Adhesive Force due to a Thin Liquid Film between Two Smooth Surfaces (Wringing Mechanism of Gage Blocks)

Size: px
Start display at page:

Download "Adhesive Force due to a Thin Liquid Film between Two Smooth Surfaces (Wringing Mechanism of Gage Blocks)"

Transcription

1 Journal of JSEM, Vol.14, Special Issue (014) s36-s41 Copyright C 014 JSEM Adhesive Force due to a Thin Liquid Film between Two Smooth Surfaces (Wringing Mechanism of Gage Blocks) Kenji KATOH 1 and Tatsuro WAKIMOTO 1 1 Department of Mechanical Engineering, Osaka City University, Osaka , Japan (Received 9 January 014; received in revised form 8 April 014; accepted 7 June 014) Abstract It is well known as the wringing phenomenon of gage blocks that a strong adhesive force appears between two smooth surfaces when a thin liquid film is applied on the interface. A theoretical and experimental study is conducted to discuss the wringing mechanism. The liquid film may be separated into a large number of small puddles when two surfaces are rubbed together. One can expect a large adhesive force due to the resultant of surface tension acting on the circumference of each puddle. Numerical results for oil distribution between two surfaces show that the total perimeter length of liquid film reaches m on the surface of 3cm, which leads to (N/m ) for the adhesive force. The adhesive forces measured experimentally roughly agree with the theoretical value. A simple model is proposed to explain the adhesive force dependence on the velocity of pulling apart two surfaces. Key words Surface Tension, Gage Blocks, Wringing Phenomenon, Surface Roughness, Viscosity 1. Introduction It is well known that a strong adhesive force appears between two smooth solid surfaces when a thin liquid film is applied on the interface. This phenomenon is usually applied to the wringing of gage blocks used in precise measurement of linear dimension [1]. The roughness of gage blocks is typically order of 0.01μm and it is very important for gage blocks to be wrung without length uncertainty. In the actual system, the adhesive force reaches several times as large as atmospheric pressure when two surfaces are rubbed together to spread the oil uniformly as a thin film between them. Many authors have been trying to explain the wringing mechanism from the intermolecular force or the viscous force of the oil film [- 9]. Based on the order of roughness and of oil film thickness, the intermolecular force should not be related to the wringing mechanism. Mainly the influences of surface tension or viscous force have been considered. However, the wringing of gage blocks has not been treated since 1980 s, although the mechanism why such a large adhesive force is generated is still an open problem The authors had proposed a theoretical model for the wringing mechanism based on the surface tension acting on the oil film distributed on the contact surface [10]. In this report, the surface characteristics of gage blocks are observed by a STM (Scanning Tunneling Microscope). Then the state of solid contact and the distribution of oil film are numerically simulated between two surfaces having statistically equivalent roughness to the observed gage block surfaces. Using the simulated results, the adhesive force is estimated based on the model proposed in the preceding report. The adhesive forces are measured experimentally for several kinds of liquids with different viscosities, and the validity of the theoretical model is examined through the comparison with the measured results. In addition, the effect of viscous force on the wringing mechanism is discussed from a simple theoretical consideration.. Theoretical Model of Adhesive Force due to Surface Tension In this section, a brief explanation is given to describe the theoretical model for the adhesive force in the preceding report [10]. The surface area of actual gage block is about 3cm and its roughness and flatness are less than 0.1μm. When two gage blocks are adhered to each other, the resulted linear length should exactly be the sum of two gage blocks with the deviation less than the roughness stated above [, 3]. The number of contact points and the real contact area between two gage blocks should be much larger than those observed in contacts between usual surfaces. Figures 1(a) and 1(b) schematically show the states of contacts between usual rough surfaces and between gage blocks, respectively. The vacant spaces surrounded by metal contacts may be fulfilled with a liquid (a) Usual surfaces (b) Gage blocks Fig. 1 State of contact between two surfaces -s36-

2 Journal of JSEM, Vol.14, Special Issue (014) such as a thin oil film when gage blocks are wrung as shown in Fig. 1(b). When the upper surface is pulled apart from the lower surface, the gas-liquid surface tension γ appears and acts as a drag on the circumference of the oil film as shown in Fig. 1(a) or 1(b), and following adhesive force should be generated as the total drag. F L (1) where L indicates the total perimeter length around oil films. The drag F in Eq. (1) should be trivial for usual contact between rough surfaces, because the surface tension γ is at most the order of 0.03 (N/m) and the length L does not become so large. On the other hand, however, the oil films between two gage blocks may be separated into great number of small puddles bounded by many contact points, as shown in Fig. 1(b). Now let us imagine that the surface roughness is simply downsized with keeping geometric similarity. The number of oil puddles increases with minus second power of the roughness size, and the total length around the perimeters increases with minus first power. Therefore the length L in Eq. (1) may be quite large and the drag F cannot be neglected. In the preceding report, the length L is estimated from a simple consideration based on the characteristics of gage block surface observed by a SEM [10]. The result showed that the length L may be order of 5000m on the gage block surface of 3cm and the adhesive force estimated from Eq. (1) reaches F~ (N/m ). This is about five times as large as the atmospheric pressure and is the same order as experienced in the practical system. 3. Distribution of Oil Films and Correct Estimation of Adhesive Force The estimations of L and F in the preceding report were not rigorous, because they were calculated based on a rough estimation for the statistics of roughness on the surface. In this report, in order to discuss the validity of the theoretical model of Eq. (1), first the surface of gage blocks is precisely observed by using a STM. Then the state of contact is numerically simulated between two surfaces with statistically equivalent surface characteristics to gage blocks. From the calculation of the total perimeter length L, the adhesive force in Eq. (1) is estimated precisely. 3.1 Characteristics of gage block surface Figure show examples of measured roughness curves on gage blocks obtained by STM. Figures (a) and (b) correspond to the roughness curves measured in longitudinal (x) and in transverse (y) direction on the rectangular surface, respectively. Although the statistical characteristics are almost similar to each other, a slight directional dependence can be observed. The standard deviation calculated from Fig. is about 5nm and it was confirmed that the probability distribution of roughness heights can be approximated by usual Gaussian profile. 3. Estimation of total perimeter length and adhesive force The roughness curves like Fig. were measured at 10 different positions on the gage block surface and the power spectrum was analyzed. Figures 3(a) and (b) show examples of measured power spectrum in x and y direction, (a) x-direction (a) x-direction 1 (b) y-direction Fig. Roughness curve on gage blocks surface (b) y-direction Fig. 3 Power spectrum of surface roughness on gage blocks -s37-

3 K. KATOH and T. WAKIMOTO (a) h = 0 Fig. 5 Ratio of contact area between two gage blocks surfaces Fig. 6 Total perimeter length of oil film on gage blocks (b) h = 5 nm Fig. 4 State of contact between two gage blocks respectively. The horizontal and longitudinal axes in the figures indicate the wave number and the power spectrum, respectively. Although the distributions of power spectrum are almost similar in both directions, the spectrum of x direction is slightly smaller than that of y direction in low wave number region, while vice versa in high wave number region. Some directional dependence may appear since the surface of gage blocks is finished by rapping. Giving random phase shift to each wave number component of averaged two-dimensional power spectrum, the gage block surface with the same statistical characteristics is simulated from the inverse Fourier transform. Then the state of contact is numerically simulated between two surfaces to detect the oil film distribution. Figure 4 shows an example of simulated contact state within surface area (1 1μm). The protrusions overlapped between two surfaces may be distorted elastically and the contacted areas are depicted by black parts as shown in Fig. 4. The white parts in the figures correspond to cavities in which oil may be fulfilled. As shown in Fig. 4(a), the oil film is distributed to many puddles with complicated configuration like fractals. When two gage blocks are pulled apart, gas-liquid interface appears and surface tension acts as the drag on the perimeter of each puddle of white parts. Figures 4(a) and (b) show the results for different average distance h between two surfaces. Figure 4(a) corresponds to h=0 when the averaged heights of two rough surfaces as shown in Fig. coincide with each other and the length at the wringing is strictly equal to the sum of two gage blocks. Figure 4(b) shows the result for h=5nm. As shown in the figures, the oil film distribution is dramatically changed even when the distance is slightly increased. Figure 5 shows the calculated result for the ratio of contact area to the total surface area, p (0 p 1). The ratio p is about 0.5 at h=0 and monotonously decreases with increasing h. As suggested in the past literature [8], the ratio of contact area is quite large as compared with (0.001~0.1) for the contact between usual surfaces. Figure 6 shows the perimeter length of oil films L varying with h. The length L can be calculated from the sum of the perimeters around the white parts as shown in Fig. 4. As expected, L becomes maximum for h=0 at which the contact area is about 0.5 as shown in Fig. 5. The perimeter length gradually decreases in proportion to -1 power of h and becomes one third as large as the maximum at h=10nm. As shown in Fig. 6, the perimeter length L reaches about m/m at h=0, corresponding to L 10500m on gage blocks of 3cm area, which is comparable to the rough estimation in the preceding report [10]. The adhesive force of Eq. (1) is then estimated as F= (N/m ) (i.e., about 10 times as large as the atmospheric pressure) for -s38-

4 Journal of JSEM, Vol.14, Special Issue (014) usual oils having γ 0.03 (N/m). It is noted that all spaces of white area shown in Fig. 4 may not be necessarily fulfilled with oil and the oil film may be distributed heterogeneously over the gage block surface. Hence the adhesive force in the actual system should be somewhat smaller than that estimated above. 3.3 Effect of viscosity In the above discussion, we have considered the effect of surface tension on the wringing force when two gage blocks are pulled apart. On the other hand, Bowden and Tabor [5] proposed the adhesive force due to viscosity F µ (N/m ) expressed as the following relation. F 3 µ d 1 µ = 3 µ d V = () 8 t 8 3 H H where d and H indicate the equivalent diameter of contact surface and the oil film thickness, respectively. μ is the viscosity of oil. t and V in the above equation are the time necessary to separate the two surfaces and the velocity of pulling apart two gage blocks, respectively. The theoretical model of Bowden and Tabor assumed that the oil film of uniform thickness H is distributed on the circular surface with diameter d. When two gage blocks are pulled apart, the oil flows toward the center of the circular surface and the pressure gradient is generated in the oil film to counterbalance the viscous drag. The adhesive force represented by Eq. () can be estimated from the integration of negative pressure on the wall surface by using the approximate solution of wedge flow equation. Some authors expected a quite large adhesive force from Eq. () such as several times as great as the atmospheric pressure for d=cm circular surface equivalent to gage block surface (i.e., 3cm ), if the film thickness is assumed as H=0~50nm, referring to the measured results [, 3]. However, it is apparent that the adhesive force of Eq. () must not exceed the atmospheric pressure because the model is originally based on the negative pressure on the wall. In other words, it is not meaningful to imagine the oil flow larger than that generated by the maximum pressure difference (i.e., atmospheric pressure). If the oil is distributed homogeneously over the gage blocks surface as a very thin film, the pressure gradient could not drive the flow against large viscous drag. In the actual system, however, the oil film may be separated into many small puddles as shown in Fig. 4. In such a case, a large pressure gradient may be possible in each puddle to drive the thin film. Here the order of viscous drag is estimated in a simple manner when the oil flows in each small puddle. Assuming i as the number of oil puddles (thickness H) per unit area and (1 p) as the ratio of occupied area by all puddles, the equivalent diameter of a 4 ( 1 p) small puddle can be estimated as d~. The total πi viscous drag can be obtained from the sum of Eq. () over whole puddles as: 3 μd 1 3 μ( 1 p) 1 3 μ( 1 p ) V F µ ~ i = = (3) 8 t it 3 H π H πih Fig. 7 Number of oil puddles on gage block surface As is clear from the above equation, the viscous drag should be negligible when the number i becomes quite large. Figure 7 shows the calculated results of the number of oil puddles (i.e., number of white parts shown in Fig. 4). As shown in the figure, the number of oil puddles per unit area reaches about when the average distance between two gage blocks surfaces is zero. Now let us estimate the viscous drag from Eq. (3). We assume here that the average oil film thickness is about H=0nm as stated before, p=0.5 from Fig. 5, and t=1s for the typical time to be separated. Then the viscous drag is estimated as F µ 1.3(N/m ) from Eq. (3) for the machine oil having viscosity μ =0.17 (Pa s). Even if one considers the separating velocity as V=10mm/min referring to the experimental results shown in section 4, the viscous drag calculated from the right hand side in Eq. (3) is F µ (N/m ), which is still quite small compared with the atmospheric pressure or the drag of surface tension. Other than Eq. (3), we may consider the viscous stress produced from the vertical flow of velocity V, when two surfaces are pulled apart. The viscous force per unit area can be estimated simply from the viscous stress tensor as: V Fµ~ µ ( 1 p) (4) H Inserting each value stated above into Eq. (4), F µ ~ (N/m ) is obtained. This is again quite small compared with the atmospheric pressure. From these results, the adhesive force due to viscosity should not exceed the atmospheric pressure and we can neglect the effect of viscosity on the wringing phenomenon. 4. Experimental Results and Discussion The wringing force between two gage blocks were actually measured by a usual tensile testing machine for three kinds of oils, in order to examine the validity of the theoretical model in the preceding section. The velocity of separating two gage blocks was widely changed from 0.05 to 1mm/min. Table 1 shows the physical properties for Table 1 Physical properties of test liquids (0 C) Surface tension (N/m) Viscosity (Pa s) Spindle oil Machine oil Chainsaw oil s39-

5 K. KATOH and T. WAKIMOTO test oils used in this experiment. As shown in the table, the surface tension is almost similar to each other, while the viscosity is varied more than 1000% among three kinds of oils. The measurement of adhesive force was repeated more than 0 times for each experimental condition and the average was calculated. Figure 8 shows the measured adhesive forces F (N/m ) for three kinds of oils at 0 C. The horizontal axis indicates the pulling velocity V. When the gage blocks are adhered, only a minute amount of oil is necessary. Since the adhesive force could be sensibly dependent on the oil film distribution, it may scatter greatly at each measurement. The standard deviation of measured adhesive force is (N/m ) (16% of average adhesive force) in this experiment. As shown in Fig. 8, the adhesive forces are not so different between three kinds of oils, in spite of large variance of viscosity. The influence of viscosity on the adhesive force can be neglected as expected in the preceding section. Although some literatures suggested that the adhesive force varies dependent on the viscosity of test liquids, the wettability between oil and solid surface should be more important. The contact angles of three kinds of oils on the gage blocks surface were measured by the contact angle meter (Kyowa Kaimen Kagaku Co. Ltd., CA-A type). The receding contact angles are 0 for all oils and the advancing contact angles range from 15 to 5. The oils used in this experiment can wet well the surface of gage blocks and the oil film may be distributed uniformly on the surface. Hence the surface tension has the most important effect on the wringing mechanism of gage blocks, if usual oils are used as in this experiment. The solid curve drawn in Fig. 8 indicates the calculated result of Eq. (1) in which the surface tension averaged between three kinds of oils is used. The theoretical result is somewhat larger than the experimental results. This is because the calculated adhesive force is obtained from the total perimeter length of all oil puddles. As stated in section 3, all puddles are not necessarily filled with the oils and the total surface tension should be smaller than that expected in the theoretical curve shown in the figure. The experimental results shown in Fig. 8 increase with V and finally approach a critical value. This tendency suggests that the oil film distribution, i.e., the configuration of liquid surface as shown in Fig. 1, may change dependent on the velocity to separate two gage blocks. Figures 9 and 10 show some models of oil behavior in a puddle when Fig. 8 Measured adhesive force between gage blocks (a) Plain view (b) Vertical view Fig. 9 Oil behavior in space between gage block surfaces (low velocity of pulling apart) (a) Plain view (b) Vertical view Fig. 10 Oil behavior in space between gage blocks surfaces (high velocity of pulling apart) gage blocks are pulled apart. The plain and vertical views are drawn in each figure. Figure 9 corresponds to the case when the velocity V is not large. As shown in the figure, the oil can follow the expansion of the puddle by the retreat of solid contact as shown by arrows in the plain and vertical view. Then the liquid surface appears in the middle of the oil film as shown in the vertical view. On the other hand, when the velocity is quite large as shown in Fig. 10, the oil cannot follow the quick expansion of the puddle. In this case, the liquid surface appears close to the contact area as shown in the figure. If one compares the perimeter length between Fig. 9 and Fig. 10, the perimeter of Fig. 10 -s40-

6 Journal of JSEM, Vol.14, Special Issue (014) is apparently larger. The model of Fig. 10 corresponds to the theoretical model drawn by the solid line in Fig. 8. Now let us estimate the adhesive force for the oil film shown in Fig. 9. The profile of perimeter shown in the vertical view is assumed as a circle having the same area as the original oil puddle shown in the plain view. The average surface area was calculated for all the oil puddles as shown by white parts in Fig. 4 and the equivalent diameter was obtained. The perimeter length is calculated as πd of the circle (d: diameter). The adhesive force is calculated from the total perimeter length multiplied by surface tension and the result is drawn by the broken line in Fig. 8. As shown in the figure, the experimental results in this paper distribute between the solid line corresponding to the model of Fig. 10 and the broken line. As the velocity V becomes large, the oil in a small puddle still can follow the expansion, while the oil in a large puddle cannot follow the movement. Hence the number of puddles in which the oil behaves like Fig. 10 increases with V and the adhesive force may approach the solid line as shown in Fig. 8. The above model is rather simple and the oil would behave more complicatedly in the actual system. The actual behavior of oil between two surfaces should be observed experimentally to ensure the validity of the theoretical model proposed here. However, the proposed model can explain the mechanism how such large adhesive force appears and the actual behavior of adhesive force dependent on the velocity of pulling apart, which cannot be explained by other models discussed in the literatures. 5. Conclusion The total perimeter length of oil film L on the interface between two gage blocks was estimated from the numerical simulation for contact problem between two surfaces with equivalent statistical characteristics. When two gage blocks are adhered, the oil film is separated into large number of small puddles. The numerical simulation shows that the length may reach L=10500m on 3cm surface. The product of surface tension and L can explain the adhesive force experienced in the actual system. The viscous force was estimated from the fluid dynamic model for the oil behavior in each small puddle. The result suggested that the influence of viscosity on the wringing phenomenon can be negligible. Actually almost the same adhesive force is observed experimentally for three kinds of oils among which the viscosity varies more than 1000%. The measured adhesive force increases with the separating velocity and approaches a constant value. A rather simple theoretical model was proposed based on the behavior of oil film in the puddle. As the velocity increases, the gas-liquid interface is more likely to be generated near the solid contacts since the liquid in the puddle cannot follow the movement. In such a case, the perimeter configuration becomes more complicated and the adhesive increases due to large gas-liquid interface length. The model can explain the tendency observed experimentally. Nomenclature d diameter of oil puddle [m] F adhesive force per unit area [N/m ] H oil film thickness [m] h distance between gage blocks [m] i number of oil puddles L total perimeter length [m] p ratio of solid contact area t time necessary to pull apart gage blocks [s] V velocity of pulling apart gage blocks [mm/s] density [kg/m 3 ] γ surface tension [N/m] μ viscosity [Pa s] References [1] Titov, A., Malinovsky, I., Belaidi, H., Franca, R. S. and Massone, C. A.: Precise Interferometric Length and Phase-change Measurement of Gauge Blocks Based on Reproducible Wringing, Applied Optics, 39-4 (000), [] Tsugami, K.: Block Gauges (in Japanese), The Nikkan Kogyo Shimbun, Ltd. (196), [3] Tsumura, K. and Fujii, K.: Cohesive Force of Block Gauges: Study on Wringing Force of Block Gauges (Report 1) (in Japanese), Journal of the Japan Society of Precision Engineering,37-7 (1971), [4] Fujii, K. and Tsumura, K.: Estimation of Wringing of Block Gages (in Japanese), Journal of Japan Society of Lubrication Engineers, 17-8 (197), [5] Bowden, E.P. and Tabor, D.: Friction and Lubrication of Solids, Clarendon Press Oxford (1954), [6] Budgett, H. M.: The Adherence of Flat Surfaces, Proc. Royal Soc. London (Ser. A), 86 (191), [7] Rolt, F. H. and Barrell, H.: Contact of Flat Surfaces, Proc. Royal Soc. London (Ser. A), 116 (197), [8] Kato, T. and Sakurai, Y.: Measurement of Real Contact Area of Wrung Gauge Block and Effect of the Area on Wringing Force (in Japanese), Journal of the Japan Society of Precision Engineering, 43-8 (1977), [9] Kato, T.: Effect of the Surface Integrity on the Wringing Force (in Japanese), Journal of the Japan Society of Precision Engineering, 48-3 (198), [10] Katoh, K. and Tsutsumi, S.: Consideration of Wringing mechanism of Gage Blocks (in Japanese), Transactions of the Japan Society of mechanical Engineers, Series C, (199), s41-

Lecture 6 Friction. Friction Phenomena Types of Friction

Lecture 6 Friction. Friction Phenomena Types of Friction Lecture 6 Friction Tangential forces generated between contacting surfaces are called friction forces and occur to some degree in the interaction between all real surfaces. whenever a tendency exists for

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

Chapter -6(Section-1) Surface Tension

Chapter -6(Section-1) Surface Tension Chapter -6(Section-1) Surface Tension Free surface of the liquid tends to minimize the surface area. e.g.(1)if the small quantity of mercury is allowed to fall on the floor, it converted in to small spherical

More information

Hydroplaning Simulation using MSC.Dytran

Hydroplaning Simulation using MSC.Dytran Hydroplaning Simulation using MSC.Dytran Toshihiko Okano * & Masataka Koishi * THE YOKOHAMA RUBBER CO., LTD 2-1 Oiwake Hiratsuka Kanagawa 254-8601, Japan ABSTRACT Hydroplaning characteristics is one of

More information

ISCST shall not be responsible for statements or opinions contained in papers or printed in its publications.

ISCST shall not be responsible for statements or opinions contained in papers or printed in its publications. Modeling of Drop Motion on Solid Surfaces with Wettability Gradients J. B. McLaughlin, Sp. S. Saravanan, N. Moumen, and R. S. Subramanian Department of Chemical Engineering Clarkson University Potsdam,

More information

Introduction to Marine Hydrodynamics

Introduction to Marine Hydrodynamics 1896 1920 1987 2006 Introduction to Marine Hydrodynamics (NA235) Department of Naval Architecture and Ocean Engineering School of Naval Architecture, Ocean & Civil Engineering First Assignment The first

More information

LIQUID FILM THICKNESS OF OSCILLATING FLOW IN A MICRO TUBE

LIQUID FILM THICKNESS OF OSCILLATING FLOW IN A MICRO TUBE Proceedings of the ASME/JSME 2011 8th Thermal Engineering Joint Conference AJTEC2011 March 13-17, 2011, Honolulu, Hawaii, USA AJTEC2011-44190 LIQUID FILM THICKNESS OF OSCILLATING FLOW IN A MICRO TUBE Youngbae

More information

PHYSICS OF FLUID SPREADING ON ROUGH SURFACES

PHYSICS OF FLUID SPREADING ON ROUGH SURFACES INTERNATIONAL JOURNAL OF NUMERICAL ANALYSIS AND MODELING Volume 5, Supp, Pages 85 92 c 2008 Institute for Scientific Computing and Information PHYSICS OF FLUID SPREADING ON ROUGH SURFACES K. M. HAY AND

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

Chapter 10. Solids and Fluids

Chapter 10. Solids and Fluids Chapter 10 Solids and Fluids Surface Tension Net force on molecule A is zero Pulled equally in all directions Net force on B is not zero No molecules above to act on it Pulled toward the center of the

More information

Name per due date mail box. Friction Lab. Challenge - move your wooden block from start to finish with the least amount of force.

Name per due date mail box. Friction Lab. Challenge - move your wooden block from start to finish with the least amount of force. Name per due date mail box Friction Lab Challenge - move your wooden block from start to finish with the least amount of force. Procedure - 1. Make sure your spring scale pointer is zeroed - if not see

More information

Lubrication and Journal Bearings

Lubrication and Journal Bearings UNIVERSITY OF HAIL College of Engineering Department of Mechanical Engineering Chapter 12 Lubrication and Journal Bearings Text Book : Mechanical Engineering Design, 9th Edition Dr. Badreddine AYADI 2016

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

WRINGING DEFORMATION AND ROUGHNESS ASPECTS IN OPTICAL LENGTH MEASUREMENTS

WRINGING DEFORMATION AND ROUGHNESS ASPECTS IN OPTICAL LENGTH MEASUREMENTS XVII IMEKO World Congress Metrology in the 3 rd Millennium June 22 27, 2003, Dubrovnik, Croatia WRINGING DEFORMATION AND ROUGHNESS ASPECTS IN OPTICAL LENGTH MEASUREMENTS A. Titov*, I. Malinovsky*, C.A.

More information

Fluid Mechanics Abdusselam Altunkaynak

Fluid Mechanics Abdusselam Altunkaynak Fluid Mechanics Abdusselam Altunkaynak 1. Unit systems 1.1 Introduction Natural events are independent on units. The unit to be used in a certain variable is related to the advantage that we get from it.

More information

Evaluation of in-plane orthotropic elastic constants of paper and paperboard

Evaluation of in-plane orthotropic elastic constants of paper and paperboard Evaluation of in-plane orthotropic elastic constants of paper and paperboard T. Yokoyama and K. Nakai Department of Mechanical Engineering, Okayama University of Science - Ridai-cho, Okayama 7-5, Japan

More information

SHAKING TABLE TEST FOR FRICTIONAL ISOLATED BRIDGES AND TRIBOLOGICAL NUMERICAL MODEL OF FRICTIONAL ISOLATOR

SHAKING TABLE TEST FOR FRICTIONAL ISOLATED BRIDGES AND TRIBOLOGICAL NUMERICAL MODEL OF FRICTIONAL ISOLATOR 13 th World Conference on Earthquake Engineering Vancouver, B.C., Canada August 1-6, 2004 Paper No. 1531 SHAKING TABLE TEST FOR FRICTIONAL ISOLATED BRIDGES AND TRIBOLOGICAL NUMERICAL MODEL OF FRICTIONAL

More information

SECONDARY MOTION IN TURBULENT FLOWS OVER SUPERHYDROPHOBIC SURFACES

SECONDARY MOTION IN TURBULENT FLOWS OVER SUPERHYDROPHOBIC SURFACES SECONDARY MOTION IN TURBULENT FLOWS OVER SUPERHYDROPHOBIC SURFACES Yosuke Hasegawa Institute of Industrial Science The University of Tokyo Komaba 4-6-1, Meguro-ku, Tokyo 153-8505, Japan ysk@iis.u-tokyo.ac.jp

More information

Supplementary Information on Thermally Enhanced Self-Propelled Droplet Motion on Gradient Surfaces

Supplementary Information on Thermally Enhanced Self-Propelled Droplet Motion on Gradient Surfaces Electronic Supplementary Material (ESI) for RSC Advances. This journal is The Royal Society of Chemistry 2015 Supplementary Information on Thermally Enhanced Self-Propelled Droplet Motion on Gradient Surfaces

More information

Particle resuspension

Particle resuspension 86 Chapter 6 Particle resuspension 6.1 Motivation In previous chapters, the relative effective viscosity of a flow with particles denser than the interstitial liquid was discussed. Such results show that

More information

Petroleum Engineering Department Fluid Mechanics Second Stage Assist Prof. Dr. Ahmed K. Alshara

Petroleum Engineering Department Fluid Mechanics Second Stage Assist Prof. Dr. Ahmed K. Alshara Continents Petroleum Engineering Department Fluid Mechanics Second Stage Assist Prof. Dr. Ahmed K. Alshara Chapter 1. Fluid Mechanics -Properties of fluids -Density, specific gravity, specific volume and

More information

Petroleum Engineering Dept. Fluid Mechanics Second Stage Dr. Ahmed K. Alshara

Petroleum Engineering Dept. Fluid Mechanics Second Stage Dr. Ahmed K. Alshara Continents Chapter 1. Fluid Mechanics -Properties of fluids -Density, specific gravity, specific volume and Viscosity -Newtonian and non Newtonian fluids -Surface tension Compressibility -Pressure -Cavitations

More information

AN EXPERIMENTAL INVESTIGATION OF BOILING HEAT CONVECTION WITH RADIAL FLOW IN A FRACTURE

AN EXPERIMENTAL INVESTIGATION OF BOILING HEAT CONVECTION WITH RADIAL FLOW IN A FRACTURE PROCEEDINGS, Twenty-Fourth Workshop on Geothermal Reservoir Engineering Stanford University, Stanford, California, January 25-27, 1999 SGP-TR-162 AN EXPERIMENTAL INVESTIGATION OF BOILING HEAT CONVECTION

More information

CHAPTER 1 Fluids and their Properties

CHAPTER 1 Fluids and their Properties FLUID MECHANICS Gaza CHAPTER 1 Fluids and their Properties Dr. Khalil Mahmoud ALASTAL Objectives of this Chapter: Define the nature of a fluid. Show where fluid mechanics concepts are common with those

More information

Observation of Falling Motion of Columnar Snow Crystals

Observation of Falling Motion of Columnar Snow Crystals 276 Journal of the Meteorological Society of Japan Vol. 54, No. 5 Observation of Falling Motion of Columnar Snow Crystals By Masahiro Kajikawa Department of Earth Science, Akita University, Akita, Japan

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

Optical Measurements of Cavitation in Tribological Contacts

Optical Measurements of Cavitation in Tribological Contacts Journal of Physics: Conference Series PAPER OPEN ACCESS Optical Measurements of Cavitation in Tribological Contacts To cite this article: Tian Tang et al 2015 J. Phys.: Conf. Ser. 656 012119 View the article

More information

University of Bath. Publication date: Document Version Early version, also known as pre-print. Link to publication

University of Bath. Publication date: Document Version Early version, also known as pre-print. Link to publication Citation for published version: Evans, M, Akehurst, S & Keogh, P 2014, 'Wear mechanisms in polyoxymethylene (POM) spur gears' Paper presented at 5th World Tribology Congress, WTC 2013, Torino, UK United

More information

BFC FLUID MECHANICS BFC NOOR ALIZA AHMAD

BFC FLUID MECHANICS BFC NOOR ALIZA AHMAD BFC 10403 FLUID MECHANICS CHAPTER 1.0: Principles of Fluid 1.1 Introduction to Fluid Mechanics 1.2 Thermodynamic Properties of a Fluid: Density, specific weight, specific gravity, viscocity (kelikatan)berat

More information

The Morton Effect. Synchronous (1X) vibration is typically present on all types of rotating machinery. Common causes or

The Morton Effect. Synchronous (1X) vibration is typically present on all types of rotating machinery. Common causes or The Morton Effect and Light Rubs in Rotating Machinery Synchronous (1X) vibration is typically present on all types of rotating machinery. Common causes or sources of this vibration component include mass

More information

MECHANICAL PROPERTIES OF FLUIDS:

MECHANICAL PROPERTIES OF FLUIDS: Important Definitions: MECHANICAL PROPERTIES OF FLUIDS: Fluid: A substance that can flow is called Fluid Both liquids and gases are fluids Pressure: The normal force acting per unit area of a surface is

More information

MM303 FLUID MECHANICS I PROBLEM SET 1 (CHAPTER 2) FALL v=by 2 =-6 (1/2) 2 = -3/2 m/s

MM303 FLUID MECHANICS I PROBLEM SET 1 (CHAPTER 2) FALL v=by 2 =-6 (1/2) 2 = -3/2 m/s MM303 FLUID MECHANICS I PROBLEM SET 1 (CHAPTER ) FALL 018 1) For the velocity fields given below, determine: i) Whether the flow field is one-, two-, or three-dimensional, and why. ii) Whether the flow

More information

Fluid Flow and Heat Transfer of Combined Forced-Natural Convection around Vertical Plate Placed in Vertical Downward Flow of Water

Fluid Flow and Heat Transfer of Combined Forced-Natural Convection around Vertical Plate Placed in Vertical Downward Flow of Water Advanced Experimental Mechanics, Vol.2 (2017), 41-46 Copyright C 2017 JSEM Fluid Flow and Heat Transfer of Combined Forced-Natural Convection around Vertical Plate Placed in Vertical Downward Flow of Water

More information

Slow viscous flow in a microchannel with similar and different superhydrophobic walls

Slow viscous flow in a microchannel with similar and different superhydrophobic walls Journal of Physics: Conference Series PAPER OPEN ACCESS Slow viscous flow in a microchannel with similar and different superhydrophobic walls To cite this article: A I Ageev and A N Osiptsov 2018 J. Phys.:

More information

Boundary Conditions in Fluid Mechanics

Boundary Conditions in Fluid Mechanics Boundary Conditions in Fluid Mechanics R. Shankar Subramanian Department of Chemical and Biomolecular Engineering Clarkson University The governing equations for the velocity and pressure fields are partial

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

AMME2261: Fluid Mechanics 1 Course Notes

AMME2261: Fluid Mechanics 1 Course Notes Module 1 Introduction and Fluid Properties Introduction Matter can be one of two states: solid or fluid. A fluid is a substance that deforms continuously under the application of a shear stress, no matter

More information

CENG 501 Examination Problem: Estimation of Viscosity with a Falling - Cylinder Viscometer

CENG 501 Examination Problem: Estimation of Viscosity with a Falling - Cylinder Viscometer CENG 501 Examination Problem: Estimation of Viscosity with a Falling - Cylinder Viscometer You are assigned to design a fallingcylinder viscometer to measure the viscosity of Newtonian liquids. A schematic

More information

CE MECHANICS OF FLUIDS UNIT I

CE MECHANICS OF FLUIDS UNIT I CE 6303- MECHANICS OF FLUIDS UNIT I 1. Define specific volume of a fluid and write its unit [N/D-14][M/J-11] Volume per unit mass of a fluid is called specific volume. Unit: m3 / kg. 2. Name the devices

More information

Lesson 6 Review of fundamentals: Fluid flow

Lesson 6 Review of fundamentals: Fluid flow Lesson 6 Review of fundamentals: Fluid flow The specific objective of this lesson is to conduct a brief review of the fundamentals of fluid flow and present: A general equation for conservation of mass

More information

STRESS STRAIN AND DEFORMATION OF SOLIDS, STATES OF STRESS

STRESS STRAIN AND DEFORMATION OF SOLIDS, STATES OF STRESS 1 UNIT I STRESS STRAIN AND DEFORMATION OF SOLIDS, STATES OF STRESS 1. Define: Stress When an external force acts on a body, it undergoes deformation. At the same time the body resists deformation. The

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

Figure 3: Problem 7. (a) 0.9 m (b) 1.8 m (c) 2.7 m (d) 3.6 m

Figure 3: Problem 7. (a) 0.9 m (b) 1.8 m (c) 2.7 m (d) 3.6 m 1. For the manometer shown in figure 1, if the absolute pressure at point A is 1.013 10 5 Pa, the absolute pressure at point B is (ρ water =10 3 kg/m 3, ρ Hg =13.56 10 3 kg/m 3, ρ oil = 800kg/m 3 ): (a)

More information

Mechanism of Friction and Real Contact Area

Mechanism of Friction and Real Contact Area CONTRIBUTION Mechanism of Friction and Real Contact Area Professor Takashi YAMAMOTO Institute of Symbiotic Science and Technology, Tokyo University of Agriculture and Technology Friction is a representative

More information

STRAIN GAUGES YEDITEPE UNIVERSITY DEPARTMENT OF MECHANICAL ENGINEERING

STRAIN GAUGES YEDITEPE UNIVERSITY DEPARTMENT OF MECHANICAL ENGINEERING STRAIN GAUGES YEDITEPE UNIVERSITY DEPARTMENT OF MECHANICAL ENGINEERING 1 YEDITEPE UNIVERSITY ENGINEERING FACULTY MECHANICAL ENGINEERING LABORATORY 1. Objective: Strain Gauges Know how the change in resistance

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

Some CFD simulations for the design of the FCC ventilation system. 9/28/2015 A. Rakai EN-CV-PJ 2

Some CFD simulations for the design of the FCC ventilation system. 9/28/2015 A. Rakai EN-CV-PJ 2 Some CFD simulations for the design of the FCC ventilation system 9/28/2015 A. Rakai EN-CV-PJ 2 FCC tunnel design 9/28/2015 A. Rakai EN-CV-PJ 3 FCC: machine tunnel A 9100 m section considered for the study,

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

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

s and FE X. A. Flow measurement B. properties C. statics D. impulse, and momentum equations E. Pipe and other internal flow 7% of FE Morning Session I

s and FE X. A. Flow measurement B. properties C. statics D. impulse, and momentum equations E. Pipe and other internal flow 7% of FE Morning Session I Fundamentals of Engineering (FE) Exam General Section Steven Burian Civil & Environmental Engineering October 26, 2010 s and FE X. A. Flow measurement B. properties C. statics D. impulse, and momentum

More information

Dynamic analysis. 1. Force and stress

Dynamic analysis. 1. Force and stress Dynamic analysis 1. Force and stress Dynamics is the part of structural geology that involves energy, force, stress, and strength. It's very important to distinguish dynamic concepts from kinematic ones.

More information

of Friction in Fluids Dept. of Earth & Clim. Sci., SFSU

of Friction in Fluids Dept. of Earth & Clim. Sci., SFSU Summary. Shear is the gradient of velocity in a direction normal to the velocity. In the presence of shear, collisions among molecules in random motion tend to transfer momentum down-shear (from faster

More information

Unit 21 Couples and Resultants with Couples

Unit 21 Couples and Resultants with Couples Unit 21 Couples and Resultants with Couples Page 21-1 Couples A couple is defined as (21-5) Moment of Couple The coplanar forces F 1 and F 2 make up a couple and the coordinate axes are chosen so that

More information

MYcsvtu Notes HEAT TRANSFER BY CONVECTION

MYcsvtu Notes HEAT TRANSFER BY CONVECTION www.mycsvtunotes.in HEAT TRANSFER BY CONVECTION CONDUCTION Mechanism of heat transfer through a solid or fluid in the absence any fluid motion. CONVECTION Mechanism of heat transfer through a fluid in

More information

A multiscale framework for lubrication analysis of bearings with textured surface

A multiscale framework for lubrication analysis of bearings with textured surface A multiscale framework for lubrication analysis of bearings with textured surface *Leiming Gao 1), Gregory de Boer 2) and Rob Hewson 3) 1), 3) Aeronautics Department, Imperial College London, London, SW7

More information

Study on Mechanism of Magnetic Abrasive Finishing Process using Low - Frequency Alternating Magnetic Field Jinzhong Wu1, a, Yanhua Zou1, b

Study on Mechanism of Magnetic Abrasive Finishing Process using Low - Frequency Alternating Magnetic Field Jinzhong Wu1, a, Yanhua Zou1, b International Conference on Electromechanical Control Technology and Transportation (ICECTT 2015) Study on Mechanism of Magnetic Abrasive Finishing Process using Low - Frequency Alternating Magnetic Field

More information

Chemical and Biomolecular Engineering 150A Transport Processes Spring Semester 2017

Chemical and Biomolecular Engineering 150A Transport Processes Spring Semester 2017 Chemical and Biomolecular Engineering 150A Transport Processes Spring Semester 2017 Objective: Text: To introduce the basic concepts of fluid mechanics and heat transfer necessary for solution of engineering

More information

Fluid Mechanics. Chapter 9 Surface Resistance. Dr. Amer Khalil Ababneh

Fluid Mechanics. Chapter 9 Surface Resistance. Dr. Amer Khalil Ababneh Fluid Mechanics Chapter 9 Surface Resistance Dr. Amer Khalil Ababneh Wind tunnel used for testing flow over models. Introduction Resistances exerted by surfaces are a result of viscous stresses which create

More information

4 Results Density and specific gravity

4 Results Density and specific gravity 4 Results 4.1. Density and specific gravity Density and specific gravity of samples, from inner, outer, bottom and middle sections of the culm are presented on Table 6. Bottom SG was around 0,63 0,64 while

More information

Analytical Prediction of Particle Detachment from a Flat Surface by Turbulent Air Flows

Analytical Prediction of Particle Detachment from a Flat Surface by Turbulent Air Flows Chiang Mai J. Sci. 2011; 38(3) 503 Chiang Mai J. Sci. 2011; 38(3) : 503-507 http://it.science.cmu.ac.th/ejournal/ Short Communication Analytical Prediction of Particle Detachment from a Flat Surface by

More information

Analysis of the occurrence of natural convection in a bed of bars in vertical temperature gradient conditions

Analysis of the occurrence of natural convection in a bed of bars in vertical temperature gradient conditions archives of thermodynamics Vol. 34(2013), No. 1, 71 83 DOI: 10.2478/aoter-2013-0005 Analysis of the occurrence of natural convection in a bed of bars in vertical temperature gradient conditions RAFAŁ WYCZÓŁKOWSKI

More information

Homework #1 Solution Problem 1

Homework #1 Solution Problem 1 Homework #1 Solution Problem 1 In this problem, we are asked to consider the design of a straw by a fast-food company for a new milkshake. We need to perform a dimensionless analysis so that there is sufficient

More information

1. The Properties of Fluids

1. The Properties of Fluids 1. The Properties of Fluids [This material relates predominantly to modules ELP034, ELP035] 1.1 Fluids 1.1 Fluids 1.2 Newton s Law of Viscosity 1.3 Fluids Vs Solids 1.4 Liquids Vs Gases 1.5 Causes of viscosity

More information

Fluid flow Pressure Bernoulli Principle Surface Tension

Fluid flow Pressure Bernoulli Principle Surface Tension Lecture 9. Fluid flow Pressure Bernoulli Principle Surface Tension A v L A is the area Fluid flow Speed of a fluid in a pipe is not the same as the flow rate Relating: Fluid flow rate to Average speed

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 5. Effects of Photonic Crystal Band Gap on Rotation and Deformation of Hollow Te Rods in Triangular Lattice

Chapter 5. Effects of Photonic Crystal Band Gap on Rotation and Deformation of Hollow Te Rods in Triangular Lattice Chapter 5 Effects of Photonic Crystal Band Gap on Rotation and Deformation of Hollow Te Rods in Triangular Lattice In chapter 3 and 4, we have demonstrated that the deformed rods, rotational rods and perturbation

More information

Sliding Contact Bearings

Sliding Contact Bearings Sliding Contact Bearings Classification of Bearings 1. According to the direction of load to be supported. The bearings under this group are classified as: (a) Radial bearings (b) Thrust bearings. In radial

More information

Fluid flow Pressure Bernoulli Principle Surface Tension

Fluid flow Pressure Bernoulli Principle Surface Tension Lecture 9. Fluid flow Pressure Bernoulli Principle Surface Tension Fluid flow Speed of a fluid in a pipe is not the same as the flow rate Depends on the radius of the pipe. example: Low speed Large flow

More information

Cracking of GSO Single Crystal Induced by Thermal Stress

Cracking of GSO Single Crystal Induced by Thermal Stress Cracking of GSO Single Crystal Induced by Thermal Stress N. Miyazaki 1,T.Tamura 2, K. Yamamoto 1 Abstract: Quantitative estimation of the failure of a gadolinium orthosilicate (Gd 2 SiO 5, hereafter abbreviated

More information

Outlines. simple relations of fluid dynamics Boundary layer analysis. Important for basic understanding of convection heat transfer

Outlines. simple relations of fluid dynamics Boundary layer analysis. Important for basic understanding of convection heat transfer Forced Convection Outlines To examine the methods of calculating convection heat transfer (particularly, the ways of predicting the value of convection heat transfer coefficient, h) Convection heat transfer

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

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

Convection. forced convection when the flow is caused by external means, such as by a fan, a pump, or atmospheric winds.

Convection. forced convection when the flow is caused by external means, such as by a fan, a pump, or atmospheric winds. Convection The convection heat transfer mode is comprised of two mechanisms. In addition to energy transfer due to random molecular motion (diffusion), energy is also transferred by the bulk, or macroscopic,

More information

Fluid Mechanics Testbank By David Admiraal

Fluid Mechanics Testbank By David Admiraal Fluid Mechanics Testbank By David Admiraal This testbank was created for an introductory fluid mechanics class. The primary intentions of the testbank are to help students improve their performance on

More information

Design of a fastener based on negative Poisson's ratio foam adapted from

Design of a fastener based on negative Poisson's ratio foam adapted from 1 Design of a fastener based on negative Poisson's ratio foam adapted from Choi, J. B. and Lakes, R. S., "Design of a fastener based on negative Poisson's ratio foam", Cellular Polymers, 10, 205-212 (1991).

More information

Everybody remains in a state of rest or continues to move in a uniform motion, in a straight line, unless acting on by an external force.

Everybody remains in a state of rest or continues to move in a uniform motion, in a straight line, unless acting on by an external force. NEWTON S LAWS OF MOTION Newton s First Law Everybody remains in a state of rest or continues to move in a uniform motion, in a straight line, unless acting on by an external force. Inertia (Newton s 1

More information

ENGR Heat Transfer II

ENGR Heat Transfer II ENGR 7901 - Heat Transfer II External Flows 1 Introduction In this chapter we will consider several fundamental flows, namely: the flat plate, the cylinder, the sphere, several other body shapes, and banks

More information

INSTITUTE OF AERONAUTICAL ENGINEERING Dundigal, Hyderabad AERONAUTICAL ENGINEERING QUESTION BANK : AERONAUTICAL ENGINEERING.

INSTITUTE OF AERONAUTICAL ENGINEERING Dundigal, Hyderabad AERONAUTICAL ENGINEERING QUESTION BANK : AERONAUTICAL ENGINEERING. Course Name Course Code Class Branch INSTITUTE OF AERONAUTICAL ENGINEERING Dundigal, Hyderabad - 00 0 AERONAUTICAL ENGINEERING : Mechanics of Fluids : A00 : II-I- B. Tech Year : 0 0 Course Coordinator

More information

(Refer Slide Time: 2:14)

(Refer Slide Time: 2:14) Fluid Dynamics And Turbo Machines. Professor Dr Shamit Bakshi. Department Of Mechanical Engineering. Indian Institute Of Technology Madras. Part A. Module-1. Lecture-3. Introduction To Fluid Flow. (Refer

More information

file:///d /suhasini/suha/office/html2pdf/ _editable/slides/module%202/lecture%206/6.1/1.html[3/9/2012 4:09:25 PM]

file:///d /suhasini/suha/office/html2pdf/ _editable/slides/module%202/lecture%206/6.1/1.html[3/9/2012 4:09:25 PM] Objectives_template Objectives In this section you will learn the following Introduction Different Theories of Earth Pressure Lateral Earth Pressure For At Rest Condition Movement of the Wall Different

More information

Influential Factors on Adhesion between Wheel and Rail under Wet Conditions

Influential Factors on Adhesion between Wheel and Rail under Wet Conditions Influential Factors on Adhesion between Wheel and Rail under Wet Conditions H. Chen, M. Ishida, 2 T. Nakahara Railway Technical Research Institute, Tokyo, Japan ; Tokyo Institute of Technology, Tokyo,

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

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

Numerical analysis of three-lobe journal bearing with CFD and FSI

Numerical analysis of three-lobe journal bearing with CFD and FSI Numerical analysis of three-lobe journal bearing with CFD and FSI Pankaj Khachane 1, Dinesh Dhande 2 1PG Student at Department of Mechanical Engineering, AISSMSCOE Pune, Maharashtra, India 2Assistant Professor

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

Analysis of Frictional Pressure Drop based on Flow Regimes of Oil-water Flow in Pipeline

Analysis of Frictional Pressure Drop based on Flow Regimes of Oil-water Flow in Pipeline Journal of Scientific & Industrial Research Vol. 74, March 2015, pp. 180-184 Analysis of Frictional Pressure Drop based on Flow Regimes of Oil-water Flow in Pipeline K R Naidu 1, T K Mandal 2 and S K Majumder

More information

Vane pump theory for mechanical efficiency

Vane pump theory for mechanical efficiency 1269 Vane pump theory for mechanical efficiency Y Inaguma 1 and A Hibi 2 1 Department of Steering Engineering, Toyoda Machine Works Limited, Okazaki, Japan 2 Department of Mechanical Engineering, Toyohashi

More information

2, where dp is the constant, R is the radius of

2, where dp is the constant, R is the radius of Dynamics of Viscous Flows (Lectures 8 to ) Q. Choose the correct answer (i) The average velocity of a one-dimensional incompressible fully developed viscous flow between two fixed parallel plates is m/s.

More information

Convective Mass Transfer

Convective Mass Transfer Convective Mass Transfer Definition of convective mass transfer: The transport of material between a boundary surface and a moving fluid or between two immiscible moving fluids separated by a mobile interface

More information

CHM The Liquid State (r15) Charles Taylor 1/7

CHM The Liquid State (r15) Charles Taylor 1/7 CHM 111 - The Liquid State (r15) - 2015 Charles Taylor 1/7 Introduction We have discussed solids and liquids in general. We're now going to discuss the liquid phase in greater detail. We will discuss properties

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

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 5.1.3. Pressure and Shear Stress

More information

The Role of Asperity Geometry and Roughness Orientation for the Friction-Reducing Effect of Adsorbed Molecular Films

The Role of Asperity Geometry and Roughness Orientation for the Friction-Reducing Effect of Adsorbed Molecular Films Tribology Online, 11, 2 (2016) 140-151. ISSN 1881-2198 DOI 10.2474/trol.11.140 Article The Role of Asperity Geometry and Roughness Orientation for the Friction-Reducing Effect of Adsorbed Molecular Films

More information

Fluid Mechanics Indian Institute of Technology, Kanpur Prof. Viswanathan Shankar Department of chemical Engineering. Lecture No.

Fluid Mechanics Indian Institute of Technology, Kanpur Prof. Viswanathan Shankar Department of chemical Engineering. Lecture No. Fluid Mechanics Indian Institute of Technology, Kanpur Prof. Viswanathan Shankar Department of chemical Engineering. Lecture No. # 05 Welcome to this fifth lecture on this nptel course on fluid mechanics

More information

Evaluation of tsunami force on concrete girder by experiment simulating steady flow

Evaluation of tsunami force on concrete girder by experiment simulating steady flow Journal of Structural Engineering Vol.61A (March 215) JSCE Evaluation of tsunami force on concrete girder by experiment simulating steady flow Li Fu*, Kenji Kosa**, Tatsuo Sasaki*** and Takashi Sato****

More information

Supplementary Information

Supplementary Information Supplementary Information Miniaturized Swimming Soft Robot with Complex Movement Actuated and Controlled by Remote Light Signals Chaolei Huang 1,4, Jiu-an Lv 2, Xiaojun Tian 1 *, Yuechao Wang 1, Yanlei

More information

Praktikum zur. Materialanalytik

Praktikum zur. Materialanalytik Praktikum zur Materialanalytik Functionalized Surfaces B510 Stand: 20.10.2017 Table of contents Introduction 2 Basics 2 Surface tension 2 From wettability to the contact angle 4 The Young equation 5 Wetting

More information

Lab Exercise #5: Tension and Bending with Strain Gages

Lab Exercise #5: Tension and Bending with Strain Gages Lab Exercise #5: Tension and Bending with Strain Gages Pre-lab assignment: Yes No Goals: 1. To evaluate tension and bending stress models and Hooke s Law. a. σ = Mc/I and σ = P/A 2. To determine material

More information

CFD based design and analysis of micro-structured. surfaces with application to drag and noise reduction

CFD based design and analysis of micro-structured. surfaces with application to drag and noise reduction KES Transactions on Sustainable Design and Manufacturing I Sustainable Design and Manufacturing 2014 : pp.162-171 : Paper sdm14-068 CFD based design and analysis of micro-structured surfaces with application

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