6, pp 2580-2587, 2014-2015
International Journal of ChemTech Research CODEN (USA): IJCRGG ISSN: 0974-4290 Vol.7, No.6, pp 2580-2587, 2014-2015 Performance Analysis of Heat Transfer and Effectiveness on Laminar Flow with Effect of
More informationp atmospheric Statics : Pressure Hydrostatic Pressure: linear change in pressure with depth Measure depth, h, from free surface Pressure Head p gh
IVE1400: n Introduction to Fluid Mechanics Statics : Pressure : Statics r P Sleigh: P..Sleigh@leeds.ac.uk r J Noakes:.J.Noakes@leeds.ac.uk January 008 Module web site: www.efm.leeds.ac.uk/ive/fluidslevel1
More information1. A belt pulley is 3 ft. in diameter and rotates at 250 rpm. The belt which is 5 ins. wide makes an angle of contact of 190 over the pulley.
Sample Questions REVISED FIRST CLASS PARTS A1, A2, AND A3 (NOTE: these questions are intended as representations of the style of questions that may appear on examinations. They are not intended as study
More informationHDA -----------------------------------------------------------
----------------------------------------------------------- Lightstrips ---------------------------------------------------------------------- Ceiling system for heating and cooling LIGHTSTRIPS LIGHTSTRIPS
More informationUnit 6: EXTRUSION. Difficult to form metals like stainless steels, nickel based alloys and high temperature metals can also be extruded.
1 Unit 6: EXTRUSION Introduction: Extrusion is a metal working process in which cross section of metal is reduced by forcing the metal through a die orifice under high pressure. It is used to produce cylindrical
More informationTheoretical and Experimental Investigation of Heat Transfer Characteristics through a Rectangular Microchannel Heat Sink
Theoretical and Experimental Investigation of Heat Transfer Characteristics through a Rectangular Microchannel Heat Sink Dr. B. S. Gawali 1, V. B. Swami 2, S. D. Thakre 3 Professor Dr., Department of Mechanical
More informationFired Heater Design and Simulation
Fired Heater Design and Simulation Mahesh N. Jethva 1, C. G. Bhagchandani 2 1 M.E. Chemical Engineering Department, L.D. College of Engineering, Ahmedabad-380 015 2 Associate Professor, Chemical Engineering
More informationTHERMAL ANALYSIS. Overview
W H I T E P A P E R THERMAL ANALYSIS Overview In this white paper we define and then outline the concept of thermal analysis as it relates to product design. We discuss the principles of conduction, convection,
More informationThermal insulation. Don t be afraid of low temperatures. www.kit.edu. Institute for Technical Physics Holger Neumann
Thermal insulation Institute for Technical Physics Holger Neumann Don t be afraid of low temperatures www.kit.edu Content Relevance of thermal insulation in cryogenics Overview of different insulation
More informationCHAPTER 29 VOLUMES AND SURFACE AREAS OF COMMON SOLIDS
CHAPTER 9 VOLUMES AND SURFACE AREAS OF COMMON EXERCISE 14 Page 9 SOLIDS 1. Change a volume of 1 00 000 cm to cubic metres. 1m = 10 cm or 1cm = 10 6m 6 Hence, 1 00 000 cm = 1 00 000 10 6m = 1. m. Change
More informationDifferential Relations for Fluid Flow. Acceleration field of a fluid. The differential equation of mass conservation
Differential Relations for Fluid Flow In this approach, we apply our four basic conservation laws to an infinitesimally small control volume. The differential approach provides point by point details of
More informationSolid shape molding is not desired in injection molding due to following reasons.
PLASTICS PART DESIGN and MOULDABILITY Injection molding is popular manufacturing method because of its high-speed production capability. Performance of plastics part is limited by its properties which
More informationHEAT AND MASS TRANSFER
MEL242 HEAT AND MASS TRANSFER Prabal Talukdar Associate Professor Department of Mechanical Engineering g IIT Delhi prabal@mech.iitd.ac.in MECH/IITD Course Coordinator: Dr. Prabal Talukdar Room No: III,
More informationBB-18 Black Body High Vacuum System Technical Description
BB-18 Black Body High Vacuum System Technical Description The BB-18 Black Body is versatile and is programmed for use as a fixed cold target at 80 K or variable target, at 80 K- 350 K no extra cost. The
More informationChapter 4: Transfer of Thermal Energy
Chapter 4: Transfer of Thermal Energy Goals of Period 4 Section 4.1: To define temperature and thermal energy Section 4.2: To discuss three methods of thermal energy transfer. Section 4.3: To describe
More informationAPPLIED THERMODYNAMICS TUTORIAL 1 REVISION OF ISENTROPIC EFFICIENCY ADVANCED STEAM CYCLES
APPLIED THERMODYNAMICS TUTORIAL 1 REVISION OF ISENTROPIC EFFICIENCY ADVANCED STEAM CYCLES INTRODUCTION This tutorial is designed for students wishing to extend their knowledge of thermodynamics to a more
More informationThe Three Heat Transfer Modes in Reflow Soldering
Section 5: Reflow Oven Heat Transfer The Three Heat Transfer Modes in Reflow Soldering There are three different heating modes involved with most SMT reflow processes: conduction, convection, and infrared
More informationFluid Mechanics: Static s Kinematics Dynamics Fluid
Fluid Mechanics: Fluid mechanics may be defined as that branch of engineering science that deals with the behavior of fluid under the condition of rest and motion Fluid mechanics may be divided into three
More informationA LAMINAR FLOW ELEMENT WITH A LINEAR PRESSURE DROP VERSUS VOLUMETRIC FLOW. 1998 ASME Fluids Engineering Division Summer Meeting
TELEDYNE HASTINGS TECHNICAL PAPERS INSTRUMENTS A LAMINAR FLOW ELEMENT WITH A LINEAR PRESSURE DROP VERSUS VOLUMETRIC FLOW Proceedings of FEDSM 98: June -5, 998, Washington, DC FEDSM98 49 ABSTRACT The pressure
More informationHeat Transfer Prof. Dr. Aloke Kumar Ghosal Department of Chemical Engineering Indian Institute of Technology, Guwahati
Heat Transfer Prof. Dr. Aloke Kumar Ghosal Department of Chemical Engineering Indian Institute of Technology, Guwahati Module No. # 02 One Dimensional Steady State Heat Transfer Lecture No. # 05 Extended
More informationThe Viscosity of Fluids
Experiment #11 The Viscosity of Fluids References: 1. Your first year physics textbook. 2. D. Tabor, Gases, Liquids and Solids: and Other States of Matter (Cambridge Press, 1991). 3. J.R. Van Wazer et
More informationDesign of heat exchangers
Design of heat exchangers Exchanger Design Methodology The problem of heat exchanger design is complex and multidisciplinary. The major design considerations for a new heat exchanger include: process/design
More informationComparison of Heat Transfer between a Helical and Straight Tube Heat Exchanger
International Journal of Engineering Research and Technology. ISSN 0974-3154 Volume 6, Number 1 (2013), pp. 33-40 International Research Publication House http://www.irphouse.com Comparison of Heat Transfer
More informationcmn_lecture.2 CAD OF DOUBLE PIPE HEAT EXCHANGERS
cmn_lecture.2 CAD OF DOUBLE PIPE HEAT EXCHANGERS A double pipe heat exchanger, in essence, consists of two concentric pipes, one fluid flowing through the inner pipe and the outer fluid flowing countercurrently
More informationThe Viscosity of Fluids
Experiment #11 The Viscosity of Fluids References: 1. Your first year physics textbook. 2. D. Tabor, Gases, Liquids and Solids: and Other States of Matter (Cambridge Press, 1991). 3. J.R. Van Wazer et
More informationFree Convection Film Flows and Heat Transfer
Deyi Shang Free Convection Film Flows and Heat Transfer With 109 Figures and 69 Tables < J Springer Contents 1 Introduction 1 1.1 Scope 1 1.2 Application Backgrounds 1 1.3 Previous Developments 2 1.3.1
More informationChapter 18 Temperature, Heat, and the First Law of Thermodynamics. Problems: 8, 11, 13, 17, 21, 27, 29, 37, 39, 41, 47, 51, 57
Chapter 18 Temperature, Heat, and the First Law of Thermodynamics Problems: 8, 11, 13, 17, 21, 27, 29, 37, 39, 41, 47, 51, 57 Thermodynamics study and application of thermal energy temperature quantity
More informationHEAT TRANSFER ENHANCEMENT AND FRICTION FACTOR ANALYSIS IN TUBE USING CONICAL SPRING INSERT
HEAT TRANSFER ENHANCEMENT AND FRICTION FACTOR ANALYSIS IN TUBE USING CONICAL SPRING INSERT Rahul M. Gupta 1, Bhushan C. Bissa 2 1 Research Scholar, Department of Mechanical Engineering, Shri Ramdeobaba
More informationCE 204 FLUID MECHANICS
CE 204 FLUID MECHANICS Onur AKAY Assistant Professor Okan University Department of Civil Engineering Akfırat Campus 34959 Tuzla-Istanbul/TURKEY Phone: +90-216-677-1630 ext.1974 Fax: +90-216-677-1486 E-mail:
More informationANSI/ASHRAE Standard 140-2004 Building Thermal Envelope and Fabric Load Tests
ANSI/ASHRAE Standard 140-2004 Building Thermal Envelope and Fabric Load Tests DesignBuilder Version 1.2.0 (incorporating EnergyPlus version 1.3.0) - June 2006 1.0 Purpose The ANSI/ASHRAE Standard 140-2004
More informationSaeid Rahimi. Effect of Different Parameters on Depressuring Calculation Results. 01-Nov-2010. Introduction. Depressuring parameters
Effect of Different Parameters on Depressuring Calculation Results Introduction Saeid Rahimi 01-Nov-2010 Emergency depressuring facilities are utilized to accomplish at least one of the following objectives:
More informationFLUID DYNAMICS. Intrinsic properties of fluids. Fluids behavior under various conditions
FLUID DYNAMICS Intrinsic properties of fluids Fluids behavior under various conditions Methods by which we can manipulate and utilize the fluids to produce desired results TYPES OF FLUID FLOW Laminar or
More informationLearning Module 4 - Thermal Fluid Analysis Note: LM4 is still in progress. This version contains only 3 tutorials.
Learning Module 4 - Thermal Fluid Analysis Note: LM4 is still in progress. This version contains only 3 tutorials. Attachment C1. SolidWorks-Specific FEM Tutorial 1... 2 Attachment C2. SolidWorks-Specific
More informationCFD Analysis of Application of Phase Change Material in Automotive Climate Control Systems
CFD Analysis of Application of Phase Change Material in Automotive Climate Control Systems Vijayakumar Nachimuthu 1, Prabhu Mani 2, Muthukumar. P 3 1 Flowxplore, Coimbatore, India., 2 Kathir College of
More information1. Fluids Mechanics and Fluid Properties. 1.1 Objectives of this section. 1.2 Fluids
1. Fluids Mechanics and Fluid Properties What is fluid mechanics? As its name suggests it is the branch of applied mechanics concerned with the statics and dynamics of fluids - both liquids and gases.
More informationLESSON 1. HEAT EXCHANGERS
LESSON 1. HEAT EXCHANGERS 1 Contents (I) Definition. Classification. Regenerators. Mixers or direct contact heat exchangers. Packed bed heat exchangers (Intercambiadores de lecho compacto). Direct flame
More informationCASL-U-2013-0193-000
L3:THM.CFD.P7.06 Implementation and validation of the new RPI boiling models using STAR-CCM+ as CFD Platform Victor Petrov, Annalisa Manera UMICH September 30, 2013 EXECUTIVE SUMMARY This milestone is
More informationTHERMAL ANALYSIS OF HEAT EXCHANGER WITH THE HELP OF TAGUCHI METHOD
International Journal of Advanced Research in Engineering and Technology (IJARET) Volume 7, Issue 1, Jan-Feb 2016, pp. 01-06, Article ID: IJARET_07_01_001 Available online at http://www.iaeme.com/ijaret/issues.asp?jtype=ijaret&vtype=7&itype=1
More informationTARIFF CODE and updates standard
TARIFF CODE and updates standard No HS CODE AHTN CODE PRODUCT DESCRIPTION PRODUCT TYPE STANDARDS IDENTIFIED 7207 Semi finished products of iron or non alloy steel Containing by weight less than 0.25% of
More informationUNIT 2 REFRIGERATION CYCLE
UNIT 2 REFRIGERATION CYCLE Refrigeration Cycle Structure 2. Introduction Objectives 2.2 Vapour Compression Cycle 2.2. Simple Vapour Compression Refrigeration Cycle 2.2.2 Theoretical Vapour Compression
More informationCBE 6333, R. Levicky 1 Review of Fluid Mechanics Terminology
CBE 6333, R. Levicky 1 Review of Fluid Mechanics Terminology The Continuum Hypothesis: We will regard macroscopic behavior of fluids as if the fluids are perfectly continuous in structure. In reality,
More informationThis will also provide you with the knowledge to insure long life for your Investment
CONDUIT PIPE DRYING This Presentation will guide you to why systems fail! This will also provide you with the knowledge to insure long life for your Investment Drainable and Dryable System Design Trough
More informationHeat Pipe Selection Revision 12/04/2001
Heat Pipe Selection Revision 12/04/2001 Heat pipes are being used very often in particular applications when conventional cooling methods are not suitable. Once the need for heat pipe arises, the most
More informationMEASUREMENT OF VISCOSITY OF LIQUIDS BY THE STOKE S METHOD
130 Experiment-366 F MEASUREMENT OF VISCOSITY OF LIQUIDS BY THE STOKE S METHOD Jeethendra Kumar P K, Ajeya PadmaJeeth and Santhosh K KamalJeeth Instrumentation & Service Unit, No-610, Tata Nagar, Bengaluru-560092.
More informationHEAT TRANSFER AUGMENTATION THROUGH DIFFERENT PASSIVE INTENSIFIER METHODS
HEAT TRANSFER AUGMENTATION THROUGH DIFFERENT PASSIVE INTENSIFIER METHODS P.R.Hatwar 1, Bhojraj N. Kale 2 1, 2 Department of Mechanical Engineering Dr. Babasaheb Ambedkar College of Engineering & Research,
More informationExperiment (13): Flow channel
Introduction: An open channel is a duct in which the liquid flows with a free surface exposed to atmospheric pressure. Along the length of the duct, the pressure at the surface is therefore constant and
More informationBattery Thermal Management System Design Modeling
Battery Thermal Management System Design Modeling Gi-Heon Kim, Ph.D Ahmad Pesaran, Ph.D (ahmad_pesaran@nrel.gov) National Renewable Energy Laboratory, Golden, Colorado, U.S.A. EVS October -8, 8, 006 Yokohama,
More informationHow To Understand Evaporator
SECTION 5 COMMERCIAL REFRIGERATION UNIT 21 EVAPORATORS AND THE REFRIGERATION SYSTEM UNIT OBJECTIVES After studying this unit, the reader should be able to Define high-, medium-, and low-temperature refrigeration.
More information4.What is the appropriate dimensionless parameter to use in comparing flow types? YOUR ANSWER: The Reynolds Number, Re.
CHAPTER 08 1. What is most likely to be the main driving force in pipe flow? A. Gravity B. A pressure gradient C. Vacuum 2.What is a general description of the flow rate in laminar flow? A. Small B. Large
More informationFundamentals of Fluid Mechanics
Sixth Edition. Fundamentals of Fluid Mechanics International Student Version BRUCE R. MUNSON DONALD F. YOUNG Department of Aerospace Engineering and Engineering Mechanics THEODORE H. OKIISHI Department
More informationA COMPUTATIONAL FLUID DYNAMICS STUDY ON THE ACCURACY OF HEAT TRANSFER FROM A HORIZONTAL CYLINDER INTO QUIESCENT WATER
A COMPUTATIONAL FLUID DYNAMICS STUDY ON THE ACCURACY OF HEAT TRANSFER FROM A HORIZONTAL CYLINDER INTO QUIESCENT WATER William Logie and Elimar Frank Institut für Solartechnik SPF, 8640 Rapperswil (Switzerland)
More informationCOIL INPUT SCREENS. ITEM NUMBER: Always use a 1 through? In this field you might also use a dash and place quantity of coils here.
COIL INPUT SCREENS Example of a Water Coil Input Screen: (*please see the appendix for an example of an Evaporator, Steam or Condenser Coil input screen) PHYSICAL DATA ITEM NUMBER: Always use a 1 through?
More informationHVAC air curtains. Type InduAir
Air Conditioning Cooling Heating Ventilation HVAC air curtains Type InduAir The Energy Saving air curtain for Industrial Applications InduAir The solid, self-supporting housing of the energy saving air
More informationSulfur Tail Gas Thermal Oxidizer Systems By Peter Pickard
Sulfur Tail Gas Thermal Oxidizer Systems By Peter Pickard Introduction SRU s (Sulfur Recovery Units) are critical pieces of equipment in refineries and gas plants. SRUs remove sulfur compounds from certain
More informationHeat Transfer Analysis of Cylindrical Perforated Fins in Staggered Arrangement
International Journal of Innovative Technology and Exploring Engineering (IJITEE) ISSN: 2278-3075, Volume-2, Issue-5, April 203 Heat Transfer Analysis of Cylindrical Fins in Staggered Arrangement Amol
More information