
- •Chapter I introduction
- •1. The subject of hydraulics
- •2. Historical background
- •3. Forces acting on a fluid. Pressure
- •4. Properties of liquids
- •Chapter II hydrostatics.
- •5. Hydrostatic pressure
- •6. The basic hydrostatic equation
- •7. Pressure head. Vacuum. Pressure measurement
- •8. Fluid pressure on a plane surface
- •Fig. 12. Pressure distribution on a rectangular wall
- •9. Fluid pressure on cylindrical and spherical surfaces. Buoyancy and floatation
- •Fig. 18. Automatic relief valve.
- •Relative rest of a liquid
- •10. Basic concepts
- •11. Liquid in a vessel moving with uniform acceleration in a straight line
- •12. Liquid in a uniformly rotating vessel
- •The basic equations of hydraulics
- •13. Fundamental concepts
- •14. Rate of discharge. Equation of continuity
- •15. Bernoulli's equation for a stream tube of an ideal liquid
- •16. Bernoulli's equation for real flow
- •17. Mead losses (general considerations)
- •18. Examples of application of bernoulli's equation to engineering problems
- •Chapter V flow through pipes. Hydrodynamic similarity
- •19. Flow through pipes
- •20. Hydrodynamic similarity
- •21. Cavitati0n
- •Chapter VI laminar flow
- •22.Laminar flow in circular pipes
- •23. Entrance conditions in laminar flow. The α coefficient
- •24. Laminar flow between parallel boundaries
- •Chapter VII turbulent flow
- •25. Turbulent flow in smooth pipes
- •26. Turbulent flow in rough pipes
- •27. Turbulent flow in noncircular pipes
- •Chapter VIII local features and minor losses
- •28. General considerations concerning local features in pipes
- •29. Abrupt expansion
- •30. Gradual expansion
- •31. Pipe contraction
- •32. Pipe bends
- •33. Local disturbances in laminar flow
- •34. Local features in aircraft hydraulic systems
- •Chapter IX flow through orifices, tubes and nozzles
- •35. Sharp-edged orifice in thin wall
- •36. Suppressed contraction. Submerged jet
- •37. Flow through tubes and nozzles
- •38. Discharge with varying head (emptying of vessels)
- •39. Injectors
- •Relative motion and unsteady pipe flow
- •40. Bernoulli's equation for relative motion
- •41. Unsteady flow through pipes
- •42. Water hammer in pipes
- •Chapter XI calculation of pipelines
- •43. Plain pipeline
- •44. Siphon
- •45. Compound pipes in series and in parallel
- •46. Calculation of branching and composite pipelines
- •47. Pipeline with pump
- •Chapter XII centrifugal pumps
- •48. General concepts
- •49. The basic equation for centrifugal pumps
- •50. Characteristics of ideal pump. Degree of reaction
- •51. Impeller with finite number of vanes
- •52. Hydraulic losses in pump. Plotting rated characteristic curve
- •53. Pump efficiency
- •54. Similarity formulas
- •55. Specific speed and its relation to impeller geometry
- •56. Relation between specific speed and efficiency
- •57. Cavitation conditions for centrifugal pumps (according to s.S. Rudnev)
- •58. Calculation of volute casing
- •59. Selection of pump type. Special features of centrifugal pumps used in aeronautical and rocket engineering
20. Hydrodynamic similarity
The Reynoldsnumber plays a significant part in hydraulics, as well as in aerodynamics, as an important criterion of the similarity of fluid flow. When incompressible liquids are considered similarity must be geometric, kinematic and dynamic.
Geometric similarity, it will be recalled from the course of geometry, means proportionality of corresponding dimensions and equality of corresponding angles. In hydraulics geometric similarity is interpreted to mean similarity of the surfaces constraining fluid flow, i. eM similarity of channels and their relative positions (Fig. 40).
* This consideration is of practical importance in the aerodynamics of air-foils (laiminar-flow wings).
Kinematic
similarity implies
similarity of streamlines and proportionality
of corresponding velocities. Obviously, kinematic similarity of
flow requires geometric similarity of the channels.
Dynamic similarity implies proportionality of the forces acting on the corresponding elements of kinematically similar streams and equality of the direction angles of those forces.
Fluid flow is usually subjected to a variety of forces, such as pressure, viscosity (friction) and gravity. For complete hydrodynamic similarity, proportionality of all these different forces must be observed.
For example, the proportionality of the pressure forces P and the friction forces F acting on the corresponding volumes in streams I and II (Fig. 40) can be written down in the form
In actual investigations it
is usually very difficult to achieve complete
hydrodynamic similarity. Experimenters commonly deal with partial
(incomplete) similarity, in which only the main forces are
proportional.
For flow under pressure in closed conduits (through pipes,
hydraulic machines, etc.) these main forces, as calculations show,
are pressure, friction and their resultants. In similar streams the
resultant forces are proportional to the product of the dynamic
pressure
times
the characteristic area S.
For a fluid particle of dimension AZ, force is the product of mass, times acceleration:
where к = dimensionless coefficient of proportionality depending on the shape of the particle; ds = elementary path of the particle.
Now
multiply and divide the foregoing expression through by
and
, thereby introducing quantities characterising
the flow as a whole. We have
The five dimensionless terms in the expression for &F have the same value for geometrically and kinematically similar streams and corresponding particles. Consequently, replacing the equality sign by a proportionality sign, we can write for these streams:
whence,
as
and,
we
finally
obtain
(5.3)
For similar streams / and II we have
or
The
last relation, which is the same
for similar streams, is called the
Newton number, denoted Ne. It
should be noted that in siifiilar streams the product
is
also proportional to the thrust which a flow exerts (or is capable
of exerting)
on obstacles, such as walls, vanes, submerged bodies, etc. Thus, if
a jet impinges normally on a flat plate of infinite area (Fig. 41)
the
direction of flow turns through 90°; from the well-known momentum
equation of mechanics the impulse is
. (5.4)
This is the dynamic force acting on the plate. If the angle of approach is different or if the obstacle has different shape or dimensions the proportionality factor is not unity.
Let us first consider the simplest case: motion of an ideal liquid in a horizontal plane, that is, motion not affected by viscosity or gravity.
For this case z, = z2, and Bernoulli's theorem for cross-sections 1-1 and 2-2 in Fig. 40 takes the form:
or
For two geometrically similar streams the right-hand sides of the equation have the same value, hence the left-hand members are also equal, i.e., the pressure differences are proportional to the dynamic pressures:
(5.5)
Thus, for the case of an ideal incompressible fluid moving without the participation of gravity forces, geometric similarity alone ensures complete similarity of flow. The dimension less quantity representing the ratio of the pressure difference to the dynamic pressure (or of the head pressure difference to the velocity head) is called the pressure coefficient, or the Euler number, denoted Eu.
Let us examine the conditions that must be satisfied by the geometrically similar streams just considered for hydrodynamic similarity when shear forces are acting and, hence, there is a degradation of energy, i. e., the conditions in which the Euler numbers are the same for the two flows.
Bernoulli's equation now takes the form
or
(5.6)
The latter equation shows that Eu is the same for both streams, hence they are similar if the loss coefficients are equal (the equality of the coefficients at and a2 for the corresponding cross-sections of the two streams follows from their kinematic similarity). Thus, in similar streams the coefficients £ must be the same, which means that the head losses in corresponding portions (see Fig. 40) are proportional to the velocity heads, i. e.,
Let us consider an important case of fluid motion: flow with friction in circular pipes, for which (see Sec. 16)
In
geometrically similar streams the ratio
is the same, hence the
similarity condition in this case is
equality
of the factor A, for both
streams. The latter, from Eq. (4.20), is expressed in terms of tne
shear stress t0
at the wajl and tbe dynamic pressure as follows:
Hence, for the two similar streams I and II we can write
(5.7)
i. e., the shear stresses are proportional to the dynamic pressure. Taking into account Newton's law of shew, the foregoing proportionality can be replaced by the following;
But, as in kinematic similarity we have the proportionality
then
After the necessary transformations we obtain the condition for the similarity of fluid flow, taking viscosity into account:
or, going over to the reciprocal quantities,
This
is Reynolds's law of similarity: For
two geometrically similar streams
of viscous fluids to be, dynamically similar, the Reynoldsnumbers
for two corresponding sections of the streams must be identical.
Now we see why the transition from one type of flow to another takes place at a specific Reynolds number. Furthermore, we find the physical meaning of the number for flow through pipes: it is a quantity characterising the ratio of the dynamic pressure to the shear -stress. The greater the velocity and the cross-section of a flow and the less the viscosity of a fluid, the larger the Reynolds number. For an ideal fluid Re is infinite since the viscosity is zero.
The problem of similarity is more difficult in cases when the difference in elevation heads cannot be neglected in Bernoulli's equation. In such cases yet another similarity criterion is introduced: the Froude number, which takes into account the effects of gravity on fluid flow. However, for the overwhelming majority of problems of interest to the mechanical engineer this characteristic is not essential and we shall not consider it.
To sum up, in similar streams the corresponding dimensionless coefficients and numbers α, ξ, λ, Eu, Ne, Re, and several others to be introduced later on, are identical. A change in the Reynolds number means a change in the relation between the basic forces acting in a stream in view of which the other factors may also change to «some extent. Thus they can all be regarded as functions of Re.