T WO previous papers4 by one of the authors (with others)

Size: px
Start display at page:

Download "T WO previous papers4 by one of the authors (with others)"

Transcription

1 Influence of Bends or O bstructions a t th e F an Discharge O u tlet on the Perform ance of C entrifugal Fans By L. S. MARKS,1 J. H. RAUB,2 a n d H. R. PRATT3 FSP The form and d im en sion s o f th e in let d u cts and in let boxes o f a centrifugal fan have been show n to have a profound effect upon th e fan perform ance. T he object o f th e investigations, described in th is paper, w as to determ ine w hether bends or obstructions close to th e discharge end o f th e fan have an y sim ilar influence. N o su ch influence was found. T he conclusion reached is th a t w ith a com plete fan housing o f good design, a bend or ob stru ction connected directly to th e fan discharge w ill have n o ap preciable effect on th e fan perform ance and w ill result in th e sam e losses th a t would occur if th e bend or obstruction were located a t a considerable distan ce from th e fan. T WO previous papers4 by one of the authors (with others) presented results of investigations conducted to determine the influence of inlet boxes and inlet ducts on the performance of a centrifugal fan. It was shown that the capacity of the fan was greatly affected by the form and dimensions of the inlet structures. For constant rpm and with unrestricted discharge a poor inlet box reduced the capacity by as much as 60 per cent and a poor arrangement of bends in the inlet duct was found to reduce the capacity 40 per cent. The maximum efficiency of the fan, however, was affected only slightly by the form of the inlet box but in greater degree by poorly arranged inlet ducts. It was further shown that the capacity and efficiency of the fan could be restored largely by the use of appropriate guide vanes in the bends in the inlet ducts. It has been thought by many engineers that the performance of a centrifugal fan would be found to be similarly influenced by the form and dimensions of the discharge duct immediately adjacent to the discharge outlet of the fan housing and it was decided to investigate this matter. It would seem from a priori reasoning that any such influence would be slight. The structures on the inlet side of the fan determine the velocity distribution of the air at the fan inlet and consequently influence the fan operation. On the discharge side, the fan has already completed its work and the effect of bends or obstructions at the fan discharge presumably would be (1) to influence the conversion of velocity head to static pressure and (2) to increase the resistance against which the fan discharges in a way precisely similar to that offered by a more distant obstruction. The velocity distribution of the air as it discharges from a fan is less uniform than it becomes after traversing a length of straight duct and, as the resistance offered by a bend or obstruction is proportional to the square of the velocity, the total resistance will be somewhat greater when the obstruction is located at the fan discharge. This difference, however, should be negligible. Apart from this, it would seem that the only effect of an obstruction on the discharge side would be its influence on the pressures and velocities of the approaching air. Theoretical considerations show that the character of a fluid stream is affected by any obstruction which it approaches and that the influence of the obstruction extends upstream for an indefinitely great distance. The magnitude of this influence diminishes very rapidly as the distance from the obstruction increases and quickly becomes negligible. The disturbance is calculable for the simple condition of streamline flow of an ideal fluid of infinite cross-section. For this condition, with a spherical obstruction, the velocity of the approaching stream at a point two diameters upstream from the center of the sphere is diminished by one per cent. With a cylindrical obstruction of infinite length with its axis normal to the stream, the velocity along the line two diameters upstream from the axis of the cylinder is diminished six per cent. With a flat plate of infinite length and for flow normal to the plate, the velocity at a distance of one and one-half times the width of the plate upstream from the center line of plate is diminished five per cent. The magnitude of this disturbance is a maximum along the flow line approaching the center of a symmetrical obstruction and diminishes rapidly as the distance from the central-flow line increases. For non-ideal fluids (having viscosity and compressibility) 1 Professor of Mechanical Engineering, H arvard University, Cambridge, N. J. M r. P ra tt was graduated in 1932 from th e W ebb Institu te of Mass. Mem. A.S.M.E. Professor M arks was born in Bir Naval Architecture and in 1934 received the degree of S.M. from mingham, England. He received the degree of B.Sc. from the University H arvard University. He has had two years engine-room experience of London in 1892 and M.M.E. from Cornell University in on both steam and m otor ships, served one summer as draftsm an with He was with the Ames Iron Works, Oswego, N. Y. in 1894 and the Electric B oat Co., Groton, Conn., and is now employed as draftsm then went to H arvard University as instructor in mechanical engineering. an with the Federal Shipbuilding and Drydock Co. In 1900 he was made assistant professor and in 1909 was advanced 4 Influence of Inlet Boxes on the Performance of Induced-D raft to his present position. Professor M arks is author of Steam Fans, by L. S. M arks and E. A. W inzenburger, A.S.M.E. Trans., Tables and Diagrams, Gas and Oil Engines, Mechanical Engineers Handbook, The Airplane Engine, and has contributed numerous articles to the technical press. vol. 54, 1932, paper FSP Influence of Bends in Inlet D ucts on the Performance of Induced-Draft Fans, by L. S. M arks, John Lomax, and Randolph 2 Galesburg, Illinois. Jun. A.S.M.E. M r. R aub studied for Ashton, A.S.M.E. Trans., vol. 55, 1933, paper FSP six months at the ficole Alsacienne, Paris, France, was graduated in 1926 with the degree of B.S. from Knox College, Galesburg, 111., and in 1929 received the degree of M.S. in Mechanical Engineering and C ontributed by the Power Division for presentation a t the Annual Meeting, New York, N. Y., December 3 to 7, , of T h e A m e r i c a n S o c ie t y o p M e c h a n ic a l E n g i n e e r s. Business Administration from H arvard University. After graduation Discussion of this paper should be addressed to the Secretary, Mr. E aub was employed by the J. I. Case Threshing Machine Co. in the testing department, then by the Nash M otors Co. on production A.S.M.E., 29 W est 39th Street, New York, N. Y., and will be accepted until January 10, 1935, for publication in a later issue of Transactions. work and later was engaged by Ingersoll Steel and Disc Co. N o t e : Statem ents and opinions advanced in papers are to be in the engineering department. 3 Draftsman, Federal Shipbuilding and Drydock Co., Kearney, understood as individual expressions of their authors, and not those of the Society. 767

2 768 TRANSACTIONS OF THE AMERICAN SOCIETY OF MECHANICAL ENGINEERS E l e v a t ion Vi e w OTHER PISCH DUCTS ATTACH E O H E R? F i g. 1 A b h a n g e m e n t f o b T e s t s o n I n. S t u e t e v a n t F a n and..with^turbulent flow no adequate theory is available, but it would appear probable that the disturbance resulting from the presence of an obstruction would extend a shorter distance upstream than with the streamline flow of an ideal fluid. In the case of the discharge from the fan, there is turbulent flow and a limited cross-section of the steam. The obstruction (elbow, tee, etc.) will usually occupy the whole cross-section as seen downstream and such obstructions increase the total resistance against which the fan is operating but do not necessarily affect the performance of the fan proper. T e s t A r r a n g e m e n t s The investigations were carried out at the Gordon McKay Laboratory of the Harvard Engineering School on the 38-in., double-inlet, radial-tip fan which had been used previously for the inlet investigations. The fan housing includes a short expanding portion on the discharge side. As the discharge conditions were to be varied, it was decided to measure air volumes on the inlet side. This is a departure from the methods of the A.S.H.&V.E. Standard Test Code but it is believed that the method actually employed permits an accuracy of measurement greater than is possible with the code. The inlet arrangements are shown in Fig. 1. The air enters through a well-rounded nozzle into a large circular duct. This is transformed into a rectangular duct which splits into two ducts connecting with the two inlet boxes. All changes in shape and dimension of the ducts, or of direction of the air currents, are gradual and guide vanes are located in the curved sections. The air enters the inlet boxes with flow lines which, it is believed, approximate closely to those obtained with the more usual inlet arrangements. The operating conditions were controlled by a grid a (Fig. 1) made up of 36 vertical wooden slats l l/i«in- wide and 38 in. high. The fan capacity was controlled by varying the number of slats in position. They were always spaced in such manner as to distribute the flow uniformly over the cross-section of the duct. The volume of air flowing was calculated from the static pressure at the middle of the parallel portion of the nozzle. This pressure was checked many times against the static pressure measured in the duct at 6 (Fig. 1), and in no case was any difference discernible. Similarly an impact tube located in the center line of the nozzle a few inches downstream from the nozzle and facing upstream always gave a reading of exactly atmospheric pressure. The nozzle coefficient was determined by traverse with a small impact tube, following the method of the Bureau of Standards (Research Paper No. 49), and a coefficient of was obtained. It is believed that the air measurements are accurate within one per cent. The nozzle air measurements were compared wit h those obtained by pitot-tube traverses in the discharge duct following the Standard Test Code procedure. The fan housing and all joints in the ducts were gone over with great care to prevent leakage which in this case would be into the system. The only unavoidable leakages were at the places where the fan shaft passes through the inlet boxes and, at these places, felt washers pressing lightly against the shaft were provided. The leakage must have been negligible. Comparative tests gave the pitot-tube volume measurements not exceeding two per cent and averaging less than one per cent greater than the nozzle measurement for fan capacities between 30 and 100 per cent. As the pitot tube tends to read high under all circumstances, this difference may be regarded as verification of the nozzle measurements. The fan is shown in Fig. 2 and the housing in Fig. 3. In these tests the discharge bends, ducts, and all other obstructions were connected directly to the discharge outlet of the housing without any intermediate run of straight duct. On their discharge sides these structures were connected to straight runs of duct of length sufficient to permit the completion of regain of pressure and then discharged directly into the atmosphere. The straight runs of duct were about three diameters in length and their friction resistances have been neglected in calculating efficiencies so that these efficiencies are slightly low. In making comparisons with the condition of unobstructed discharge, the standard for comparison had a straight discharge duct about three diameters in length and for this case also the friction resistance of the discharge duct was neglected. The static pressure against which a fan operates is the difference between the static pressure at the discharge and the total pressure at the inlet. The inlet in this case is at the entrance

3 FUELS AND STEAM POWER FSP to the inlet boxes. Traverses were made at this location with pitot tubes, following the procedure of the Standard Test Code. The total pressure was not constant across the sections, although the variation was slight. After investigating the total pressure distribution for various fan capacities, it was found that the average total pressure occurred always at certain locations in the cross-section and in subsequent tests the pitot tubes were set in these locations for determining the total pressure at the inlet to the fan. of the fan. Any change in fan performance resulting from the presence of these bends or obstructions may result from (a) the resistance to flow offered by the bend or obstruction and/or (&) the influence which the bend or obstruction exercises on the fan performance. When there is no perceptible change in fan performance as determined in this manner, both of these factors must be negligible. The total resistance against which the fan operates is the sum of the static resistance and the velocity head. The velocity head was calculated from the mean velocity at the end of the discharge duct. This velocity is equal to the volume flowing per unit time, as determined by the inlet-nozzle measurement, F i g. 3 F a n H o u s in g a n d I n l e t B o x e s F ig. 4 A r r a n g e m e n t of D e g B e n d s F i o. 5 A r r a n g e m e n t of T e e D u c t On the discharge side a traverse of the cross-section near the discharge outlet of the fan housing shows considerable variation in static pressure too great to permit the use of any observation in that location for determining the fan resistance. The static pressure at the final discharge of the air was always atmospheric pressure and this was taken as the static pressure against which the fan discharged. By this procedure the bends or other obstructions on the discharge side of the fan were included as part divided by the terminal cross-sectional area of the discharge duct. T h e D is c h a r g e A r r a n g e m e n t s Two commonly occurring arrangements of the discharge were selected for investigation; 90-deg bend and tee discharge ducts. The details of these structures are shown in Figs. 4 and 5, respectively. As the discharge outlet in the fan housing was square, it was possible to test with the 90-deg bend in two different

4 770 TRANSACTIONS OF TH E AMERICAN SOCIETY OF MECHANICAL ENGINEERS orientations, discharging vertically upward and discharging laterally. Discharging vertically upward, the air passes through the bend with the same direction of rotation that it had when passing through the fan, while discharging laterally the direction of rotation is changed to a plane at 90 deg to that in the fan. The tee discharge duct (Fig. 5) consists of a short duct 14 in. long, 36 in. square containing three butterfly dampers and connecting with a larger duct, 44 in. square, with a sudden enlargement. The dampers were always operated wide open and can be oriented either with horizontal or vertical axes. The large duct can be blocked at one end so that the air may be discharged at either one or at both outlets. orifice of the fan housing and in the median line is given in Fig. 7. This curve shows that the velocity is practically uniform over the whole cross-section thereby explaining why the orientation of the 90-deg bend has no influence on the performance of the combination of fan and bend. The identity of the test results for (1) a straight discharge duct and (2 ) a 90-deg bend provided with guide vanes indicates (a) that the resistance of the 90-deg bend is negligible and (b) that its presence does not affect perceptibly the action of the fan. The difference between the performance curves with and without the guide vanes must be ascribed entirely to the losses in the vaneless bend. This same loss would have occurred if the bend had been placed in a more remote location in the discharge duct. The performance of the fan itself is uninfluenced by connecting a 90-deg bend directly to the fan discharge. R e s u l t s o p T e s t s W i t h T e e D is c h a r g e D u c t s The variables in the operating conditions for these tests were: (1) The orientation of the dampers, either with vertical or with horizontal axes, (2) discharge through both branches of the tee or through only one branch, and (3 ) the use of guide vanes as shown by dotted line in Fig. 5. F i o. 6 P e r f o r m a n c e C o r v e s W i t h D e g B e n d s To diminish the resistance of these structures, they were later provided with guide vanes which are indicated by dotted lines in Figs. 4 and 5. For the 90-deg bend, two guide vanes were used, concentric with the bend and dividing it into three channels of equal depth. For the tee duct an attem pt was made to divide the approaching air into ten streams of equal horizontal width. No attem pt was made, however, to control the sudden enlargement of each stream. R e s u l t s o f T e s t s W i t h a D e g B e n d The performance curves shown in Fig. 6 are for three conditions: (1) With a straight discharge duct 9 ft 5 in. long; (2) with the 90-deg bend oriented horizontally and terminating in a straight run of duct 9 ft 5 in. long; and (3) with the 90 deg bend oriented as in (2), but fitted with two guide vanes, and terminating in the same straight run of duct. For conditions (1) and (3) the curves are so close together that they may be considered identical; for condition (2) the total pressures and total efficiencies at any capacity are less than for conditions (1) and (3), but the power requirements are the same in all cases. Performance curves drawn for the same conditions as in Fig. 6 but with the 90-deg bend discharging vertically upward are identical with those of Fig. 6. If the velocity of the air leaving the fan housing is uniform across the discharge section, there would be no reason to expect that the orientation of the 90-deg bend would have any effect on the performance of the combination of fan and bend. A vertical traverse by pitot tube near the discharge F io. 7 V e l o c i t y - H e a d D i s t r i b u t i o n a t D i s c h a r g e F r o m F a n The results obtained are as follows: The investigation of the influence of the orientation of the dampers yielded entirely negative results. The performance of the fan was not observably affected. This result is interpreted as indicating that the flow through the dampers is substantially parallel to the axis of the duct. Discharge through both branches of the tee duct is found to give better performance than through one branch only. This is quite marked when static pressures and static efficiencies alone are considered as shown in Fig. 8. It is less marked, however, for

5 total pressures and total efficiencies (Fig. 9) because of the doubled terminal velocity, for a given capacity, when discharging through one branch only. The use of guide vanes has no appreciable influence either for single or for double discharge. The static pressures and efficiencies with two-way discharge are found to coincide with the values for a short straight duct, but this result must be fortuitous since the terminal discharge areas are entirely different in the two cases. FUELS AND STEAM POWER FSP F x o. 8 P e r f o r m a n c e C u r v e s W i t h T e e D u c t (B ased on s ta tic pressu re.) The total pressures and efficiencies are considerably less than for a straight-discharge duct. With the tee duct there is a sudden enlargement from a cross-section of 9 sq ft to one of 26.8 sq ft and, at 40,000 cfm, the mean velocity changes suddenly from 74 to 25 ft per sec. The corresponding velocity heads are 1.23 and 0.14 in. of water, or a drop in velocity head of 1.09 in. The tests show that the loss in total pressure resulting from the use of the tee duct is approximately this amount whether guide vanes are used or not. The presence of guide vanes does not affect the magnitude of the sudden enlargement but might be expected to guide the air so as to result in increased regain. This F i g. 9 P e r f o r m a n c e C u r v e s W i t h T e e D u c t (B ased on to ta l pressure.) result, if it actually occurred, was not of sufficient magnitude to be perceptible. Additional tests were made to determine the resistance of the tee duct by connecting it to the end of a 60-ft run of straight duct. At a capacity of 40,000 cfm its resistance was in good agreement with the difference between the total pressures for the straight duct and the tee as shown in Fig. 9. It would appear then that the only effect of the tee duct is to increase the resistance on the discharge side and that it has no influence on the fan performance. C o n c l u s i o n s It may be concluded from this investigation that the operation of the fan tested was not affected to any appreciable extent by sudden enlargement or change of direction of the air stream as it left the fan housing. It is the opinion of the authors that the conclusions stated may be applied quite generally whenever the fan housing is sufficiently complete to give the discharged air a general direction of flow and a uniform distribution at the outlet. Any extension of the conclusion, however, to other types of fan and other arrangements of housing must be based largely on opinion.

HVAC Clinic. Duct Design

HVAC Clinic. Duct Design HVAC Clinic Duct Design Table Of Contents Introduction... 3 Fundamentals Of Duct Design... 3 Pressure Changes In A System... 8 Example 1... 13 Duct Design Methods... 15 Example 2... 15 Introduction The

More information

Flow Measurement in Pipes and Ducts COURSE CONTENT

Flow Measurement in Pipes and Ducts COURSE CONTENT Flow Measurement in Pipes and Ducts Dr. Harlan H. Bengtson, P.E. COURSE CONTENT 1. Introduction This course is about measurement of the flow rate of a fluid flowing under pressure in a closed conduit.

More information

Lesson 37 Transmission Of Air In Air Conditioning Ducts

Lesson 37 Transmission Of Air In Air Conditioning Ducts Lesson 37 Transmission Of Air In Air Conditioning Ducts Version 1 ME, IIT Kharagpur 1 The specific objectives of this chapter are to: 1. Describe an Air Handling Unit (AHU) and its functions (Section 37.1).

More information

Lecture 22. Mechanical Energy Balance

Lecture 22. Mechanical Energy Balance Lecture 22 Mechanical Energy Balance Contents Exercise 1 Exercise 2 Exercise 3 Key Words: Fluid flow, Macroscopic Balance, Frictional Losses, Turbulent Flow Exercise 1 It is proposed to install a fan to

More information

Applied Fluid Mechanics

Applied Fluid Mechanics Applied Fluid Mechanics 1. The Nature of Fluid and the Study of Fluid Mechanics 2. Viscosity of Fluid 3. Pressure Measurement 4. Forces Due to Static Fluid 5. Buoyancy and Stability 6. Flow of Fluid and

More information

Chapter Four fluid flow mass, energy, Bernoulli and momentum

Chapter Four fluid flow mass, energy, Bernoulli and momentum 4-1Conservation of Mass Principle Consider a control volume of arbitrary shape, as shown in Fig (4-1). Figure (4-1): the differential control volume and differential control volume (Total mass entering

More information

Applied Fluid Mechanics

Applied Fluid Mechanics Applied Fluid Mechanics 1. The Nature of Fluid and the Study of Fluid Mechanics 2. Viscosity of Fluid 3. Pressure Measurement 4. Forces Due to Static Fluid 5. Buoyancy and Stability 6. Flow of Fluid and

More information

AEROSPACE ENGINEERING DEPARTMENT. Second Year - Second Term ( ) Fluid Mechanics & Gas Dynamics

AEROSPACE ENGINEERING DEPARTMENT. Second Year - Second Term ( ) Fluid Mechanics & Gas Dynamics AEROSPACE ENGINEERING DEPARTMENT Second Year - Second Term (2008-2009) Fluid Mechanics & Gas Dynamics Similitude,Dimensional Analysis &Modeling (1) [7.2R*] Some common variables in fluid mechanics include:

More information

COURSE NUMBER: ME 321 Fluid Mechanics I 3 credit hour. Basic Equations in fluid Dynamics

COURSE NUMBER: ME 321 Fluid Mechanics I 3 credit hour. Basic Equations in fluid Dynamics COURSE NUMBER: ME 321 Fluid Mechanics I 3 credit hour Basic Equations in fluid Dynamics Course teacher Dr. M. Mahbubur Razzaque Professor Department of Mechanical Engineering BUET 1 Description of Fluid

More information

ASSESSMENT OF DESIGN METHODOLOGY AND THREE DIMENSIONAL NUMERICAL (CFD) ANALYSIS OF CENTRIFUGAL BLOWER

ASSESSMENT OF DESIGN METHODOLOGY AND THREE DIMENSIONAL NUMERICAL (CFD) ANALYSIS OF CENTRIFUGAL BLOWER ASSESSMENT OF DESIGN METHODOLOGY AND THREE DIMENSIONAL NUMERICAL (CFD) ANALYSIS OF CENTRIFUGAL BLOWER D. R. Chaudhari 1, H. N. Patel 2 1,2 Mechanical Department, Government Engineering College Dahod, (India)

More information

ME332 FLUID MECHANICS LABORATORY (PART I)

ME332 FLUID MECHANICS LABORATORY (PART I) ME332 FLUID MECHANICS LABORATORY (PART I) Mihir Sen Department of Aerospace and Mechanical Engineering University of Notre Dame Notre Dame, IN 46556 Version: January 14, 2002 Contents Unit 1: Hydrostatics

More information

Visualization of flow pattern over or around immersed objects in open channel flow.

Visualization of flow pattern over or around immersed objects in open channel flow. EXPERIMENT SEVEN: FLOW VISUALIZATION AND ANALYSIS I OBJECTIVE OF THE EXPERIMENT: Visualization of flow pattern over or around immersed objects in open channel flow. II THEORY AND EQUATION: Open channel:

More information

equation 4.1 INTRODUCTION

equation 4.1 INTRODUCTION 4 The momentum equation 4.1 INTRODUCTION It is often important to determine the force produced on a solid body by fluid flowing steadily over or through it. For example, there is the force exerted on a

More information

Chapter 4 DYNAMICS OF FLUID FLOW

Chapter 4 DYNAMICS OF FLUID FLOW Faculty Of Engineering at Shobra nd Year Civil - 016 Chapter 4 DYNAMICS OF FLUID FLOW 4-1 Types of Energy 4- Euler s Equation 4-3 Bernoulli s Equation 4-4 Total Energy Line (TEL) and Hydraulic Grade Line

More information

Chimney Sizing. Project Name: Location: Type Appliance: Hot Water Heater Incinerator. LP Gas #2 Oil #6 Oil Wood/Coal Waste (Type ) Appliance Input:

Chimney Sizing. Project Name: Location: Type Appliance: Hot Water Heater Incinerator. LP Gas #2 Oil #6 Oil Wood/Coal Waste (Type ) Appliance Input: Chimney Sizing Project Name: Location: Type Appliance: Type Fuel: Appliance Input: Boiler Hot Water Heater Incinerator Natural Gas LP Gas #2 Oil #6 Oil Wood/Coal Waste (Type ) BTU Hp Lbs/hr Height Above

More information

Consider a control volume in the form of a straight section of a streamtube ABCD.

Consider a control volume in the form of a straight section of a streamtube ABCD. 6 MOMENTUM EQUATION 6.1 Momentum and Fluid Flow In mechanics, the momentum of a particle or object is defined as the product of its mass m and its velocity v: Momentum = mv The particles of a fluid stream

More information

10.52 Mechanics of Fluids Spring 2006 Problem Set 3

10.52 Mechanics of Fluids Spring 2006 Problem Set 3 10.52 Mechanics of Fluids Spring 2006 Problem Set 3 Problem 1 Mass transfer studies involving the transport of a solute from a gas to a liquid often involve the use of a laminar jet of liquid. The situation

More information

Lab Section Date. ME4751 Air Flow Rate Measurement

Lab Section Date. ME4751 Air Flow Rate Measurement Name Lab Section Date ME4751 Air Flow Rate Measurement Objective The objective of this experiment is to determine the volumetric flow rate of air flowing through a pipe using a Pitot-static tube and a

More information

LECTURE-11 FAN AND DUCT SYSTEM-2

LECTURE-11 FAN AND DUCT SYSTEM-2 L ecturer: -D D r. E sam M ejbil A bid Subject: A ir Conditioning and R efrigeration Year: Y Fourth B.Sc. D E P A R TM E N O F M E CH A N ICA L E N G IN E E R IN B abylon U niversity College of E ngineering

More information

Experiment (4): Flow measurement

Experiment (4): Flow measurement Experiment (4): Flow measurement Introduction: The flow measuring apparatus is used to familiarize the students with typical methods of flow measurement of an incompressible fluid and, at the same time

More information

nozzle which is fitted to a pipe through which the liquid is flowing under pressure.

nozzle which is fitted to a pipe through which the liquid is flowing under pressure. Impact of Jets 1. The liquid comes out in the form of a jet from the outlet of a nozzle which is fitted to a pipe through which the liquid is flowing under pressure. The following cases of the impact of

More information

Introduction to Fluid Machines, and Compressible Flow Prof. S. K. Som Department of Mechanical Engineering Indian Institute of Technology, Kharagpur

Introduction to Fluid Machines, and Compressible Flow Prof. S. K. Som Department of Mechanical Engineering Indian Institute of Technology, Kharagpur Introduction to Fluid Machines, and Compressible Flow Prof. S. K. Som Department of Mechanical Engineering Indian Institute of Technology, Kharagpur Lecture - 09 Introduction to Reaction Type of Hydraulic

More information

PART 1B EXPERIMENTAL ENGINEERING. SUBJECT: FLUID MECHANICS & HEAT TRANSFER LOCATION: HYDRAULICS LAB (Gnd Floor Inglis Bldg) BOUNDARY LAYERS AND DRAG

PART 1B EXPERIMENTAL ENGINEERING. SUBJECT: FLUID MECHANICS & HEAT TRANSFER LOCATION: HYDRAULICS LAB (Gnd Floor Inglis Bldg) BOUNDARY LAYERS AND DRAG 1 PART 1B EXPERIMENTAL ENGINEERING SUBJECT: FLUID MECHANICS & HEAT TRANSFER LOCATION: HYDRAULICS LAB (Gnd Floor Inglis Bldg) EXPERIMENT T3 (LONG) BOUNDARY LAYERS AND DRAG OBJECTIVES a) To measure the velocity

More information

Piping Systems and Flow Analysis (Chapter 3)

Piping Systems and Flow Analysis (Chapter 3) Piping Systems and Flow Analysis (Chapter 3) 2 Learning Outcomes (Chapter 3) Losses in Piping Systems Major losses Minor losses Pipe Networks Pipes in series Pipes in parallel Manifolds and Distribution

More information

V/ t = 0 p/ t = 0 ρ/ t = 0. V/ s = 0 p/ s = 0 ρ/ s = 0

V/ t = 0 p/ t = 0 ρ/ t = 0. V/ s = 0 p/ s = 0 ρ/ s = 0 UNIT III FLOW THROUGH PIPES 1. List the types of fluid flow. Steady and unsteady flow Uniform and non-uniform flow Laminar and Turbulent flow Compressible and incompressible flow Rotational and ir-rotational

More information

CHAPTER 3 BASIC EQUATIONS IN FLUID MECHANICS NOOR ALIZA AHMAD

CHAPTER 3 BASIC EQUATIONS IN FLUID MECHANICS NOOR ALIZA AHMAD CHAPTER 3 BASIC EQUATIONS IN FLUID MECHANICS 1 INTRODUCTION Flow often referred as an ideal fluid. We presume that such a fluid has no viscosity. However, this is an idealized situation that does not exist.

More information

4 Mechanics of Fluids (I)

4 Mechanics of Fluids (I) 1. The x and y components of velocity for a two-dimensional flow are u = 3.0 ft/s and v = 9.0x ft/s where x is in feet. Determine the equation for the streamlines and graph representative streamlines in

More information

ME332 FLUID MECHANICS LABORATORY (PART II)

ME332 FLUID MECHANICS LABORATORY (PART II) ME332 FLUID MECHANICS LABORATORY (PART II) Mihir Sen Department of Aerospace and Mechanical Engineering University of Notre Dame Notre Dame, IN 46556 Version: April 2, 2002 Contents Unit 5: Momentum transfer

More information

Lecture 24. Design of flow meters

Lecture 24. Design of flow meters Lecture 24 Design of flow meters Contents Exercise 1 Exercise 2 Exercise 3 Key Words: Fluid flow, Macroscopic Balance, Frictional Losses, Turbulent Flow, Venturimeter, Orifice Meter, Pitot Tube Exercise

More information

EXPERIMENT No.1 FLOW MEASUREMENT BY ORIFICEMETER

EXPERIMENT No.1 FLOW MEASUREMENT BY ORIFICEMETER EXPERIMENT No.1 FLOW MEASUREMENT BY ORIFICEMETER 1.1 AIM: To determine the co-efficient of discharge of the orifice meter 1.2 EQUIPMENTS REQUIRED: Orifice meter test rig, Stopwatch 1.3 PREPARATION 1.3.1

More information

Experiment No.4: Flow through Venturi meter. Background and Theory

Experiment No.4: Flow through Venturi meter. Background and Theory Experiment No.4: Flow through Venturi meter Background and Theory Introduction Flow meters are used in the industry to measure the volumetric flow rate of fluids. Differential pressure type flow meters

More information

405 Compact Orifice Series and 1595 Conditioning Orifice Plate Flow Test Data Book and Flow Handbook

405 Compact Orifice Series and 1595 Conditioning Orifice Plate Flow Test Data Book and Flow Handbook Reference Manual 405 Compact Orifice Series and 1595 Conditioning Orifice Plate Flow Test Book and Flow Handbook www.rosemount.com Reference Manual 405 and 1595 405 Compact Orifice Series and 1595 Conditioning

More information

Friction Factors and Drag Coefficients

Friction Factors and Drag Coefficients Levicky 1 Friction Factors and Drag Coefficients Several equations that we have seen have included terms to represent dissipation of energy due to the viscous nature of fluid flow. For example, in the

More information

vector H. If O is the point about which moments are desired, the angular moment about O is given:

vector H. If O is the point about which moments are desired, the angular moment about O is given: The angular momentum A control volume analysis can be applied to the angular momentum, by letting B equal to angularmomentum vector H. If O is the point about which moments are desired, the angular moment

More information

Signature: (Note that unsigned exams will be given a score of zero.)

Signature: (Note that unsigned exams will be given a score of zero.) Neatly print your name: Signature: (Note that unsigned exams will be given a score of zero.) Circle your lecture section (-1 point if not circled, or circled incorrectly): Prof. Dabiri Prof. Wassgren Prof.

More information

5 ENERGY EQUATION OF FLUID MOTION

5 ENERGY EQUATION OF FLUID MOTION 5 ENERGY EQUATION OF FLUID MOTION 5.1 Introduction In order to develop the equations that describe a flow, it is assumed that fluids are subject to certain fundamental laws of physics. The pertinent laws

More information

Lecture23. Flowmeter Design.

Lecture23. Flowmeter Design. Lecture23 Flowmeter Design. Contents of lecture Design of flowmeter Principles of flow measurement; i) Venturi and ii) Orifice meter and nozzle Relationship between flow rate and pressure drop Relation

More information

FE Fluids Review March 23, 2012 Steve Burian (Civil & Environmental Engineering)

FE Fluids Review March 23, 2012 Steve Burian (Civil & Environmental Engineering) Topic: Fluid Properties 1. If 6 m 3 of oil weighs 47 kn, calculate its specific weight, density, and specific gravity. 2. 10.0 L of an incompressible liquid exert a force of 20 N at the earth s surface.

More information

Hydraulics and hydrology

Hydraulics and hydrology Hydraulics and hydrology - project exercises - Class 4 and 5 Pipe flow Discharge (Q) (called also as the volume flow rate) is the volume of fluid that passes through an area per unit time. The discharge

More information

Fluid Dynamics Exercises and questions for the course

Fluid Dynamics Exercises and questions for the course Fluid Dynamics Exercises and questions for the course January 15, 2014 A two dimensional flow field characterised by the following velocity components in polar coordinates is called a free vortex: u r

More information

An Experimental Investigation to Control the Flow Emerging From a Wide Angle Diffuser

An Experimental Investigation to Control the Flow Emerging From a Wide Angle Diffuser IOSR Journal of Engineering (IOSRJEN) ISSN: 5-3 ISBN: 878-879 PP 7-3 National Symposium on engineering and Research An Experimental Investigation to Control the Flow Emerging From a Wide Angle Diffuser

More information

Twin City Fan Companies. Fan System Effects

Twin City Fan Companies. Fan System Effects Fan System Effects Outline Fan Testing Review Definition of System Effect Old ASHRAE guidelines AMCA 201 System Effect Factors Examples Demonstration Aimed at the fan system designer There are two goals:

More information

Applied Fluid Mechanics

Applied Fluid Mechanics Applied Fluid Mechanics 1. The Nature of Fluid and the Study of Fluid Mechanics 2. Viscosity of Fluid 3. Pressure Measurement 4. Forces Due to Static Fluid 5. Buoyancy and Stability 6. Flow of Fluid and

More information

Mechanical Measurements and Metrology Prof. S. P. Venkateshan Department of Mechanical Engineering Indian Institute of Technology, Madras

Mechanical Measurements and Metrology Prof. S. P. Venkateshan Department of Mechanical Engineering Indian Institute of Technology, Madras Mechanical Measurements and Metrology Prof. S. P. Venkateshan Department of Mechanical Engineering Indian Institute of Technology, Madras Module - 3 Lecture - 33 Measurement of Volume and Mass Flow Rate

More information

Please welcome for any correction or misprint in the entire manuscript and your valuable suggestions kindly mail us

Please welcome for any correction or misprint in the entire manuscript and your valuable suggestions kindly mail us Problems of Practices Of Fluid Mechanics Compressible Fluid Flow Prepared By Brij Bhooshan Asst. Professor B. S. A. College of Engg. And Technology Mathura, Uttar Pradesh, (India) Supported By: Purvi Bhooshan

More information

UNIT I FLUID PROPERTIES AND STATICS

UNIT I FLUID PROPERTIES AND STATICS SIDDHARTH GROUP OF INSTITUTIONS :: PUTTUR Siddharth Nagar, Narayanavanam Road 517583 QUESTION BANK (DESCRIPTIVE) Subject with Code : Fluid Mechanics (16CE106) Year & Sem: II-B.Tech & I-Sem Course & Branch:

More information

2 Internal Fluid Flow

2 Internal Fluid Flow Internal Fluid Flow.1 Definitions Fluid Dynamics The study of fluids in motion. Static Pressure The pressure at a given point exerted by the static head of the fluid present directly above that point.

More information

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 information

Chapter 7 The Energy Equation

Chapter 7 The Energy Equation Chapter 7 The Energy Equation 7.1 Energy, Work, and Power When matter has energy, the matter can be used to do work. A fluid can have several forms of energy. For example a fluid jet has kinetic energy,

More information

405 Compact Orifice Series and 1595 Conditioning Orifice Plate Flow Test Data Book and Flow Handbook

405 Compact Orifice Series and 1595 Conditioning Orifice Plate Flow Test Data Book and Flow Handbook 405 Compact Orifice Series and 1595 Conditioning Orifice Plate Flow Test Book and Flow Handbook www.rosemount.com 405 Compact Orifice Series and 1595 Conditioning Orifice Plate Flow Test Book NOTICE Read

More information

FLUID MECHANICS PROF. DR. METİN GÜNER COMPILER

FLUID MECHANICS PROF. DR. METİN GÜNER COMPILER FLUID MECHANICS PROF. DR. METİN GÜNER COMPILER ANKARA UNIVERSITY FACULTY OF AGRICULTURE DEPARTMENT OF AGRICULTURAL MACHINERY AND TECHNOLOGIES ENGINEERING 1 5. FLOW IN PIPES Liquid or gas flow through pipes

More information

Numerical and Experimental Study on the Effect of Guide Vane Insertion on the Flow Characteristics in a 90º Rectangular Elbow

Numerical and Experimental Study on the Effect of Guide Vane Insertion on the Flow Characteristics in a 90º Rectangular Elbow Numerical and Experimental Study on the Effect of Guide Vane Insertion on the Flow Characteristics in a 90º Rectangular Elbow Sutardi 1, Wawan A. W., Nadia, N. and Puspita, K. 1 Mechanical Engineering

More information

ABSTRACT I. INTRODUCTION

ABSTRACT I. INTRODUCTION 2016 IJSRSET Volume 2 Issue 4 Print ISSN : 2395-1990 Online ISSN : 2394-4099 Themed Section: Engineering and Technology Analysis of Compressible Effect in the Flow Metering By Orifice Plate Using Prasanna

More information

Principles of Convection

Principles of Convection Principles of Convection Point Conduction & convection are similar both require the presence of a material medium. But convection requires the presence of fluid motion. Heat transfer through the: Solid

More information

The Fluid Flow in the T-Junction. The Comparison of the Numerical Modeling and Piv Measurement

The Fluid Flow in the T-Junction. The Comparison of the Numerical Modeling and Piv Measurement Available online at www.sciencedirect.com Procedia Engineering 39 (2012 ) 19 27 XIIIth International Scientific and Engineering Conference HERVICON-2011 The Fluid Flow in the T-Junction. The Comparison

More information

If a stream of uniform velocity flows into a blunt body, the stream lines take a pattern similar to this: Streamlines around a blunt body

If a stream of uniform velocity flows into a blunt body, the stream lines take a pattern similar to this: Streamlines around a blunt body Venturimeter & Orificemeter ELEMENTARY HYDRAULICS National Certificate in Technology (Civil Engineering) Chapter 5 Applications of the Bernoulli Equation The Bernoulli equation can be applied to a great

More information

Objectives. Conservation of mass principle: Mass Equation The Bernoulli equation Conservation of energy principle: Energy equation

Objectives. Conservation of mass principle: Mass Equation The Bernoulli equation Conservation of energy principle: Energy equation Objectives Conservation of mass principle: Mass Equation The Bernoulli equation Conservation of energy principle: Energy equation Conservation of Mass Conservation of Mass Mass, like energy, is a conserved

More information

Mass of fluid leaving per unit time

Mass of fluid leaving per unit time 5 ENERGY EQUATION OF FLUID MOTION 5.1 Eulerian Approach & Control Volume In order to develop the equations that describe a flow, it is assumed that fluids are subject to certain fundamental laws of physics.

More information

UNIT II CONVECTION HEAT TRANSFER

UNIT II CONVECTION HEAT TRANSFER UNIT II CONVECTION HEAT TRANSFER Convection is the mode of heat transfer between a surface and a fluid moving over it. The energy transfer in convection is predominately due to the bulk motion of the fluid

More information

Chapter 6. Losses due to Fluid Friction

Chapter 6. Losses due to Fluid Friction Chapter 6 Losses due to Fluid Friction 1 Objectives ä To measure the pressure drop in the straight section of smooth, rough, and packed pipes as a function of flow rate. ä To correlate this in terms of

More information

AN INVESTIGATION OF VELOCITY DISTRIBUTION IN TEST SECTION OF WRIGHT BROTHERS WIND TUNNEL. Holden W. Withington

AN INVESTIGATION OF VELOCITY DISTRIBUTION IN TEST SECTION OF WRIGHT BROTHERS WIND TUNNEL. Holden W. Withington AN NVESTGATON OF VELOCTY DSTRBUTON N TEST SECTON OF WRGHT BROTHERS WND TUNNEL by Holden W. Withington Submitted in Partial Fulfillment of the Requirements for the Degree of Bachelor of Science in Aeronautical

More information

Efficiency of an Expansive Transition in an Open Channel Subcritical Flow

Efficiency of an Expansive Transition in an Open Channel Subcritical Flow DUET Journal Vol., Issue, June of an Expansive Transition in an Open Channel Subcritical Flow B. C. Basak and M. Alauddin Department of Civil Engineering Dhaka University of Engineering & Technology, Gazipur,

More information

The online of midterm-tests of Fluid Mechanics 1

The online of midterm-tests of Fluid Mechanics 1 The online of midterm-tests of Fluid Mechanics 1 1) The information on a can of pop indicates that the can contains 460 ml. The mass of a full can of pop is 3.75 lbm while an empty can weights 80.5 lbf.

More information

Analysis of Pressure Losses in Conditioned Air Distribution: Case Study of an Industrial Cafeteria

Analysis of Pressure Losses in Conditioned Air Distribution: Case Study of an Industrial Cafeteria International Journal of Engineering Works Kambohwell Publisher Enterprises ISSN: 0-0 Vol., Issue, pp. -, March, 0 www.kwpublisher.com Analysis of Pressure Losses in Conditioned Air Distribution: Case

More information

A STUDY ON THE BEHAVIOR OF SHOCK WAVE AND VORTEX RING DISCHARGED FROM A PIPE

A STUDY ON THE BEHAVIOR OF SHOCK WAVE AND VORTEX RING DISCHARGED FROM A PIPE A STUDY ON THE BEHAVIOR OF SHOCK WAVE AND VORTEX RING DISCHARGED FROM A PIPE S. KITAJIMA 1, J. IWAMOTO 2 and E. TAMURA 3 Corresponding author S. KITAJIMA ABSTRACT In this paper, the behavior of shock wave

More information

R09. d water surface. Prove that the depth of pressure is equal to p +.

R09. d water surface. Prove that the depth of pressure is equal to p +. Code No:A109210105 R09 SET-1 B.Tech II Year - I Semester Examinations, December 2011 FLUID MECHANICS (CIVIL ENGINEERING) Time: 3 hours Max. Marks: 75 Answer any five questions All questions carry equal

More information

ISO 9906 INTERNATIONAL STANDARD. Rotodynamic pumps Hydraulic performance acceptance tests Grades 1 and 2

ISO 9906 INTERNATIONAL STANDARD. Rotodynamic pumps Hydraulic performance acceptance tests Grades 1 and 2 INTERNATIONAL STANDARD ISO 9906 First edition 1999-1-15 Rotodynamic pumps Hydraulic performance acceptance tests Grades 1 and Pompes rotodynamiques Essais de fonctionnement hydraulique pour la réception

More information

405 Compact Orifice Series and 1595 Conditioning Orifice Plate Flow Test Data Book and Flow Handbook

405 Compact Orifice Series and 1595 Conditioning Orifice Plate Flow Test Data Book and Flow Handbook 405 Compact Orifice Series and 1595 Conditioning Orifice Plate Flow Test Book and Flow Handbook www.rosemount.com 405 and 1595 405 Compact Orifice Series and 1595 Conditioning Orifice Plate Flow Test

More information

DESIGN AND CONSTRUCTION OF A WATER TUNNEL. Stephen C. Ko

DESIGN AND CONSTRUCTION OF A WATER TUNNEL. Stephen C. Ko i DESGN AND CONSTRUCTON OF A WATER TUNNEL By Stephen C. Ko This work has been carried out as a part of a grant from the National Science Foundation for the development of fluid mechanics laboratory equipments

More information

Department of Energy Sciences, LTH

Department of Energy Sciences, LTH Department of Energy Sciences, LTH MMV11 Fluid Mechanics LABORATION 1 Flow Around Bodies OBJECTIVES (1) To understand how body shape and surface finish influence the flow-related forces () To understand

More information

6.1 Momentum Equation for Frictionless Flow: Euler s Equation The equations of motion for frictionless flow, called Euler s

6.1 Momentum Equation for Frictionless Flow: Euler s Equation The equations of motion for frictionless flow, called Euler s Chapter 6 INCOMPRESSIBLE INVISCID FLOW All real fluids possess viscosity. However in many flow cases it is reasonable to neglect the effects of viscosity. It is useful to investigate the dynamics of an

More information

Viscous Flow in Ducts

Viscous Flow in Ducts Dr. M. Siavashi Iran University of Science and Technology Spring 2014 Objectives 1. Have a deeper understanding of laminar and turbulent flow in pipes and the analysis of fully developed flow 2. Calculate

More information

S.E. (Mech.) (First Sem.) EXAMINATION, (Common to Mech/Sandwich) FLUID MECHANICS (2008 PATTERN) Time : Three Hours Maximum Marks : 100

S.E. (Mech.) (First Sem.) EXAMINATION, (Common to Mech/Sandwich) FLUID MECHANICS (2008 PATTERN) Time : Three Hours Maximum Marks : 100 Total No. of Questions 12] [Total No. of Printed Pages 8 Seat No. [4262]-113 S.E. (Mech.) (First Sem.) EXAMINATION, 2012 (Common to Mech/Sandwich) FLUID MECHANICS (2008 PATTERN) Time : Three Hours Maximum

More information

Pipe Flow. Lecture 17

Pipe Flow. Lecture 17 Pipe Flow Lecture 7 Pipe Flow and the Energy Equation For pipe flow, the Bernoulli equation alone is not sufficient. Friction loss along the pipe, and momentum loss through diameter changes and corners

More information

Fluid Mechanics II 3 credit hour. Fluid flow through pipes-minor losses

Fluid Mechanics II 3 credit hour. Fluid flow through pipes-minor losses COURSE NUMBER: ME 323 Fluid Mechanics II 3 credit hour Fluid flow through pipes-minor losses Course teacher Dr. M. Mahbubur Razzaque Professor Department of Mechanical Engineering BUET 1 Losses in Noncircular

More information

1.060 Engineering Mechanics II Spring Problem Set 4

1.060 Engineering Mechanics II Spring Problem Set 4 1.060 Engineering Mechanics II Spring 2006 Due on Monday, March 20th Problem Set 4 Important note: Please start a new sheet of paper for each problem in the problem set. Write the names of the group members

More information

Part A: 1 pts each, 10 pts total, no partial credit.

Part A: 1 pts each, 10 pts total, no partial credit. Part A: 1 pts each, 10 pts total, no partial credit. 1) (Correct: 1 pt/ Wrong: -3 pts). The sum of static, dynamic, and hydrostatic pressures is constant when flow is steady, irrotational, incompressible,

More information

Given the water behaves as shown above, which direction will the cylinder rotate?

Given the water behaves as shown above, which direction will the cylinder rotate? water stream fixed but free to rotate Given the water behaves as shown above, which direction will the cylinder rotate? ) Clockwise 2) Counter-clockwise 3) Not enough information F y U 0 U F x V=0 V=0

More information

Applied Fluid Mechanics

Applied Fluid Mechanics Applied Fluid Mechanics 1. The Nature of Fluid and the Study of Fluid Mechanics 2. Viscosity of Fluid 3. Pressure Measurement 4. Forces Due to Static Fluid 5. Buoyancy and Stability 6. Flow of Fluid and

More information

2 Navier-Stokes Equations

2 Navier-Stokes Equations 1 Integral analysis 1. Water enters a pipe bend horizontally with a uniform velocity, u 1 = 5 m/s. The pipe is bended at 90 so that the water leaves it vertically downwards. The input diameter d 1 = 0.1

More information

Flow in a P ipe o f Rectangular Cross-Section.

Flow in a P ipe o f Rectangular Cross-Section. 691 Flow in a P ipe o f Rectangular Cross-Section. By R. J. Co rnish, M.Sc., Assistant Lecturer in Engineering in the University of Manchester. (Communicated by E. A. Milne, F.R.S. Received June 22, 1928.)

More information

ENGINEERING FLUID MECHANICS. CHAPTER 1 Properties of Fluids

ENGINEERING FLUID MECHANICS. CHAPTER 1 Properties of Fluids CHAPTER 1 Properties of Fluids ENGINEERING FLUID MECHANICS 1.1 Introduction 1.2 Development of Fluid Mechanics 1.3 Units of Measurement (SI units) 1.4 Mass, Density, Specific Weight, Specific Volume, Specific

More information

1-Reynold s Experiment

1-Reynold s Experiment Lect.No.8 2 nd Semester Flow Dynamics in Closed Conduit (Pipe Flow) 1 of 21 The flow in closed conduit ( flow in pipe ) is differ from this occur in open channel where the flow in pipe is at a pressure

More information

The Design of Gating System 3. Theoretical considerations in gating design

The Design of Gating System 3. Theoretical considerations in gating design MME 345 Lecture 16 The Design of Gating System 3. Theoretical considerations in gating design Ref: [1] ASM Metal Handbook, Vol. 15: Casting, ASM International [] Taylor, Flemings, and Wulff. Foundry engineering,

More information

CH.1 Overview of Fluid Mechanics/22 MARKS. 1.1 Fluid Fundamentals.

CH.1 Overview of Fluid Mechanics/22 MARKS. 1.1 Fluid Fundamentals. Content : 1.1 Fluid Fundamentals. 08 Marks Classification of Fluid, Properties of fluids like Specific Weight, Specific gravity, Surface tension, Capillarity, Viscosity. Specification of hydraulic oil

More information

T HIS PAPER deals with the design and performance of an

T HIS PAPER deals with the design and performance of an T he D esign and P erform ance of an A xial-flow Fan LIONEL S. MARKS1 a n d JOHN R. W ESKE,2 CAMBRIDGE, MASS. T h is p ap er d ea ls w ith th e d e s ig n a n d p e r fo r m a n c e o f a n a xia l-flo

More information

Hydraulics. B.E. (Civil), Year/Part: II/II. Tutorial solutions: Pipe flow. Tutorial 1

Hydraulics. B.E. (Civil), Year/Part: II/II. Tutorial solutions: Pipe flow. Tutorial 1 Hydraulics B.E. (Civil), Year/Part: II/II Tutorial solutions: Pipe flow Tutorial 1 -by Dr. K.N. Dulal Laminar flow 1. A pipe 200mm in diameter and 20km long conveys oil of density 900 kg/m 3 and viscosity

More information

OPEN QUIZ WHEN TOLD AT 7:00 PM

OPEN QUIZ WHEN TOLD AT 7:00 PM 2.25 ADVANCED FLUID MECHANICS Fall 2013 QUIZ 1 THURSDAY, October 10th, 7:00-9:00 P.M. OPEN QUIZ WHEN TOLD AT 7:00 PM THERE ARE TWO PROBLEMS OF EQUAL WEIGHT Please answer each question in DIFFERENT books

More information

Predictionof discharge coefficient of Venturimeter at low Reynolds numbers by analytical and CFD Method

Predictionof discharge coefficient of Venturimeter at low Reynolds numbers by analytical and CFD Method International Journal of Engineering and Technical Research (IJETR) ISSN: 2321-0869, Volume-3, Issue-5, May 2015 Predictionof discharge coefficient of Venturimeter at low Reynolds numbers by analytical

More information

The Aerodynamics of the Inlet of Centrifugal Compressor

The Aerodynamics of the Inlet of Centrifugal Compressor Purdue University Purdue e-pubs International Compressor Engineering Conference School of Mechanical Engineering 1998 The Aerodynamics of the Inlet of Centrifugal Compressor J. Mulugeta York International

More information

CFD Analysis of Forced Convection Flow and Heat Transfer in Semi-Circular Cross-Sectioned Micro-Channel

CFD Analysis of Forced Convection Flow and Heat Transfer in Semi-Circular Cross-Sectioned Micro-Channel CFD Analysis of Forced Convection Flow and Heat Transfer in Semi-Circular Cross-Sectioned Micro-Channel *1 Hüseyin Kaya, 2 Kamil Arslan 1 Bartın University, Mechanical Engineering Department, Bartın, Turkey

More information

Reynolds, an engineering professor in early 1880 demonstrated two different types of flow through an experiment:

Reynolds, an engineering professor in early 1880 demonstrated two different types of flow through an experiment: 7 STEADY FLOW IN PIPES 7.1 Reynolds Number Reynolds, an engineering professor in early 1880 demonstrated two different types of flow through an experiment: Laminar flow Turbulent flow Reynolds apparatus

More information

Chapter -5(Section-1) Friction in Solids and Liquids

Chapter -5(Section-1) Friction in Solids and Liquids Chapter -5(Section-1) Friction in Solids and Liquids Que 1: Define friction. What are its causes? Ans : Friction:- When two bodies are in contact with each other and if one body is made to move then the

More information

NORTH SEA FLOW MEASUREMENT WORKSHOP 2004 In. St Andrews, Scotland

NORTH SEA FLOW MEASUREMENT WORKSHOP 2004 In. St Andrews, Scotland NORTH SEA FLOW MEASUREMENT WORKSHOP 2004 In St Andrews, Scotland From the 26 th to 28 th October, 2004 Tests of the V-Cone Flow Meter at Southwest Research Institute and Utah State University in Accordance

More information

Study on the Performance of a Sirocco Fan (Flow Around the Runner Blade)

Study on the Performance of a Sirocco Fan (Flow Around the Runner Blade) Rotating Machinery, 10(5): 415 424, 2004 Copyright c Taylor & Francis Inc. ISSN: 1023-621X print / 1542-3034 online DOI: 10.1080/10236210490474629 Study on the Performance of a Sirocco Fan (Flow Around

More information

Chapter 3 Bernoulli Equation

Chapter 3 Bernoulli Equation 1 Bernoulli Equation 3.1 Flow Patterns: Streamlines, Pathlines, Streaklines 1) A streamline, is a line that is everywhere tangent to the velocity vector at a given instant. Examples of streamlines around

More information

Experimental Investigation on the Influence of Density of Fluid. On Efficiency of V- Notch

Experimental Investigation on the Influence of Density of Fluid. On Efficiency of V- Notch International Journal of Advances in Scientific Research and Engineering (ijasre) E-ISSN : 2454-8006 DOI: http://dx.doi.org/10.7324/ijasre.2017.32515 Vol.3 (9) Oct - 2017 Experimental Investigation on

More information

Chapter (6) Energy Equation and Its Applications

Chapter (6) Energy Equation and Its Applications Chapter (6) Energy Equation and Its Applications Bernoulli Equation Bernoulli equation is one of the most useful equations in fluid mechanics and hydraulics. And it s a statement of the principle of conservation

More information

UNIT II Real fluids. FMM / KRG / MECH / NPRCET Page 78. Laminar and turbulent flow

UNIT II Real fluids. FMM / KRG / MECH / NPRCET Page 78. Laminar and turbulent flow UNIT II Real fluids The flow of real fluids exhibits viscous effect that is they tend to "stick" to solid surfaces and have stresses within their body. You might remember from earlier in the course Newtons

More information

ORIFICE COEFFICIENTS DATA AND RESULTS OF TESTS

ORIFICE COEFFICIENTS DATA AND RESULTS OF TESTS N o. 1870 ORIFICE COEFFICIENTS DATA AND RESULTS OF TESTS B y J a c o b M. S p itz g la s s, C h ic a g o, III. Member of the Society This paper discusses the results of experimental work conducted at the

More information