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Análisis de influencia de parametros geometricos en tanques agitados verticales

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  • AN EXAMINATION OF SOME GEOMETRIC PARAMETERS OF IMPELLER POWER

    R O B E R T L . B A T E S , P H I L I P L. F O N D Y , A N D R O B E R T R . C O R P S T E I N Chemincer, Inc., Dayton, Ohio

    The simplified equation for impeller power is well known and power coefficients have been published for most impellers. But many of the parameters of impeller and system geometry which appear in the gener- alized form of the equation are not well established. This paper is a study of the effect of some of the shape factors on impeller power. Including consideration of both impeller and vessel geometry, data are presented on impeller blade width, number of blades, blade angle, proximity of impellers to system bounda- ries, shrouding, spacing of multiple impellers, and extent of baffling. Both radial and axial flow turbine impellers are treated. New basic Power number curves are presented for the full Reynolds number range for a variety of turbine impellers.

    INCE Unwin (75) delivered a paper before the Royal S Society in London in 1880, there have been over 100 publications on the subject of impeller power. This would seem to indicate a subject SO well explored as to allow little room for further fruitful study. But this is far from the case. In the early studies the existence of a transition flow range and the effect of flow pattern on power were not fully appreciated. The tendency then, in attempting to write a "power equation," was to select average exponents for the various variables when actually operation under several flow conditions was repre- sented. Experimental facilities were often crude and even in some relatively recent papers the power data are not reliable. The trend in recent years toward use of the simplified form of the power number for all correlations has resulted in much apparent conflict of data.

    The initial purpose of this paper is to re-introduce the ex- panded form of the power equation, to establish perspective for this and future discusion of impeller power. Then, some of the terms representing impeller and system geometry are examined and new data on their effect on power presented.

    Background of Power Theory

    General Power Equation. White and coworkers (77- 79) were the first to point out the possibility and advan- tage of correlating impeller power by dimensional analysis. To them goes credit for originating the drag coefficient group now known as the Power number. The development of a full generalized form of an equation for correlating power has been well covered by Hixson and Luedeke (5) , Johnstone and Thring ( 6 ) , and Rushton, Costich, and Everett (73). A re- lationship in its full form, using impeller diameter. D. as the referenced length, is:

    The dependent variable in Equation 1 characterizes the basic flow pittern, as proposed by White and Brenner (77), and is called the Power number, Np. The first independent dimensionless group is readily recognized as the impeller Reynolds number, 'YRe. The second group is the Froude

    number, NFr, theoretically required to account for the vortex formation in a swirling system. The next seven terms in Equation 1 define the effect of system and impeller geometry. The last term is not a linear dimension ratio but is required to account for a change in number of impeller blades, referenced to some standard design basis. To be fully inclusive, the equation should be expanded to include: baffle nidth and number of baffles; spacing of multiple impellers; and off- center impeller positioning.

    The last seven terms of Equation 1 and the three just mentioned are parameters of geometry. If geometric similarity is stipulated and a non- swirling system employed, the equation simplifies to

    A', = K(NR,)* (2)

    First, it makes for easier evaluation of the more critical factors affect- ing power since, admittedly, the effect of many of the shape factors can be minor. And it recognizes that geometric similitude is easily maintained in scale-up work-and is usually desirable.

    For illustrative purposes and for many applications, the simplified version is acceptable. But the very ease ivith which it can be used has led to widespread use for correlating all power data, irrespective of geometry. The result has been some confusion and several useless correlations. There are many ways of treating the shape factors in correlating power. The full general equation could be used but is obviously cumbersome. The conventional plot of log Zip zs. log i\rRe is undoubtedly the best way to present the basic power behavior of an impeller, but its use would seem to be best restricted to representing a stipulated and essentially standardized set of conditions for impeller and system geometry. Deviations from the standard can then be treated individually or collectively in the manner best adapted to the particular variables. Fore- glimpsing the results of this study, we find that some of the parameters may be analyzed individually and that others are interrelated and must be grouped. Thus, it may be antici- pated that a simple exponential representation as indicated in Equation 1 is not always feasible or especially helpful for many of the geometric factors.

    Simplification of Power Equation.

    The justification for this simplification is twofold.

    310 l&EC PROCESS DESIGN AND DEVELOPMENT

  • Experimental

    The content of this paper is derived from a broad study of all types of impellers--radial, axial, and tangential-in the range of flow from laminar to fully turbulent. Since the majority of geometric factors are prevalent in the turbulent range and, in practice, with turbine-type impellers, the data presented here (with the exception of Figure 1) are for these conditions. Table I presents the range of variables used in this work. In the portion of this study where it was desired to maintain geometric similitude, the following "standard con- ditions" were used: D,/T = l / 3 , C / T = ;/?, Z / T = 1, nb = 4, t u b = T/12.

    Table 1. Range of Variables Used in This Work Vessel diameters. Turbine diameters. Turbine styles. Flat six-blade disk style; flat, curved, and 45

    pitched six-blade open styles ; styles with blade angles 25 to 90

    6, lC, 12, 15, and 24 inches 3, 4, 5, 6, 7, 8, and 10 inches

    four-blade open

    w / D range. 0.062 to 0.37 D I T range. 0.25 to 0.50 nb range. 1 through 12 wb/T range. 7 to 15% nbwb/T range. 0.1 to 1 Newtonian fluids used. Viscosity range. N R ~ range. 10 -l to 106

    Water, corn sirup 1 to 120,000 cp.

    The variable-speed drive and dynamometer assembly used in most of the work was the Model ELB assembly manufactured by Chemineer, Inc., and described by Bates ( 7 ) . A larger version of this system was used for runs in the 24-inch diameter vessel.

    This was accomplished here by using investment castings for the

    Impeller dimensions were controlled very accurately.

    500

    standard impellers and machined fabrications for the special styles studied, The projected blade width of the pitched blade impellers was rigorously controlled by machining both blade edges in the plane of rotation. This was necezsary to eliminate any possible "edge" effect in the smaller impellers.

    Impeller Geometry

    Figure 1 is the conventional log-log plot of the simplified power equation and is presented here to submit new data on radial discharging impellers and to illustrate the characteristic curves for different impeller styles. These data represent over 1000 points recorded for the various designs under the "standard" conditions in Newtonian fluids.

    Curve 1 is the correlation from this study for the radial discharging six-blade turbine impeller on which data were originally presented by Rushton, Costich, and Everett (74). Several investigators (3, 70) have since obtained values of the Power number lower than the 6.3 reported by Rushton for the turbulent range. The data of this study indicate a value of 4.8 for four T/12 bafRes and 5.0 for four T/10 baffles..

    Noteworthy is the finding that a difference in power require- ment exists between the disk style of construction and the flat- blade turbine in the turbulent range. Curve 2 is this open flat-blade style with a full blade originating a t the hub. Though it has a longer blade than the disk style, it consumes approximately 25% less power. Since this study was con- cerned only with impeller power consumption, it has not been established whether the vaned-disk construction yields a higher performance for its increased power requirement.

    For the same "standard" system conditions, full curves are also shown for flat, curved: and 45" pitched-blade open style six-blade turbines kvith rc/D of l/,+

    Style.

    I CURVE 3 CURVE 4 CURVE 5 CURVE 6 I

    IO

    5

    I

    0.5 I IO I 0' I o3 I 0' I o5

    - P N D ~ NRI- 7 Figure 1. Power number-Reynolds number correlation in Newtonian fluids for various iurbine impeller designs

    VOL. 2 NO. 4 O C T O B E R 1 9 6 3 311

  • 0 05 01 02 03 04 0 5

    # Figure 2. blades on power

    Effect of width and number of turbine

    Blade Width and Number of Blades. In using the simpli- fied relationship where power is proportional to D3 in the lami- nar and D5 in the turbulent range it is often assumed that w is equivalent to a D term and that power is directly proportional to the blade width. This is not true in the laminar and transi- tion range but has been generally thought to be true for the turbulent case. The fact that the exponents of all linear dimension terms will total the exponent of the diameter term merely confirms the cumulative effect of impeller geometry. The exponent of the D term must always be recognized as of variable composition.

    In the fundamental study of OConnell and Mack (72), where open-style radial discharging turbines were used, blade width and number of blades were found to be interdependent variables. For the six-blade design they found power to vary as ( z e ~ / D ) ~ . ~ ~ . Their four-blade design had a blade width effect of (wD)1.lj.

    Figure 2 is the correlation from this work for both the four- and six-blade open-style designs again operating in the standard system. The range of 0.067 to 0.37 w / D ratios more than spans those commercially used.

    For the four-blade design, the exponent of the a / D ratio was found to be 1.25 but the six-blade was 1 .O.

    10

    0 9

    OB

    07

    06

    0 5 0

    $ 04 L.

    03

    02 I I I 1 02 03 0 4 05 0 6 07 08 09 10

    POWER RATIO - P, IPw. Figure 3. Effect of turbine blade angle on power

    312 I & E C PROCESS D E S I G N A N D D E V E L O P M E N T

    Thus the effect of blade width and number of blades for these two designs is seen to be interrelated. I t is not possible to establish the independent effect of blade width and number by the simple (w/D)O and (nz ln l )% from Equation 1. The easiest approach involves preparing a plot similar to Figure 2 for the style of impeller being considered and obtaining power cor- rection factors directly.

    The universal use of the 45 blade angle for pitched-blade turbines has resulted in a complete lack of data on the effect of blade angle on power. The two fre- quently cited sources, Hixson and Baum (4) and Van de Vusse (76), are for unbaffled systems and thus not helpful for the usual application. Since turbine impellers have a constant blade angle, as contrasted with the helicoidal design of propel- lers, the term pitch has no real significance. Thus. this correlation of power with pitch uses a function of blade angle rather than the ( p / D ) term of Equation 1.

    Figure 3 is the correlation for four-blade open-style pitched turbines operating in a standard system. Projected blade width in the elevation (w sine B ) was held constant for each series of runs. The abscissa term P B / P s o ~ is simply the ratio of power in a given condition of pitch to the power consumption ofa radial discharging style with vertical blades. Over a blade angle range of 25 to 90 then, we may substitute-for four- blade turbines-for the (p /D) term the expression (sine e)? 5 .

    Shrouded Impellers. A radical discharging turbine is frequently equipped with a partial or full plate on the top and/or bottom to control the suction. The few writers who mention this style of construction used impellers similar to a centrifugal pump impeller and the separate influence of the shroud is not indicated. Lee, Finch, and Wooledge (7) used a shrouded disk turbine in their high viscosity work, and their data for the laminar and transition range indicate an increase in power of as much as 50%.

    From this study. data on the effect of the two most common shroud modifications are available. The basis is operation in the turbulent flow range, with impeller location and baffle design as stated earlier for standard conditions. With the shroud plate fully covering the top of the turbine, the power increase is 30%. \Vith a full bottom shroud, the increase is

    Impeller Pitch.

    47%.

    System Geometry

    The environmental effect of fluid properties is generally well appreciated and always included in evaluation of a given im- peller. But the external factors of geometry relating the im- peller to the system boundaries and influencing flow pattern have received remarkably scant attention.

    An investigation to confirm the published statement that the ratio of impeller to tank diameter ( D / T ) has no effect on power revealed that there is an effect-at least with the flat open-style six-blade turbine-and that this variable is interrelated with the extent of antiswirl baffling present.

    The phrases 100% baffling or full baffling are commonly used in both academic and industrial parlance, but are variously defined in terms of the number and width of baffle plates. These are, of course, assumed to be conditions which give ap- proximately maximum power consumption. Four flat baffles are most frequently used. Many fundamental studies have used a baffle width of T/10. but industrial practice is almost universally T/12. The precise effect on power of variation in number of baffles and baffle widths has been presented in two contemporary works, although the findings are not in agree- ment. Bissell et d. ( 2 ) tabulated, without supporting data, the

    DIT and Barnes.

  • 30

    2.5

    2.0

    01 02 0 3 04 06 08 I O

    BAFFLE RATIO - 9 Figure 4. Effect of baffling and D/T on power

    5

    4

    3

    N, 2

    050

    008 01 J2 0 3 0 4 0 5 0 6 0 8 10

    3AFFLE RATIO - Figure 5. Composite curve from Figure 4

    25 I

    I I 0 5 10 1 5 2 0 2 5 3 0 35

    IMPELLER SPACING RATIO - S/D Figure 6. Effect of dual turbine spacing on power

    per cent power based on four T I 1 2 baffles and show an increase in power above four baffles and above T12 width. Mack and Kroll (8) found a limiting condition of number and width of baffle. above which no increase in power occurred. The recent work of Sagata and associates ( 7 7 ) shobvs that the power for a given number of baffles reaches a maximum and then decreases somewhat as width increases. An approximation of their results gives the relation

    nbZeb 0.5 T (3)

    for maximum poiver consumption. This result. however, waa based on a study involving a two-blade impeller in only one vessel diameter.

    Each poinl was computed from r.p.m.-horsepower correlations (approximately 1000 recorded data points) of six flat open- style six-blade turbines in three tank diameters using no baffles 1 through 12 in w o / T ratios from 7 to 15%. It is apparent that a variable power effect results from changes in D , / T ratio and opposed baffle area.

    Figure 5, combining the curves from Figure 4, shows the combined effect of D / T ratio and baffling. Data points are omitted for clarity. .4t nbreb/Tvalues less than 0.20: measured Power numbers decrease with increasing D,IT ratio. Con- versely, a t nbzeb,/T values above 0.33, measured Power numbers increase with increasing D l T . The industry standard of four T j 1 2 baffles gives an n,,zeb/T value of 0.33. Figure 5 shows that the change in Power number lvith D , T ratio is essentially negligible, within 5% for the D I T range studied.

    The studies of Kushton et al. (74) indicate no effect on power for variation in D / T . The only significant difference between that work and this study is that a disk-style turbine was used.

    Shape Factors. Practically all power studies have been made in vertical cylindrical vessels. Data on other arrange- ments which occur in practice are limited. Table I1 shoivs results for several common applications for flat open-style six- blade radial discharging turbines with impeller diameter 40% the width or diameter of the tank and bottom clearance at one impeller diameter. The factor shown is the ratio of impeller power drawn in the specific geometry to that for standard conditions.

    Even though equivalent poiver consumption is apparent for several situations, there is a drastic difference in the nature of the flow pattern. Choice of the style of installation Ivould be determined by the particular process requirement.

    Spacing. The effect of impeller spacing on power is shown in Figure 6. Spacing as used here is the vertical dimension between the bottom edges of the two turbines; a spacing of 0 indicates complete coincidence of the two impellers. In the ratio P*/PI, the reference power, PI, is a flat open-style six- blade turbine in all cases. The 45 pitched-blade turbine then falls lowest and the combination of the two styles is inter- mediate. Both styles have W I D = l i s . \\?thin a spacing of four impeller diameters, dual pitched-blade turbines do not yet equal twice the po\ver consumption of a single. The com- bination of two types? the pitched above the flat, reaches a level of the sum of the two a t about one diameter spacing. But two flat-blade turbines actually develop a total power almost 2570 greater than the sum of the two when the spacing is less than one diameter.

    This study shows that the space beneath a turbine impeller has a definite effect on power. These data are in disagreement with those of Mack and Kroll (8) : who noted no change in power for two-blade turbinesover a range of C / D values from 0.35 to 2.5.

    Figure 4 is a summary of data for four D I T ratios.

    Proximity to Tank Bottom.

    VOL. 2 NO. 4 O C T O B E R 1963 313

  • ~~~ ~~~

    Table II. Vessel Shape Power Factors for Six-Blade Open-Style Turbine

    WID = 1/8 Impellm Vertical Bajj7es

    Installation D I T Location Vumber Location Factor

    Horizontal cylindrical tank, 5 :1 0 . 4 Center mounted None 1 . o (2) T/10 D/4 distance, 180 longitudinal 1 .O

    Square tank axis

    0 . 4 Center mounted None . . . T/4 eccentric mounted None . . .

    (2) T/10 180, wall center Center mounted (4) TI10 90, wall center

    0.75 1 . o 1 . o 1 .o

    To indicate clearly the typical behavior of the three styles of turbines, Figure 7 shows the Power number for the ordinate rather than a power factor. For direct use as a geometric factor in Equation 1, the ratio of the N p value for a specific condition to the N p value at standard conditions-Le., C/ T = l / g c a n be used.

    For the disk turbine, since the suction is partitioned by the disk, there is a marked reduction in power as clearance is de- creased. The flat open-style six-blade turbine ( w / D = l / ~ ) displays a variable effect a t different clearances, but in general a slightly higher power level a t lower values of C/D.

    Increasing the proximity of a 45 pitched open-style six- blade turbine (w/D = l / ~ ) , as expected, increases power con- sumption. The data of Miller and Mann (9) note a reduction in power rather than a n increase, but their data were taken in an unbaffled system and thus are not comparable.

    DISC TYPE

    I

    I , I 01 02 03 0 4 06 O B 10 20

    CLEARANCE RATIO + C/D

    Figure 7. Effect of turbine proximity on power

    Nomenclature

    C = impeller distance off tank bottom, measured from

    D = impeller diameter g, K = constant 1 = blade length n nb = number of baffles .V = impeller speed, r.p.m. ArFp = Froude number N p = Power number NRe = Reynolds number

    = blade pitch PP = power S = impeller spacing

    underside of impeller

    = gravitational constant or conversion factor

    = number of impeller blades

    T = tank diameter w = impeller blade width wb = baffle width Z = liquid depth

    GREEK LETTERS e p = viscosity p = density

    SUBSCRIPTS 1 = condition 1 2 = condition 2 EXPONENTS = a, b , G, etc.

    = angle of impeller blade from horizontal

    literature Cited

    (1) (2)

    (3) (4) (5) (6)

    Bates, R. L., Ind. Eng. C h m . 51, 1245 (1959). Bissell, E. S., Hesse, H. C., Everett, H. J., Rushton, J. H.,

    Calderbank, P. H., Trans. Inst. Chem. Engrs. 36, 443 (1958). Hixson, A. W., Baum, S. J.. Ind. Eng. Chem. 34, 194 (1942). Hixson, A. W., Luedeke, V. C., Ibid., 29, 927 (1937). Johnstone, R. E., Thring, M. W., Pilot Plants, Models and

    Scale-up Methods in Chemical Engineering, McGraw-Hill, New York. 1957.

    Chem. Eng. Progr. 43, 649 (1947).

    (7) Lee, R. E., Finch, C. R., Wooledge, J. D.. Ind. Eng. Chem.

    (8) Mack, D. E., Kroll, A. E., Chem. Eng. Progr. 44,189 (1948). (9) Miller, S. A., Mann, C. A.. Trans. A.I.CI1.E. 40, 709 (1944). (10) Nanata. S.. Yokovama. T., Mem. Fac. Ene., Kyoto Unzv.

    49, 1849 (1957).

    , , I . , (Japm,17, 25 3 (1 9 5 5) . (11) (12)

    Nagata, S., Yokoyama, T., Maeda, H., Ibid., 18, 13 (1956). OConnell, F. D., Mack, D. E., Chem. Eng. Aogr. 46, 358,

    (1 950).

    395 (1950). (13) Rushton, J. H., Costich, E. W., Everett. H J.. Ibzd., 46,

    (14) Ibid., b. 467. (15) (16) (17) (18)

    (19)

    Unwin, W. C.: Proc. Roy. Sac. (London) A31, 54 (1880). Van de Vusse, J. G.. Chem. Eng. Sci. 4, 178, 209 (1955). White, A. M.: Brenner, E., Trans. A.Z.Ch.E. 30, 585 (1934). White, A. M., Brenner, E.: Phillips, G. L4., Morrison, M. S.,

    White, A. M., Somerford, S. D., Chem. M e f . Eng. 43, 370

    RECEIVED for review December 31, 1962 ACCEPTED June 10, 1963

    Ibid., 30, 570 (1934).

    (1936).

    A.1.Ch.E. Meeting, Chicago, Ill., December 1962.

    Correction

    THE KINETICS OF NICKEL CARBONYL FOR MATI ON

    In this article by M. M. Goldberger and D. F. Othmer [IND. ENG. CHEM. PROCESS DESIGN AND DEVELOP. 2, 202 (1 963) 1, on page 209, reference 8 should read :

    Othmer, D. F.. Luley, .4. H.. Ind. Eng. Chem. 38,408 (1946).

    314 I h E C PROCESS D E S I G N A N D D E V E L O P M E N T