- •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
24. Laminar flow between parallel boundaries
We shall now consider laminar flow between two parallel flat walls (Fig. 48). Placing the origin of our coordinate system halfway between the two walls, the x axis is pointed in the direction of flow and the у axis is normal to the walls.
Passing two cross-sections normal to the flow the distance between which is l, consider a rectangular volume of thickness 2y and unitwidth perpendicular to the page (Fig. 48). The condition for uniform motion of the control volume along the x axis is:
where pf = рг — p2 is the difference between the pressure intensities at the two cross-sections. The minus is due to the negative value of the derivative du/dy.
From the foregoing, determine the velocity increment dv corresponding to the coordinate increment dy:
Integrating,
(6.11)
As, at у = , и = 0, then , whence finally
То compute the rate of discharge per unit width, first take two elementary areas of size I X dy located symmetrically relative to the z axis and express the elementary discharge:
whence
(6.12)
From this, expressing the pressure loss in terms of the mean velocity
(6.12)
The relations obtained can be used to investigate flow through a space between two nested cylinders parallel to their centre lines if the space a is small in relation to the cylinder diameters: otherwise the law is more complicated, and we shall not examine it here.
When one of the walls is moving parallel to the other with velocity U, the pressure intensity in the space being constant along its length, the moving wall carries the fluid along. The velocity distribution is linear (Fig. 49) and therefore expressed in the form
(6.14)
The rate of discharge per unit width of the spacing perpendicular to the page is determined from the mean velocity, which is , i. e.,
(6.15)
If there is a pressure drop in the fluid filling the spacing, the velocity distribution law across the space is found as the sum (or difference, depending on the direction of motion of the wall) of expressions (6.11) and (6.14):
The resultant velocity distribution across the space is shown in Fig. 50 when (a) the wall moves in the direction of flow due to the pressure drop, and (b) the wall moves in the opposite direction.
The rate of discharge is determined as the sum of the discharges given by Eqs (6.12) and (6.15):
This kind of flow through narrow spaces is found in pumps and other hydraulic machines.
Example. Determine whether an aircraft lubricating system with the characteristics given below will function in horizontal flight at an altitude of 16,000m (mm Hg) (i. e., determine absolute pressure at pimp intake
in mm Hg). The length of the intake pipeline is / = 2 m, the diameter d -18 mm; elevation of the oil surface in the tank above the pump z = 0.7 m; tin pressure in the oil tank is atmospheric (Fig. 51). The required flow rate to ensure the necessary heat transfer into the oil at maximum performance of the engiiu is Q = 16 lit/min; viscosity of MK-8 oil v = 0.11 cm2/sec, yoil=900 kg/m. Neglect local losses.
Solution, (i) Velocity of oil in pipeline:
(ii) Reynolds number:
(iii) Friction loss in intake pipe:
(iv) Pressure at pump intake from Bernoulli's equation between sections 0-0 and 1-1:
whence
or
Hg