IMPROVEMENT IN OR RELATING TO IMPELLERS

Abstract: A rotatable impeller (49) for stirring liquids contained in tanks. Strip-like blades (50) of simple form radiate from a central hub (51), in swept-back configuration relative to the direction (54) of rotation. The blades are angled relative to the hub so as to exert a forward and downward force upon the liquid as the impeller rotates, and the blade curvature is such that the area projected upon the liquid by the solid structure of the rotating blade is less than the corresponding area that would be projected by an otherwise similar blade in which imaginary straight lines connected all adjacent vertices, and any void areas lying within the boundaries of those imaginary lines had been filled in. The preferred arrangement of the blades is such that when the impeller is arranged with its axis (67) vertical, curvature of each blade along its length is such that it extends away from the hub in a diminishing downward curve, reaches a lowest point (70, 71 Fig. 10), and then rises again before the blade tip (58) is reached. In cross-section each blade will typically be straight and parallel-sided, but may also be slightly curved (68), of aerofoil section (69), etc.

Description: This invention relates to rotatable impellers for stirring liquids contained in tanks, and to mixing apparatus comprising tanks fitted with such impellers. In typical industrial applications, liquid to be stirred is contained in a cylindrical tank arranged with its axis vertical, and the depth of the liquid is of the same order as the diameter of the tank. Stirring is effected by a rotating impeller immersed in the liquid, and mounted on a shaft co-axial with the tank. Typically the stirring takes place for one or both of two reasons. Firstly, the liquid may contain particles, which it is necessary to suspend and distribute homogeneously throughout the liquid. Secondly, air or other gas may be blown into the liquid, for instance through a perforated tube which is typically immersed in the liquid on the tube axis below the impeller, and it is necessary to achieve good dispersion of the gas within the liquid. The undesirable effect of gross rotation of the liquid within the tank by the rotating impeller is often inhibited by vertical baffles mounted at equal angular intervals around the inner surface of the cylindrical wall of the tank. Three impellers, each now regularly in use for the commercial stirring of liquids, are illustrated in Figures 1 to 3 of the accompanying diagrammatic drawings. Each such Figure shows a tank and the respective impeller in diagrammatic axial section, and Figures 1 and 2 also include a further underneath plan view of the impeller alone. The axial section gives an impression of the flow patterns that are set up when the impeller is mounted at the bottom end of a vertical shaft and rotated within a body of liquid contained in a cylindrical vessel. Figure 1 shows the kind of impeller usually known as a "disk turbine" or "Rushton impeller", comprising a circular disk 1 with six paddles 2 mounted at equal spacing around the periphery 3. Each paddle 2 is a plane rectangular metal sheet coplanar with the axis of the shaft 4 on which the disk is mounted, and extending both above and below the disk. In operation the dominant centrifugal action of the rotating paddles 2 throws the liquid out radially, generating the two circulation loops 5 and 6 within the liquid contained within a cylindrical vessel 7. The latter has a circular base 8 and a side wall 9, and vertical baffles 10 are mounted on the inner surface of the wall to inhibit gross rotation of the liquid by the impeller. Where the liquid contains particles, it is a drawback of this type of impeller that particle pick-up from close to the base 8 of the vessel is poor, because the circulation velocity in loop 6 close to the base is low. Also when gas is injected into the liquid, for instance through a sparging head 11 comprising a perforated ring 12 connected by radial feed conduits 13 to a vertical inlet pipe 14, the gas bubbles tend to enter the eye of the impeller because of both their buoyancy and the action of circulation loop 6; this gas then tends to form a gas cavity behind each paddle 2, so reducing the power transmitted to the liquid by that paddle. More generally, when any liquid is stirred by such a paddle intense local turbulence will be generated around the tips of the paddles in the region indicated by reference 15; this turbulence has the disadvantage of dissipating much of the input power. This disadvantage can be diminished by mounting the plane paddles 2 in sweepback fashion as at 2a, so that they lie at an acute angle to the tangent 16 to the periphery 3 instead of at right-angles. The second form of known stirring impeller illustrated in Figure 2 is a standard marine propeller 20, with the typical complement of three blades 21. The blades are of complex but well-known shape, designed to exert a screw action upon the liquid and to accelerate it in a downward direction, parallel to the axis of shaft 4. A single circulation loop 22 is therefore set up within the liquid, and high velocity in the lower part 23 of the loop between the impeller 20 and the base 8 promotes good particle pick-up where particles are present in the liquid. However, if gas is being introduced through sparging head 11, that gas tends to bypass much of the liquid because the strong loop 22 carries the bubbles both outwardly towards the wall 9, and then up that wall between baffles 10 and straight to the surface 24 of the liquid, because the circulation in the top part 25 of loop 22 is relatively weak so that bubbles tend to break the surface rather than remain within the loop 22. In the pitched-bladed impeller 30 of Figure 3, six plane strip-like blades 31 are mounted at equal angular intervals around the rim 32 of a rotor 33, from which they each extend radially outwards. The line along which the root of each blade is attached to the rim is inclined to the vertical, so that as the shaft 4 rotates in the direction of arrow 34 the forward face of each blade 31 is angled downwards. In operation the illustrated flow pattern therefore results; some turbulence in region 35, as in region 15 in Figure 1, and two circulation loops 36 and 37 with a particularly vigorous downward and outward motion 38 at the start of loop 37, due to the angling of blades 31. The present invention arises from the search for an impeller comparably simple in construction with those of Figures 1 and 3 but with improved performance in general, and in particular with less tendency to generate excessive turbulence immediately outboard of the tips of the blades or paddles, and with reduced energy requirement in order to achieve a pre-determined standard of mixing. In the course of the search, one factor that has become seen to be of significance is the effective area that is "swept" through the liquid by each blade or paddle as the impeller rotates. Figure 4 is a diagrammatic radial section through one of the paddles 2 of the impeller of Figure 1. Because the paddle is plane and rectangular, the area which it sweeps through the liquid as the impeller spins is simply the area (a x b) of the paddle itself. If the paddles does not lie at right-angles to the local tangent but is inclined to it, as at 2a in Figure 1, the area which it sweeps is diminished, by multiplying the same paddle area (a x b) by the sine of the angle of the inclination. However, we have appreciated that if the blade has at least one curved side, either by being so formed or by being bent after formation or both, what is in effect an enhancement of the swept area can be obtained. In Figure 5 the plane rectangular paddle 2 of Figure 4 is replaced by a plane paddle 40 having four vertices A, B, C, D and fixed to disk 1 so as to be coplanar with the axis of shaft 4. Opposite sides AD and BC are straight and vertical while the other two opposite sides AB and CD are curved and parallel. The area actually swept by paddle 40 as disk 1 rotates is therefore the area of the four-sided plate ABCD itself, and will be referred to as the actual swept area. However, we have found that while the power required to drive an impeller with such paddles tends to be related to the actual swept area, the degree of mixing achieved tends to reflect the sum of that actual area and any further area that can be enclosed by joining adjacent vertices by a straight line instead of by the curved side of the solid figure. In Figure 5, such a further area (shown shaded) is indicated by reference 41 and is of segmental shape, being bounded on one side by the curved side AB of the solid plate and on the other by the imaginary straight line 42 joining vertices A and B. In the following text, the sum of the actual swept area (in Figure 5, the area of the four-sided plate ABCD) and such a further area (in Figure 5, the shaded area 41) will be referred to as the total swept area. It will thus be apparent that the actual swept area represents the actual area projected upon the fluid by the solid structure of a rotating blade, while the total swept area represents the area projected by an otherwise similar blade in which imaginary lines connect all adjacent vertices, and any void areas lying within the boundaries of those lines have been filled in. The present invention is defined by the claims, the contents of which are to be read as included within the disclosure of this specification. The characterising feature of the invention is therefore that the blades are so arranged that when the impeller is arranged with its axis of rotation vertical, and is viewed in elevation, the curvature of each blade along its length is such that it extends away from the hub in a diminishing downward curve, reaches a lowest point, and then rises again to some extent before the blade tip is reached. This is to be contrasted with the kind of impeller shown in Patent Specification US-A-3397869, in which the blades shown in some of the drawings are curved along their length, but in which that curvature is always wholly upwards or wholly downwards relative to the impeller axis when the latter is held vertical. The invention will now be described, by way of example, with reference to the following further figures of drawings in which:- Figure 6 is a perspective view of an impeller rotated about a vertical axis, taken from above; Figure 7 is another perspective view, but from underneath; Figure 8 is a plan view of one form of blade, when first cut from flat material; Figure 9 shows the same blade in elevation, when ready for attachment to the hub after bending about is long axis; Figure 10 is a diagrammatic view of the impeller in vertical elevation, and includes a part similar to the second parts of Figures 1 to 3, diagrammatically illustrating the flow pattern set up in use by an impeller as shown in Figures 6 to 9; and Figure 11 is an alternative diagrammatic illustration of how the shape of the blade of Figures 8 and 9 may be determined. The impeller 49 of Figures 6 to 10 comprises six blades 50 extending outwardly at sixty-degree intervals from a hub 51. A central hole 52 in the hub receives shaft 4 to which the hub will be fixed by screw means shown diagrammatically at 53 in Figure 6, and by which the impeller will be rotated in the direction of arrow 54 in the same way as the known impellers shown in Figures 1 to 3 and already described. Each blade 50 is first stamped as a blank from flat metal sheet, to the four-sided shape shown in Figure 8. Of the two pairs of opposite and parallel sides of this four-sided figure, one pair (55,56) are long and curved and the other pair (57,58) are short and straight. The imaginary line 59 will be referred to as the long axis of the blank, and the imaginary line 60 as one of the transverse axes - that is to say the axes related to the depth dimension of the blade - and because axis 59 is long compared with axis 60 the blank may be described as being elongated in shape. To convert it to the form required of one of the blades 50, the blank is bent along its long axis 59 as shown in Figure 9. The short end 57 of the blade is the end welded, slotted or otherwise attached to the hub so that the locus of the meeting of hub and blade is a line 61 (see Figures 6 and 10) which is slanted to the vertical so that the forward face 62 of each blade (examples of which are best seen in Figure 7) is angled downwardly at about 45 degrees to the vertical. Because line 61 is necessarily curved, the short side 57 of the blank must of course be reshaped into a corresponding curve before the blade is actually fixed to the hub. Because the illustrated blades 50 are stamped from flat sheet and formed as described, the transverse axes 60 will be straight. However the blades could as one alternative be slightly curved over their depth dimensions as indicated in outline at 68 in Figure 6, giving rise to some degree of 'hydrofoil" action as each blade moves through the surrounding fluid in use. As another alternative the invention includes not only blades of uniform thickness but also thin blades of non-uniform section, for instance the foil section indicated in outline at 69. Figure 10 shows best the relationship between the total and actual swept areas which are swept by the blades 50. In the enlarged detail of that Figure, showing the blade (50a) lying most nearly at right-angles to the direction from which the view is taken, it is clear that the actual swept area, represented by the structure of the blade itself which is shown shaded, is less than the total swept area which includes also the area above the top edge 55a of the blade but below the imaginary line 63 joining vertices 64 and 65 which preferably (and as shown) lie in the same horizontal plane. From this Figure it is also apparent that due to the curvature of long axis 59 of the blade, and the angling of the line 61 along which the root of the blade is attached to the hub 51, each blade slopes downwardly away from its attachment to the hub 51 but reaches a lowest level (70,71) and is rising again as the blade tip (short side 58) is approached. It will be noted that with such geometry the centre of gravity of the blade lies higher, and thus closer to the level of the root line 61, than would be the case if the blade sloped downwards continuously from root to tip, and thus promotes better mechanical balance and strength. Figure 10 also indicates the typical flow pattern which an impeller according to the invention sets up in use. Like the pitched-bladed impeller 30 of Figure 3, impeller 49 sets up two strong and beneficial circulation loops 36 and 37. However, the curvature of each blade along its long axis 59 results in each blade being swept back in relation to the direction of rotation of the impeller which is indicated by arrow 54. In the case of the impeller actually illustrated in Figures 6 to 10, the extent of the sweepback is such that at the tip 58 of each blade the long axis 59 makes an angle α of about forty-five degrees to the radial line 66 joining that tip to the axis of shaft 4, as is best shown in Figure 6. This sweepback has an advantage comparable to that of the alternative, angled arrangement of paddle (2a) in Figure 1, namely that the reaction of the paddle against the fluid imparts so that fluid an element of motion that is not aligned with the motion of the blade itself, so reducing the absolute velocity relative to the container that is imparted to the fluid. This reduction of the absolute velocity reduces the dissipation of energy near the impeller - that is to say the energy wasted in regions 15 and 35 in Figures 1 and 3 - so that more of the input power goes into the loops 36, 37 thus giving better mixing. In general the impeller illustrated in Figures 6 to 10 generates a combination of downward and radial motion appropriate for mixing. When gas is introduced to the vessel 7 of Figure 10, for instance by sparge pipe 11 as before, the turbulent wake which formed behind each paddle or blade of the known impellers of Figures 1 and 3 is largely avoided; the shape and mounting of the blades of the impeller according to the invention promotes a smooth flow pattern over each blade so that when gas is injected below the impeller there is less tendency to form gas cavities behind the impeller blades. Compared with the ship's propeller shown in Figure 2, the impeller of Figures 6 to 10 has the potential advantages of better bubble distribution when gas is injected, due to greater radial liquid velocities in loops 36 and 37, and better particle distribution due to the combination of better upward liquid velocities near to the base of the tank, and higher radial velocities in the upper part of the tank at the crest of loop 36. An experiment was performed to compare the blending efficiency of an impeller according to the invention, as shown in Figures 6 to 10, with that of the three known impellers shown in Figures 1 to 3 and also the modified version of Figure 1 in which the paddles (2a) are swept back at forty-five degrees. The following dimensions were common to all five experiments :- tank diameter 0.3 m liquid depth 0.3 m impeller diameter (D) 0.1 m height of impeller above bottom of tank 0.1 m and gross rotation of the fluid within the tank was inhibited by four vertical baffles 10, each of height 0.3 m and width 0.1 m, equally spaced around the inner face of the cylindrical side wall 9. In the experiments a tracer was injected into the liquid and the concentration of the tracer was measured as a function of time at a fixed point in the liquid. If stirring is continued indefinitely, ultimately the concentration reaches a steady value c when mixing is complete. A mixing time N ϑ is defined as the time taken to reach a concentration within the range 1.05 c to 0.95 c, i.e. a concentration when c varies from its ultimate value by no more than 5%. N ϑ is found to be constant for a given impeller/vessel combination, and its value is a measure of the effectiveness of the impeller, small values being better than large. The following table records not only N ϑ , and the energy (in Joules) expended in 10 seconds of operation using each impeller, but also the power number N P =P/ρN³D⁵, P being the power to drive the impeller, ρ the liquid density and N the speed of rotation. For high values of Reynolds number ND²/µ, µ being the liquid viscosity, the power number is constant. A low value of power number is desirable to minimise driving power. The point at which tracer was introduced, the volume and concentration of the tracer and other relevant parameters were the same in all the experiments which gave rise to the results tabulated above: the type of impeller used was the only apparently significant variable. In these experiments the impeller according to the invention thus gave the best reading for mixing time, by far the best reading for energy consumption, and came a close second to the marine propeller of Figure 2 on power number. Figure 11 illustrates the form of a blade as so far described by imagining it to be cut from a sheet metal tube 90 of diameter 0.7D, D being as before the diameter of the impeller. The blade is generated by cutting out a piece of the tube wall, double hatched in Figure 11. The boundary of the blade is as before defined by the four lines AB, BC, CD and DA. AB and CD are straight lines parallel to the axis 91 of the tube, and 0.35D apart. The curve AD is generated by the intersection of an imaginary cylinder 72 of radius 0.475D with the tube 90, the axis 73 of cylinder 72 being at right angles to axis 91. The curve BC is generated in the same way as the curve AD, but the intersecting cylinder 72 is displaced downwards, in the elevation by a distance of 0.2D. The curvature of the long axis 59 is of course now the curvature (radius 0.35D) of the wall of tube 90. The effect on impeller performance of the curvatures just discussed will now be considered. The curvature of the long axis 59 of the blade is altered by increasing or decreasing the radius of tube 90 of Figure 11, and affects angle α of Figure 6. Reducing the radius increases α which reduces the strength of the circulation loops 36 and 37 in Figure 10. Increasing the radius decreases α and leads to high swirl, i.e. rotation of the liquid around the axis of the impeller in its direction of rotation: such swirl dissipates energy by impact on the baffles 10 Figure 1. A suitable compromise between the conflicting requirements of (i) strong circulation loops, and (ii) low swirl, is obtained by having α about 45°. As to the curvatures of the long blade sides 55 and 56, the "total swept area" as described and illustrated earlier in this specification is also represented by the sum of the single hatched and double hatched areas in Figure 11. When the blades are mounted on the hub, the liquid stirred by motion of the blades is proportional to the "total swept area" because liquid passing through the single hatched area subsequently passes over the blade near the corner D, D being at the outer periphery when the blade is mounted on the hub. As already noted, mixing effect is approximately proportional to the total swept area, whereas the power is approximately proportional to the swept area, i.e. the double hatched are on Figure 11. From this it follows that it is desirable to maximise the total swept area by increasing the curvatures 55 and 56, say by reducing the radius of intersecting cylinder 72 to 0.4D or 0.3D. However, if the curves AD and BC are too strongly curved, i.e. have too small a radius of curvature, this leads to an unsatisfactory design: the centre of gravity of the blades could be below the hub 51. Also the lowest point of curve BC will be much below the hub level, which will increase the circulation strength of the loop 37 and reduce the circulation strength of loop 36 of Figure 10, adversely affecting the mixing performance. A suitable compromise is to choose the radius of curvature of blade sides 55 and 56 (AD and BC in Figure 11) so that, when viewed from a point on the hub axis 67 (Figure 6), those sides appear as approximately straight lines.

Claims: An impeller (49) comprising a plurality of blades (50) or paddles radiating symmetrically from a rotatable hub (51), in which each blade is of elongated form and is curved along its length (59), one end (57) of the length being attached to the hub and the other (58) constituting the blade tip; and in which the curvature of the blades gives them a swept-back configuration relative to the direction of rotation (54) of the impeller; characterised in that the arrangement of the blades is such that when the impeller is arranged with its axis of rotation (67) vertical, and is viewed in elevation, the curvature of each blade along its length is such that it extends away from the hub in a diminishing downward curve, reaches a lowest point (70, 71, Figure 10), and then rises again to some extent before the tip is reached. An impeller according to Claim 1 characterised in that each blade is bent in a continuous curve along its length. An impeller according to Claim 2 characterised in that the curvature is uniform along the length. An impeller according to Claim 1 characterised in that the two opposite long edges (55, 56 Fig. 8) of the blade are parallel and curved. An impeller according to Claim 1 characterised in that each blade is attached to the hub along a line (61, Figs. 6, 10) inclined to a plane which intersects the axis of rotation (67) of the hub at right angles, the arrangement being such that if the impeller is rotated about a vertical axis the blades exert a forward and downward force upon liquid within which the impeller is rotated. An impeller according to Claim 1 characterised in that the tip (58) of the blade, and the locus of attachment of the blade to the hub (61, Figs. 6, 10), lie at substantially the same horizontal level when the impeller is so viewed. An impeller according to Claim 1 characterised in that each blade is twisted to some extent along its length, in the manner of a marine propeller. An impeller according to Claim 1 characterised in that each blade is slightly curved (68, Fig. 6) over its depth dimension. An impeller according to Claim 1 characterised in that each blade is of non-uniform thickness, having for instance a shallow aerofoil (69, Fig. 6) shape when viewed in cross-section.

Inventors: DAVIDSON, JOHN FRANK, NIRANJAN, KESHAVAN, PANDIT, ANIRUDDHA BHALCHANDRA
Applicants: BRITISH TECHNOLOGY GROUP LTD
Application year: 1987
Main classification: B01F15
IPC codes: B01F15, B01F7, B01F3