CA1221659A - Hydrocyclone featuring hydraulic jump in overflow passage - Google Patents
Hydrocyclone featuring hydraulic jump in overflow passageInfo
- Publication number
- CA1221659A CA1221659A CA000426450A CA426450A CA1221659A CA 1221659 A CA1221659 A CA 1221659A CA 000426450 A CA000426450 A CA 000426450A CA 426450 A CA426450 A CA 426450A CA 1221659 A CA1221659 A CA 1221659A
- Authority
- CA
- Canada
- Prior art keywords
- passage
- diameter
- truncated cone
- hydrocyclone
- segment
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21D—TREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
- D21D5/00—Purification of the pulp suspension by mechanical means; Apparatus therefor
- D21D5/18—Purification of the pulp suspension by mechanical means; Apparatus therefor with the aid of centrifugal force
- D21D5/24—Purification of the pulp suspension by mechanical means; Apparatus therefor with the aid of centrifugal force in cyclones
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C5/00—Apparatus in which the axial direction of the vortex is reversed
- B04C5/12—Construction of the overflow ducting, e.g. diffusing or spiral exits
- B04C5/13—Construction of the overflow ducting, e.g. diffusing or spiral exits formed as a vortex finder and extending into the vortex chamber; Discharge from vortex finder otherwise than at the top of the cyclone; Devices for controlling the overflow
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Cyclones (AREA)
Abstract
HYDROCYCLONE FEATURING HYDRAULIC JUMP IN OVERFLOW PASSAGE
ABSTRACT OF THE DISCLOSURE:
A hydrocyclone featuring a longitudinally extended pas-sage defining an outlet from its separating chamber wherein means bounding a relatively short segment of its length, at a location downstream from its inlet, is constructed and arranged to convert kinetic energy in the flow therethrough to pressure energy and to produce a resultant application of the converted energy to the slurry moving within the separating chamber to increase its spin velocity.
ABSTRACT OF THE DISCLOSURE:
A hydrocyclone featuring a longitudinally extended pas-sage defining an outlet from its separating chamber wherein means bounding a relatively short segment of its length, at a location downstream from its inlet, is constructed and arranged to convert kinetic energy in the flow therethrough to pressure energy and to produce a resultant application of the converted energy to the slurry moving within the separating chamber to increase its spin velocity.
Description
122165g HYD~OCYCLONE FEATURI~G HYDRAULIC JU~P IN OVERFLOW PASSAGE
BACKGROUND OP THE INVENTION:
This invention relates to improvements in hydrocyclones, which includes centrifugal separators and centrifugal clean-ers. Its embodiment provides an improved construction forthe overflow tube of a hydrocyclone which has unexpectedly resulted in the recovery of kinetic energy in the overflow as well as other significant benefits in the performance of the hydrocyclone. ~his is particularly evidenced in the application of the invention to the processing of pulp in a pulp refining operation. Accordingly, the invention will be described in this frame of reference, but only for pur-pose of illustration and not by way of limitation.
A hydrocyclone is a device used for cleaning, separa-tion and/or classification of the contents of a relativefluid mass. As applied to a pulp slurry, the objective in its use is to extract and separate therefrom elements or particles of wood or other fibrous matter in the slurry best suited, and in a form best suited, for use in a par-ticular end product. It has been found in many cases thatthe level and amount of energy required for the operation of prior art hydrocyclones or hydrocyclone systems can be quite substantial. It has also been found that the extent of the pressure drop which occurs in the use of prior art hydrocyclones to process a pulp slurry limits the through-- put of the slurry as well as its flow rate in moving through and from the hydrocyclone. The problems noted are and have been a matter of serious concern for a long period of time.
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~221659 The prese~t invention not only overcomes the ~oreqoing problems to a substantial degree but its application to any hydrocyclone of a given size provides it with an inherent mode of operation resulting in an increase in its feed 5 - flow rate as well as a significant improvement in its cleaning efficiency. ~s a matter of fact, the application of the invention enables more of the energy applied in use of a hydrocyclone to contribute, very effectively, to the spin of the flow of a slurry introduced to and moved within and longitudinally of the hydrocyclone separating chamber.
The result of this last feature is a cleaner and more ef-fective separation of the contents of the slurry which is subjected to a separating procedure.
As far as novelty is concerned, there is no knowledge of any prior hydrocyclone art which is specific to the improvements of the present invention. A search of the records of the 17. S. Paten~ and Trademark Office appears to confirm this fact. All that the search produced is exemplified by the following patents:
Patent No. Name Date 3,037,628 G. H. Tomlinson II June 5, 1962 3,129,173 W. G. A. Schulze April 14, 1964 3,261,467 N. A. L. Wikdahl July 19, 1966 3,613,887 N. A. L. Wikdahl Oct. 19, 1971 3,746,173 W. H. Daniel July 17, 1973 4,259,180 Jorma Surakka et al M.ar. 31, 1981 .
~ ZZ16S9 S~'.~MARY OF T~IE INVENTION:
Preferred emb~diments of the present invention comprise a hydrocyclone the body of which defines therein a separating chamber having an overflo~ end and an underflow end, an inlet and at least two outlets, one to each of the opposite ends of the ~eparating chamber. One of these outlets provides an underflow outlet and the other an overflow outlet. The inner wall of the hydrocyclone has a tubular configuration and the underflow and overflow outlets are in a substantially coaxial alignment. In the introduction of a pulp slurry, the contents of which are to be separated and/or cleaned or classified, the inlet applies the slurry tangential to thë inner wall surface of the hydrocyclone to develop within its separating chamber a vortex-type flow of the slurry producing counterflowing vortices thereof. The result of the counterflowing vortices is to induce, normally, a particularly desired portion of the contents of the slurry to move to an area within the separating chamber comprising its central longitudinally extending core from which such material is inherently in-duced to flow to and through the overflow outlet of the hydrocyclone. At the same time another portion of the contents of the slurry within the separating cham~er in-cluded in the outer of said counterflowing vortices is caused to move to and through the underflow outlet of the hydrocyclone. In accordance with the invention, the over-~5 flow outlet is defined by an overflow tube structure, here-- inafter referred to as an overflow tube, the diameter of ~ - 3 -t~e inner surface of which is stepped along its length. ks will be obvious, the inner surface of the overflow tube de-fines an overflow passage one end of which communicates with the overflow end of the hydrocyclone separating chamber and the other end of which connects to a conduit or conduits for directing the discharge from the overflow tube to a desired place of storage or use. Per the invention the inner surface of the overflow tube and the overflow passaye which it defines are formed to produce therein a conversion of kinetic energy in flow therethrough from the hydrocyclone separating chamber to pressure energy. This produces inobvious and most ad-vantageous improvements in the performance of the hydrocyclone.
Actually, what has been observed to occur in the use of an overflow tube havina an overflow passage formed in accordance with the invention is a "hydraulic jump" phenomena.
Ihen comparing the operation of a conventional hydro-cyclone having an overflow passage in accordance with the prior art with the operation of a hydrocyclone of the same size embody-ing the invention, it is seen that the use of the invention re-sults in the following benefits and improvements:
a. A decrease in pressure drop in the flow through the hydrocyclone;
b. An increase in the "spin" of the material introduced to and passed through the hydrocyclone separating chamber;
c. A significant increase in the cleaning and sepa-rating efficiency of the hydrocyclone and an increase in its operating capacity and feed flow rate;
d. ~n increase in the throughput or flow rate of the , ' '" ' . ' ' ' ' : '',' ' ~ ..
12Zl~iS9 material to be separated or cleaned in the movement thereof through and from the separating cha~er of the hydrocyclone.
A preferred embodiment of the invention provides that the outflow passage defined by its overflow tube includes straight line segments of its length which are spaced by a relatively short coaxial segment which has the shape of a truncated cone. In this case the upstream of these straight line segments will have a diameter corresponding to the small-est diameter of the relatively short segment which has the confi~uration of a truncated cone while the straight line segment of the outflow passage immediately downstream of this short segment will have a dlameter which is relatively enlarged as compared to that of the upstream segment and corresponds with that of the downstream end of said short segment. In use of this preferred embodiment the efficiency of the operation of a hydrocyclone of a given size is sub-stantially improved and there is a corresponding saving and added utilization of the available energy. A significant aspect of the invention is the economy possible in its em-bodiment.
While in describing the invention reference is madeherein to an overflow tube applied to a conventionally opera-ting hydrocyclone, it is to be understood that an outflow pas-sage of the nature herein described and claimed may be formed in any tube or body structure providing an outlet from the separating cha~er of any type hydrocyclone and ?roduce similar results and benefits in its use.
It is therefore a primary object of the invention to provide economically achieved improvements in hydrocyclones :. -lZZ1659 which are easy to fabricate and which render such devices ~ore efficient and satisfactory in use, adaptable to a wide variety of applications and less likely to adversely function.
In one broad aspect, the invention resides in a hydro-cyclone comprising a housing having a separating chamber, an inlet to said chamber and at least two outlets therefrom, said inlet being constructed and arranged to deliver a slurry or other fluid mass containing solids the contents of which are to be separated, cleaned or classified, to said chamber in a substantially helical, swirling, flow pattern to cause the movement thereof within said chamber in counterflowing vortices inherently causing solids in the flow which are light and relatively small in size to move to the inner vortex of the flow and exit from a first outlet while the remainder of said flow embodying large and heavy solids seeks another outlet from said chamber, said first outlet being a longi-tudinally extended passage having an inlet end open to said separ-ating chamber and a discharge end remote therefrom, characterized by a truncated cone bounding a relatively short segment of the length of said passage, at a location spaced downstream from said passage inlet constructed and arranged to convert kinetic energy in the helical, swirling vortex of flow passing therethrough to pressure energy and produce a resultant application of said con-verted energy to increase the "spin" velocity of said helical swirling flow of said slurry as it moves in said counterflowing vortices within said chamber, said truncated cone having its minimum diameter end upstream from its maximum diameter end .
. , lZZ~659 and having a cone angle as measured from its center line to its outer peripheral limit in the range from about 40 to about 80.
In a further broad aspect, the invention resides in apparatus for connection with the housing of a hydrocyclone to define an~outlet from its separating chamber for receiving a sub-stantially helical, swirling vortex flow therefrom comprising a body for connection to the housing, said body having therein a flow passage the inlet to which in connection thereof to the hydrocyclone housing opens to its separating chamber, said flow passage having a discharge end, characterized in that said flow passage has an upstream portion, a downstream and a truncated cone portion disposed intermediate therebetween, said upstream portion having a cross-sectional area smaller in dimension than the cross-sectional area of said downstream portion, said truncated cone portion having a minimum diameter end opening to said upstream portion and a maximum diameter end opening to said downstream portion, said truncated cone having a cone angle as measured from its center line to its outer peripheral limit in the range from about 40 to about 80.
With the above and other incidental objects in view as will more fully appear in the specification, the invention intended to be protected by Letters Patent consists of the features of construction, the parts and combinations thereof, and the mode of operation as hereinafter described or illustrated in the accompanying drawings, or their equivalents.
A
12;~1659 Referring to the drawings wherein are shown one or more embodiments of the present invention, Figures 1-4 each schematically exhibit the application of an overflow tube to a hydrocyclone having a form and construc-tion and composition which is basically similar but somewhat different in each of the illustrations.
Like parts are indicated by similar characters of refer-ence throughout the several views.
As noted previously, the invention is herein illustrated and described with particular reference to its application to a hydrocyclone of the type advantageously used for the processing of the contents of a pulp slurry.
The embodiment of Figure 1 illustrates a hydrocyclone of this type the body or housing of which comprises an integral tubular shell-like peripheral wall structure 10 one longitudinally extending section 12 of the length of which is - 7a -,.
12~6S9 cylindrical in configur~tion. The dia~eter of the cross section of the section 12 is uniform the lensth thereof.
The section 12 has one end thereof integrated with and longi-tudinally extended by a coaxial section 14 of the tubular wall structure 10. The section 14 which is thus a direct extension of the section 12 has the shape of a truncated cone which conically converges from the end of the section 12 with which it is integrally connected. The truncated apex end of the section 14 rims a small diameter opPning 16 at this end of the tubular wall structure 10.
Connected with and in bridging relation to the end 18 of the section 12 which is remote from the section 14 is an annular plate 20. The outer limit of plate 20 is fixed in a sealed tight relation to the end 18 of section 12 and i~s inner limit is fixed about and in a sealed tight relation to the outer wall surface of a tubular overflow structure, hereinafter referred to as an overflow tube 22.
A short tube 24 has one end thereof intesrally connected to the section 12 immediately of the plate 20 to have what constitutes its discharge end rim an inlet opening 26 in the wall structure 10. The short tube 24 is so related to the opening 26 and the opening 26 so related to the inner sur-face of the wall structure 10 as to provide a tangential inlet to the separating chamber 28 which is defined by the plate 20 and the wall structure 10.
As is well recognized by those versed in the pulp pro-cessing art, the plate 20 defines the overflow end of the ~2Z1659 separating chamber 28 while the opening at the convergent end of the ~Yall section 14 defines what is considered to be the underflow end and outlet 16 from the chamber 28. Correspondingly, the overflow tube 22 defines an overflow passage 30 leadins from and communicating at its inlet end with the separating chamber 28.
As seen in Fig. 1, the overflow tube 22 is coaxi~lly aligned with the underflow outlet 16. Furthermore, the inner wall surface of the overflow tube 22 is so constructed that the overflow pas-sage 30 has a central longitudinal axis the configux~ion of which is that of a straight line. As the overflow tu~e 22 is applied to the hydrocyclone in Fig. 1, its extremity which is innermost of the chamber 28 occupies a plane commonly occupied by the in-tegrated ends of the sections 12 and 14 of the wall structure 10.
Correspondingly, the innermost extremity of the overflow tube 22 rims the inlet opening 23 to its overflow passage 30. This in-let end of the passage 30 exhibits the diameter of a segment 32 of the length of the overflow passage which extends from its in-let end to a plane transversely of and perpendicular to the cen-tral longitudinal axis of the chamber 28 which is parallel to the plane of the inlet end and spaced therefrom slightly more than one-half the distance between the inlet end and the outer-most surface of the plate 20. The segment 32 of the passage 30 has a uniform but relatively small diameter and is immediately followed by a segment 34 of the passage 30 which is very short in length. The portion of the inner wall surface of the tube 22 bounding the se~ment 34 has and provides the segment 34 with a configuration corresponding to that of a truncated cone. The cross sectional ar~a exhibited by one end of this truncated cone has a diameter corresponding to that of the segment 32 of the overflow passage which is immediately upstream _ g _ ~ Z2~i9 thereof and opens thereto. From the segment 32 the segment 34 is configured to conically expand as its larger diameter extremity connects to the immediately downstream segment 36 of the overflow passage 30. of course the largest diameter of the segment 34 corresponds to the diameter of the section 3~ of the overflow passace, which is uniform along its length.
Thus, the overflow tube 22 has an inner wall surface which is stepped as to its diameter along the length thereof, thereby to provide an upstream segment 32 and a downstream sesment 36 of the overflow passage spaced by the interposed conical segment 34.
As shown in Fig. 1, the thickness of the wall 40 of the overflow tube 22 is uniform except at its inlet end 42, where its outer surface expands to produce thereon a bell-shape i~mediately a~out the inlet to the overflow passage.
Accordingly, except for the bell-shaped modification at its inlet end, the outer wall surface of the overflow tube has a configuration along its length which corresponds in all respects with the configuration of its inner wall sur-face which defines the overflow passage. Further notingFig. 1, the overflow tube 22, as shown, has its enlarged diameter end projected outwardly of the plate 20 a limited extent and perpendicular thereto.
~ig. 2 shows a hydrocyc}one structure identical to that shown in and described with reference to Fig. 1 except for the construction and relative position of the illustrated overflow tube and the lensth of the section 12 of the wall ~ 'ZZ16S~
structure 10 being somewhat shorter than that illustrated in ~ig. 1. In Fig. 2 the overflow tu~e 52 of the hydrocyclone is distinguished by a uniformly cylindrical outer wall sur-face S0 the diameter of which is uniform from one end thereof to the other. ~.lso, the overflow tube 52 is so positioned in its perpendicular relation to the plate 20 that its re-spective ends are substantially equidistantly spaced from the adjacent surfaces of the plate 20 and its innermost ex-tremity is spaced longitudinally and outwardly from the plane transversely of and perpendicular to the longitudi-nal axis of the separating chamber 28 which intersects the connection between the sections 12 and 14 of the wall structure 10. The inner wall surface 58 defining the overflow ox outflow passage 60 of the overflow tube 52 has the same general configuration as the inner wall sur-face of the overflow tube 22 but differs in that here the length of the smaller diameter upstream segment of the overflow passage which corresponds to the segment 32 of Pig. 1 is shorter and the length of its larger diameter downstream segment which corresponds to the segment 36 of Fig. 1 is longer than the respective lengths of the corresponding segments of the overflow passage 30 o~ the overflow tune 22.
The hydrocyclone assembly of Pis. 3 is identical to that of Fig. 1 except for the following differences.
12:~659 Its overflow tube 22' which otherwise has a construction and configuration identical with that of the overflow tube 22 differs by reason of the elimination of the bell shape at the mouth of its inlet end. Another difference in the hydrocyclone assembly shown in Fig. 3 from that of Fig. 1 is that its overflow tube is so mounted with reference to the plate 20 to provide that the portion of the wall struc-ture of the overflow tube 22' bounding the segments 34 and 35 of its overflow passage are positioned exteriorly of the plate 20. As a result the opening in the plate 20 is re-duced in diameter sufficient to accommodate and seal about the reduced external diameter portion of the wall of the overflow tube 22' bounding the upstream segment 32 of the overflow passage 30. As may be seen with reference to Fig. 3, the relative position of the overfiow tube 22' provides that the reduced diameter end of the conically configured segment 34 of its overflow passage lies in a plane corresponding to the plane of the outer surface of the plate 20. Note further that in Fig. 3 the axial length of the section 12 of the wall structure 10 is shortened in correspondence with the limited projection of the inlet end portion of the o~erflow tube with ref-erence to the inner surface of the plate 20.
l~:Z~659 In the hydrocyclone modification of Fiq. 4, the con-figuration of the wall structure 10 provides that the sections 12 and 14 thereof are relatively elongated but otherwise ~imilar to the corresponding sections in Fig. 1.
Here, however, rather-than finding a use of a head plate such as the plate 20 incorporated in the embodiments of Figs. 1, 2 and 3, we find the overflow end of the separating chamber 28 defined by the innermost surface 62 of a gener-ally cylindrical body forming a head 64 plug fit in and to the end of the section 12 of wall structure 10 remote from the section 14. The head 64 is configured to provide the overflow end of the hydrocyclone with an axial inlet 66 which is a blind bore parallel. to the central longitudinal axis of its separating chamber 28. m e inlet 66 opens later-ally to one end of a restricted helical flow passage 68 de-fined by the head with the inner wall surface¦of the end of the wall structure 10 in which the head is plug fit. The flow passage 68 is extended and exits to a continuation of its helical form defined by the inner surface 62 of the head which defines the overflow end of the separating chamber 28.
With the arrangement provided, a slurry directed inwardly of the head by way of the inlet 66 will move in a high velocity flow through the passage 68 and in exit from the passage 68 will move over the surface 62 in a continuing helical flow pattern about a central relatively axially projected tubular portion 70 of the head. The tubular projection 70 is thus innermost of.the head 64 and projects .
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122~659 inwardly of the separating chamber from the surface 62 to have its innermost end terminate in a plane parallel to and in an adjacent spaced relation to and short of a plane transverse to the separatinq chamber 28 and perpendicular to its longi-tudinal axis which intersects the wall structure 10 at theconnection between the sections 12 and 14 thereof. The tubular projection 70 defines part of the inlet segment 74 of an overflow passage 72 which is directed through the head from the separating chamber 28. In this case the overflow passage 72 is composed of successive communicating segments a portion of which is angularly diverted and offset from the line of the segment 74 as the overflow passaqe extends through the head to have its outermost segments position parallel to the line of the inlet segment 74.
The segment 76 of the overflow passage 72 immediately following the inlet segment 74 is angularly diverted from the line of segment 74 as it extends outwardly from the separating chamber and forms a continuation of the segment 74. The segments following the segment 76, in succession, which form a continuation thereof and each other, are re-spectively numbered in succession 78, 80 and 82. The seg-.
ments 78, 80 and 82, which have a coaxial alignment, are diverted, commonly, from the line of the segment 76 to extend in a line offset from and parallel to the line of the inlet segment 74. The diameter of the segments 74, 76 and 78 of the overflow passage are essentially the same and these segments are generally elongate, but in the case l;Z Zl~;59 illustrated successively somewhat shorter in length. rrhe segment 80, however, is very short in length and its cross section exhibits the shape of a conically expanding truncated cone. The smallest diameter of this cone is at its end im-mediately of the segment 78 and corresponds in dimension tothe dimension of its diameter. The largest diameter end of the cone of the segment 80 opens to the segment 82 the di-ameter of which corresponds thereto.
The operation of any one of the foregoing embodiments of the invention is essentially the same, as are the unexpected benefits and advantages attendant its use. Basically, a slurry the contents of which are to be separated, cleaned and/or classified is in each case directed through the hydrocyclone inlet to the separating chamber 28 to move therein and the length thereof in a helical flow pattern producing counter-10wing vortices which inherently result in a portion of the slurry contents which have the form of fibers and fiber bundles which are light in weight and desirable in form being caused to move to the inner vortex portion of the slurry flow.
As this most desirable portion of the slurry contents reaches the inner vortex portion or core of the cleaner, as a re-sult thereof it will move, inherently, to and through the overflow passage 30, 60, or 82, as the case may be, de-pending upon the modification. The outer portions of the slurry flow will, in the case illustrated, exit from the separating chamber by way of the underflow outlet 16. It has been found in test and by practice that by virtue of ; - ~ 15 -.
.
'' ' ', -'~ '' . ~' ~221659 the inner wall surface of the overflow tube which bounds and defines the configuration of the overflow passage and in particular the inclusion therein of its conical segment 34, 80 there is produced in the flow through the overflow passage the equivalent of a "hydraulic jump". The consequence of this is that there is an actual conversion of kinetic energy to pressure energy in the overflow. This is extremely signif-icant since as far as has been ablP to be determined in any prior art, no one has heretofore achieved "hydraulic jump"
in a flow through a pipe. Apparently no one practicing in applied fluid mechanics has heretofore observed this phenom-ena or contemplated the same in flow through a pipe, either as a scientific curiosity or as a natural phenomena which may be harnessed for beneficial purposes. The construction of an overflow passage as described in reference to each em-bodiment of the invention has been found to serve to make additional energy available and cause the swirl velocity within a hydrocyclone of a given size to be higher than in a hydrocyclone of the same size having a conventional over-flow tube configuration. More than this, the result ofmaking such additional energy available is the production of greater separating and cleaning forces within the sepa-rating chamber of the hydrocyclone.
It has been determined that the expansion of the over-flow passage as here provided triggers a flow condition in the overflow tube that causes a conversion of the kinetic energy to pressure energy with a reasonably high efficiency lZZ1659 estimated at about 75%. As an adjunct to the improved sepa-rating efficiency caused by the incorporation of the inven-tion, there is not only improved cleaning efficiency result-ing but an increase in the throughput as well as the flow rate of a slurry as it is moved through and from a hydro-cyclone per the invention.
Accordingly, common to the various embodiments of the invention illustrated is an expansion from an upstream to a downstream segment of an overflow passage achieved through the medium of a short expanding segment of the overflow pas-sage which has impressive results.
In preferred and effective embodiments of the invention the conically expanded segment 34, 80,of the overflow passage, which is very short in length, has a "free expansion" cone angle expanding down~tream in the direction of flow which can range from about 40 to about 80 as measured from the center line of the truncated conical segment to the conical ~urface defining its expansion and shape.
In most preferred embodiments of the invention, the length of the segment of the overflow passage immediately upstream of the conically expanding segment should be equal to at least three times the dimension of the diameter of the inlet to the overflow passage. Furthermore, it is preferred and most desirable that the extension of the conical segment of the flow passage in the segment of this passage which is immediately downstream thereof should have a length equal to at least twice the dimension of the maximum diameter of the conical segment of the flow passage.
, ~2Zi659 r optimal results, the segments of the overflow passage immediately upstream and downstream of the conically expanding short segment thereof should have a coaxial relation.
As far as the Pxpansion ratio is concerned,for a most signif-icant conversion of kinetic energy to pressure energy in theoverflow passage 30, 82, its diameter downstream of th~ con-ically expanded portion of the flow passage should be from about 1-1/2 to 2 times its diameter immediately upstream thereof. Smaller ratios could provide some benefit but would not achieve the practical gains so advantageous in the use of a hydrocyclone as herein described.
Laboratory tests have established that when a 6" diameter hydrocyclone has an overflow tube construction such as herein described, there is an approximately 15% increase in its feed flow rate as compared to that found in the operation of a hydrocyclone of the same size having the same inlet and out-let sizes and a conventional overflow tube. This increase in flow rate is somewhat larger for smaller diameter hydrocyclones and somewhat less for larger diameter hydrocyclones. In any case, the invention does provide a sisnificant increase in flow rate. At the same time it has been found that the cleaning efficiency is likewise sianificantly improved thereby, by about 7%.
Considering the advantages and benefits of achieving hydraulic jump in the flow throu~h an overflow tube of a hydrocyclone in accordance with the present invention, it follows that one can operate a hydrocyclone using a smaller lZZ1659 diameter for the inlet ~o the overflow tube than would nor-mally be provided and achieve therein better cleaning and separating efficiency with the same overall pressure drop as would be conventionally experienced using a prior art overflow tube. By the same token, one can bave the benefit of the invention and operate a hydrocyclone with a pressure drop reduced, for example, from 35 to 25 p.s.i.g. and still get a cleaninq and separating efficiency equivalent to that found in the operation of a conventionally constructed hydro-cyclone unit wherein the-pressure drop is 35 p.s.i.g. In this latter case, the invention application provides an ad-ditional benefit, namely an approximately 20~ increase in the throughput of the hydrocyclone.
It is noted that the somewhat de~ious overflow passage which is illustrated in the invention em~odiment shown in Fig. 4 of the accompanying drawings has been found to function equally as well as the other embodiments illustrated.
While tbe foregoing sugg~sts certain limitations as to the lengths and diameters of the critical segments of the ovèrflow pas~age, there may be limited deviation therefrom without departing from the principles and basics of the teachiny herein set forth. One caution is definitely to be observed. If the expansion provided in the overflow passage by virtue of the short segment 34, 80, which induces hydraulic jump in flow therethrough, is immediately followed by a sharp turn in the overflow passage, this will be detrimental to the efficiency of the hydrocyclone structure which it services.
' i2Z~659 In summary, simple though the invention might be the advances af~orded thereby are so sisnificant that hydro-cyclones em~odying the same are not only highly advantageous for use in pulp processing systems but they inherently pro-vide means and methods of a highly improved nature which maybe applied to the cleaning of coal, the dressing of minerals, commercial extraction systems, starch processing systems and, for that matter, the removal of light particles from any liquid vehicle.
~0 r'rom the above description it will be apparent that there is thus provided a device of the character described possessing the particular features of advantage before enu-merated as desirable, but which obviously is susceptible of modification in its form, proportions, detail construction and arrangement of parts without departing from the principle involved or sacrificing any of its advantages.
~ 'hile in order to comply with the statute the invention has been described in language more or less specific as to structural features, it is to be understood that the inv~-tion is not limited to the specific features shown, but thatthe means and construction herein disclosed comprise but one of several modes of putting the invention into effect and the invention is therefore claimed in any of its forms or modifications within the legitimate and valid scope of the appended claims.
BACKGROUND OP THE INVENTION:
This invention relates to improvements in hydrocyclones, which includes centrifugal separators and centrifugal clean-ers. Its embodiment provides an improved construction forthe overflow tube of a hydrocyclone which has unexpectedly resulted in the recovery of kinetic energy in the overflow as well as other significant benefits in the performance of the hydrocyclone. ~his is particularly evidenced in the application of the invention to the processing of pulp in a pulp refining operation. Accordingly, the invention will be described in this frame of reference, but only for pur-pose of illustration and not by way of limitation.
A hydrocyclone is a device used for cleaning, separa-tion and/or classification of the contents of a relativefluid mass. As applied to a pulp slurry, the objective in its use is to extract and separate therefrom elements or particles of wood or other fibrous matter in the slurry best suited, and in a form best suited, for use in a par-ticular end product. It has been found in many cases thatthe level and amount of energy required for the operation of prior art hydrocyclones or hydrocyclone systems can be quite substantial. It has also been found that the extent of the pressure drop which occurs in the use of prior art hydrocyclones to process a pulp slurry limits the through-- put of the slurry as well as its flow rate in moving through and from the hydrocyclone. The problems noted are and have been a matter of serious concern for a long period of time.
~r~ ~-"~ ~
~" :
~221659 The prese~t invention not only overcomes the ~oreqoing problems to a substantial degree but its application to any hydrocyclone of a given size provides it with an inherent mode of operation resulting in an increase in its feed 5 - flow rate as well as a significant improvement in its cleaning efficiency. ~s a matter of fact, the application of the invention enables more of the energy applied in use of a hydrocyclone to contribute, very effectively, to the spin of the flow of a slurry introduced to and moved within and longitudinally of the hydrocyclone separating chamber.
The result of this last feature is a cleaner and more ef-fective separation of the contents of the slurry which is subjected to a separating procedure.
As far as novelty is concerned, there is no knowledge of any prior hydrocyclone art which is specific to the improvements of the present invention. A search of the records of the 17. S. Paten~ and Trademark Office appears to confirm this fact. All that the search produced is exemplified by the following patents:
Patent No. Name Date 3,037,628 G. H. Tomlinson II June 5, 1962 3,129,173 W. G. A. Schulze April 14, 1964 3,261,467 N. A. L. Wikdahl July 19, 1966 3,613,887 N. A. L. Wikdahl Oct. 19, 1971 3,746,173 W. H. Daniel July 17, 1973 4,259,180 Jorma Surakka et al M.ar. 31, 1981 .
~ ZZ16S9 S~'.~MARY OF T~IE INVENTION:
Preferred emb~diments of the present invention comprise a hydrocyclone the body of which defines therein a separating chamber having an overflo~ end and an underflow end, an inlet and at least two outlets, one to each of the opposite ends of the ~eparating chamber. One of these outlets provides an underflow outlet and the other an overflow outlet. The inner wall of the hydrocyclone has a tubular configuration and the underflow and overflow outlets are in a substantially coaxial alignment. In the introduction of a pulp slurry, the contents of which are to be separated and/or cleaned or classified, the inlet applies the slurry tangential to thë inner wall surface of the hydrocyclone to develop within its separating chamber a vortex-type flow of the slurry producing counterflowing vortices thereof. The result of the counterflowing vortices is to induce, normally, a particularly desired portion of the contents of the slurry to move to an area within the separating chamber comprising its central longitudinally extending core from which such material is inherently in-duced to flow to and through the overflow outlet of the hydrocyclone. At the same time another portion of the contents of the slurry within the separating cham~er in-cluded in the outer of said counterflowing vortices is caused to move to and through the underflow outlet of the hydrocyclone. In accordance with the invention, the over-~5 flow outlet is defined by an overflow tube structure, here-- inafter referred to as an overflow tube, the diameter of ~ - 3 -t~e inner surface of which is stepped along its length. ks will be obvious, the inner surface of the overflow tube de-fines an overflow passage one end of which communicates with the overflow end of the hydrocyclone separating chamber and the other end of which connects to a conduit or conduits for directing the discharge from the overflow tube to a desired place of storage or use. Per the invention the inner surface of the overflow tube and the overflow passaye which it defines are formed to produce therein a conversion of kinetic energy in flow therethrough from the hydrocyclone separating chamber to pressure energy. This produces inobvious and most ad-vantageous improvements in the performance of the hydrocyclone.
Actually, what has been observed to occur in the use of an overflow tube havina an overflow passage formed in accordance with the invention is a "hydraulic jump" phenomena.
Ihen comparing the operation of a conventional hydro-cyclone having an overflow passage in accordance with the prior art with the operation of a hydrocyclone of the same size embody-ing the invention, it is seen that the use of the invention re-sults in the following benefits and improvements:
a. A decrease in pressure drop in the flow through the hydrocyclone;
b. An increase in the "spin" of the material introduced to and passed through the hydrocyclone separating chamber;
c. A significant increase in the cleaning and sepa-rating efficiency of the hydrocyclone and an increase in its operating capacity and feed flow rate;
d. ~n increase in the throughput or flow rate of the , ' '" ' . ' ' ' ' : '',' ' ~ ..
12Zl~iS9 material to be separated or cleaned in the movement thereof through and from the separating cha~er of the hydrocyclone.
A preferred embodiment of the invention provides that the outflow passage defined by its overflow tube includes straight line segments of its length which are spaced by a relatively short coaxial segment which has the shape of a truncated cone. In this case the upstream of these straight line segments will have a diameter corresponding to the small-est diameter of the relatively short segment which has the confi~uration of a truncated cone while the straight line segment of the outflow passage immediately downstream of this short segment will have a dlameter which is relatively enlarged as compared to that of the upstream segment and corresponds with that of the downstream end of said short segment. In use of this preferred embodiment the efficiency of the operation of a hydrocyclone of a given size is sub-stantially improved and there is a corresponding saving and added utilization of the available energy. A significant aspect of the invention is the economy possible in its em-bodiment.
While in describing the invention reference is madeherein to an overflow tube applied to a conventionally opera-ting hydrocyclone, it is to be understood that an outflow pas-sage of the nature herein described and claimed may be formed in any tube or body structure providing an outlet from the separating cha~er of any type hydrocyclone and ?roduce similar results and benefits in its use.
It is therefore a primary object of the invention to provide economically achieved improvements in hydrocyclones :. -lZZ1659 which are easy to fabricate and which render such devices ~ore efficient and satisfactory in use, adaptable to a wide variety of applications and less likely to adversely function.
In one broad aspect, the invention resides in a hydro-cyclone comprising a housing having a separating chamber, an inlet to said chamber and at least two outlets therefrom, said inlet being constructed and arranged to deliver a slurry or other fluid mass containing solids the contents of which are to be separated, cleaned or classified, to said chamber in a substantially helical, swirling, flow pattern to cause the movement thereof within said chamber in counterflowing vortices inherently causing solids in the flow which are light and relatively small in size to move to the inner vortex of the flow and exit from a first outlet while the remainder of said flow embodying large and heavy solids seeks another outlet from said chamber, said first outlet being a longi-tudinally extended passage having an inlet end open to said separ-ating chamber and a discharge end remote therefrom, characterized by a truncated cone bounding a relatively short segment of the length of said passage, at a location spaced downstream from said passage inlet constructed and arranged to convert kinetic energy in the helical, swirling vortex of flow passing therethrough to pressure energy and produce a resultant application of said con-verted energy to increase the "spin" velocity of said helical swirling flow of said slurry as it moves in said counterflowing vortices within said chamber, said truncated cone having its minimum diameter end upstream from its maximum diameter end .
. , lZZ~659 and having a cone angle as measured from its center line to its outer peripheral limit in the range from about 40 to about 80.
In a further broad aspect, the invention resides in apparatus for connection with the housing of a hydrocyclone to define an~outlet from its separating chamber for receiving a sub-stantially helical, swirling vortex flow therefrom comprising a body for connection to the housing, said body having therein a flow passage the inlet to which in connection thereof to the hydrocyclone housing opens to its separating chamber, said flow passage having a discharge end, characterized in that said flow passage has an upstream portion, a downstream and a truncated cone portion disposed intermediate therebetween, said upstream portion having a cross-sectional area smaller in dimension than the cross-sectional area of said downstream portion, said truncated cone portion having a minimum diameter end opening to said upstream portion and a maximum diameter end opening to said downstream portion, said truncated cone having a cone angle as measured from its center line to its outer peripheral limit in the range from about 40 to about 80.
With the above and other incidental objects in view as will more fully appear in the specification, the invention intended to be protected by Letters Patent consists of the features of construction, the parts and combinations thereof, and the mode of operation as hereinafter described or illustrated in the accompanying drawings, or their equivalents.
A
12;~1659 Referring to the drawings wherein are shown one or more embodiments of the present invention, Figures 1-4 each schematically exhibit the application of an overflow tube to a hydrocyclone having a form and construc-tion and composition which is basically similar but somewhat different in each of the illustrations.
Like parts are indicated by similar characters of refer-ence throughout the several views.
As noted previously, the invention is herein illustrated and described with particular reference to its application to a hydrocyclone of the type advantageously used for the processing of the contents of a pulp slurry.
The embodiment of Figure 1 illustrates a hydrocyclone of this type the body or housing of which comprises an integral tubular shell-like peripheral wall structure 10 one longitudinally extending section 12 of the length of which is - 7a -,.
12~6S9 cylindrical in configur~tion. The dia~eter of the cross section of the section 12 is uniform the lensth thereof.
The section 12 has one end thereof integrated with and longi-tudinally extended by a coaxial section 14 of the tubular wall structure 10. The section 14 which is thus a direct extension of the section 12 has the shape of a truncated cone which conically converges from the end of the section 12 with which it is integrally connected. The truncated apex end of the section 14 rims a small diameter opPning 16 at this end of the tubular wall structure 10.
Connected with and in bridging relation to the end 18 of the section 12 which is remote from the section 14 is an annular plate 20. The outer limit of plate 20 is fixed in a sealed tight relation to the end 18 of section 12 and i~s inner limit is fixed about and in a sealed tight relation to the outer wall surface of a tubular overflow structure, hereinafter referred to as an overflow tube 22.
A short tube 24 has one end thereof intesrally connected to the section 12 immediately of the plate 20 to have what constitutes its discharge end rim an inlet opening 26 in the wall structure 10. The short tube 24 is so related to the opening 26 and the opening 26 so related to the inner sur-face of the wall structure 10 as to provide a tangential inlet to the separating chamber 28 which is defined by the plate 20 and the wall structure 10.
As is well recognized by those versed in the pulp pro-cessing art, the plate 20 defines the overflow end of the ~2Z1659 separating chamber 28 while the opening at the convergent end of the ~Yall section 14 defines what is considered to be the underflow end and outlet 16 from the chamber 28. Correspondingly, the overflow tube 22 defines an overflow passage 30 leadins from and communicating at its inlet end with the separating chamber 28.
As seen in Fig. 1, the overflow tube 22 is coaxi~lly aligned with the underflow outlet 16. Furthermore, the inner wall surface of the overflow tube 22 is so constructed that the overflow pas-sage 30 has a central longitudinal axis the configux~ion of which is that of a straight line. As the overflow tu~e 22 is applied to the hydrocyclone in Fig. 1, its extremity which is innermost of the chamber 28 occupies a plane commonly occupied by the in-tegrated ends of the sections 12 and 14 of the wall structure 10.
Correspondingly, the innermost extremity of the overflow tube 22 rims the inlet opening 23 to its overflow passage 30. This in-let end of the passage 30 exhibits the diameter of a segment 32 of the length of the overflow passage which extends from its in-let end to a plane transversely of and perpendicular to the cen-tral longitudinal axis of the chamber 28 which is parallel to the plane of the inlet end and spaced therefrom slightly more than one-half the distance between the inlet end and the outer-most surface of the plate 20. The segment 32 of the passage 30 has a uniform but relatively small diameter and is immediately followed by a segment 34 of the passage 30 which is very short in length. The portion of the inner wall surface of the tube 22 bounding the se~ment 34 has and provides the segment 34 with a configuration corresponding to that of a truncated cone. The cross sectional ar~a exhibited by one end of this truncated cone has a diameter corresponding to that of the segment 32 of the overflow passage which is immediately upstream _ g _ ~ Z2~i9 thereof and opens thereto. From the segment 32 the segment 34 is configured to conically expand as its larger diameter extremity connects to the immediately downstream segment 36 of the overflow passage 30. of course the largest diameter of the segment 34 corresponds to the diameter of the section 3~ of the overflow passace, which is uniform along its length.
Thus, the overflow tube 22 has an inner wall surface which is stepped as to its diameter along the length thereof, thereby to provide an upstream segment 32 and a downstream sesment 36 of the overflow passage spaced by the interposed conical segment 34.
As shown in Fig. 1, the thickness of the wall 40 of the overflow tube 22 is uniform except at its inlet end 42, where its outer surface expands to produce thereon a bell-shape i~mediately a~out the inlet to the overflow passage.
Accordingly, except for the bell-shaped modification at its inlet end, the outer wall surface of the overflow tube has a configuration along its length which corresponds in all respects with the configuration of its inner wall sur-face which defines the overflow passage. Further notingFig. 1, the overflow tube 22, as shown, has its enlarged diameter end projected outwardly of the plate 20 a limited extent and perpendicular thereto.
~ig. 2 shows a hydrocyc}one structure identical to that shown in and described with reference to Fig. 1 except for the construction and relative position of the illustrated overflow tube and the lensth of the section 12 of the wall ~ 'ZZ16S~
structure 10 being somewhat shorter than that illustrated in ~ig. 1. In Fig. 2 the overflow tu~e 52 of the hydrocyclone is distinguished by a uniformly cylindrical outer wall sur-face S0 the diameter of which is uniform from one end thereof to the other. ~.lso, the overflow tube 52 is so positioned in its perpendicular relation to the plate 20 that its re-spective ends are substantially equidistantly spaced from the adjacent surfaces of the plate 20 and its innermost ex-tremity is spaced longitudinally and outwardly from the plane transversely of and perpendicular to the longitudi-nal axis of the separating chamber 28 which intersects the connection between the sections 12 and 14 of the wall structure 10. The inner wall surface 58 defining the overflow ox outflow passage 60 of the overflow tube 52 has the same general configuration as the inner wall sur-face of the overflow tube 22 but differs in that here the length of the smaller diameter upstream segment of the overflow passage which corresponds to the segment 32 of Pig. 1 is shorter and the length of its larger diameter downstream segment which corresponds to the segment 36 of Fig. 1 is longer than the respective lengths of the corresponding segments of the overflow passage 30 o~ the overflow tune 22.
The hydrocyclone assembly of Pis. 3 is identical to that of Fig. 1 except for the following differences.
12:~659 Its overflow tube 22' which otherwise has a construction and configuration identical with that of the overflow tube 22 differs by reason of the elimination of the bell shape at the mouth of its inlet end. Another difference in the hydrocyclone assembly shown in Fig. 3 from that of Fig. 1 is that its overflow tube is so mounted with reference to the plate 20 to provide that the portion of the wall struc-ture of the overflow tube 22' bounding the segments 34 and 35 of its overflow passage are positioned exteriorly of the plate 20. As a result the opening in the plate 20 is re-duced in diameter sufficient to accommodate and seal about the reduced external diameter portion of the wall of the overflow tube 22' bounding the upstream segment 32 of the overflow passage 30. As may be seen with reference to Fig. 3, the relative position of the overfiow tube 22' provides that the reduced diameter end of the conically configured segment 34 of its overflow passage lies in a plane corresponding to the plane of the outer surface of the plate 20. Note further that in Fig. 3 the axial length of the section 12 of the wall structure 10 is shortened in correspondence with the limited projection of the inlet end portion of the o~erflow tube with ref-erence to the inner surface of the plate 20.
l~:Z~659 In the hydrocyclone modification of Fiq. 4, the con-figuration of the wall structure 10 provides that the sections 12 and 14 thereof are relatively elongated but otherwise ~imilar to the corresponding sections in Fig. 1.
Here, however, rather-than finding a use of a head plate such as the plate 20 incorporated in the embodiments of Figs. 1, 2 and 3, we find the overflow end of the separating chamber 28 defined by the innermost surface 62 of a gener-ally cylindrical body forming a head 64 plug fit in and to the end of the section 12 of wall structure 10 remote from the section 14. The head 64 is configured to provide the overflow end of the hydrocyclone with an axial inlet 66 which is a blind bore parallel. to the central longitudinal axis of its separating chamber 28. m e inlet 66 opens later-ally to one end of a restricted helical flow passage 68 de-fined by the head with the inner wall surface¦of the end of the wall structure 10 in which the head is plug fit. The flow passage 68 is extended and exits to a continuation of its helical form defined by the inner surface 62 of the head which defines the overflow end of the separating chamber 28.
With the arrangement provided, a slurry directed inwardly of the head by way of the inlet 66 will move in a high velocity flow through the passage 68 and in exit from the passage 68 will move over the surface 62 in a continuing helical flow pattern about a central relatively axially projected tubular portion 70 of the head. The tubular projection 70 is thus innermost of.the head 64 and projects .
- . :
- . .
.
122~659 inwardly of the separating chamber from the surface 62 to have its innermost end terminate in a plane parallel to and in an adjacent spaced relation to and short of a plane transverse to the separatinq chamber 28 and perpendicular to its longi-tudinal axis which intersects the wall structure 10 at theconnection between the sections 12 and 14 thereof. The tubular projection 70 defines part of the inlet segment 74 of an overflow passage 72 which is directed through the head from the separating chamber 28. In this case the overflow passage 72 is composed of successive communicating segments a portion of which is angularly diverted and offset from the line of the segment 74 as the overflow passaqe extends through the head to have its outermost segments position parallel to the line of the inlet segment 74.
The segment 76 of the overflow passage 72 immediately following the inlet segment 74 is angularly diverted from the line of segment 74 as it extends outwardly from the separating chamber and forms a continuation of the segment 74. The segments following the segment 76, in succession, which form a continuation thereof and each other, are re-spectively numbered in succession 78, 80 and 82. The seg-.
ments 78, 80 and 82, which have a coaxial alignment, are diverted, commonly, from the line of the segment 76 to extend in a line offset from and parallel to the line of the inlet segment 74. The diameter of the segments 74, 76 and 78 of the overflow passage are essentially the same and these segments are generally elongate, but in the case l;Z Zl~;59 illustrated successively somewhat shorter in length. rrhe segment 80, however, is very short in length and its cross section exhibits the shape of a conically expanding truncated cone. The smallest diameter of this cone is at its end im-mediately of the segment 78 and corresponds in dimension tothe dimension of its diameter. The largest diameter end of the cone of the segment 80 opens to the segment 82 the di-ameter of which corresponds thereto.
The operation of any one of the foregoing embodiments of the invention is essentially the same, as are the unexpected benefits and advantages attendant its use. Basically, a slurry the contents of which are to be separated, cleaned and/or classified is in each case directed through the hydrocyclone inlet to the separating chamber 28 to move therein and the length thereof in a helical flow pattern producing counter-10wing vortices which inherently result in a portion of the slurry contents which have the form of fibers and fiber bundles which are light in weight and desirable in form being caused to move to the inner vortex portion of the slurry flow.
As this most desirable portion of the slurry contents reaches the inner vortex portion or core of the cleaner, as a re-sult thereof it will move, inherently, to and through the overflow passage 30, 60, or 82, as the case may be, de-pending upon the modification. The outer portions of the slurry flow will, in the case illustrated, exit from the separating chamber by way of the underflow outlet 16. It has been found in test and by practice that by virtue of ; - ~ 15 -.
.
'' ' ', -'~ '' . ~' ~221659 the inner wall surface of the overflow tube which bounds and defines the configuration of the overflow passage and in particular the inclusion therein of its conical segment 34, 80 there is produced in the flow through the overflow passage the equivalent of a "hydraulic jump". The consequence of this is that there is an actual conversion of kinetic energy to pressure energy in the overflow. This is extremely signif-icant since as far as has been ablP to be determined in any prior art, no one has heretofore achieved "hydraulic jump"
in a flow through a pipe. Apparently no one practicing in applied fluid mechanics has heretofore observed this phenom-ena or contemplated the same in flow through a pipe, either as a scientific curiosity or as a natural phenomena which may be harnessed for beneficial purposes. The construction of an overflow passage as described in reference to each em-bodiment of the invention has been found to serve to make additional energy available and cause the swirl velocity within a hydrocyclone of a given size to be higher than in a hydrocyclone of the same size having a conventional over-flow tube configuration. More than this, the result ofmaking such additional energy available is the production of greater separating and cleaning forces within the sepa-rating chamber of the hydrocyclone.
It has been determined that the expansion of the over-flow passage as here provided triggers a flow condition in the overflow tube that causes a conversion of the kinetic energy to pressure energy with a reasonably high efficiency lZZ1659 estimated at about 75%. As an adjunct to the improved sepa-rating efficiency caused by the incorporation of the inven-tion, there is not only improved cleaning efficiency result-ing but an increase in the throughput as well as the flow rate of a slurry as it is moved through and from a hydro-cyclone per the invention.
Accordingly, common to the various embodiments of the invention illustrated is an expansion from an upstream to a downstream segment of an overflow passage achieved through the medium of a short expanding segment of the overflow pas-sage which has impressive results.
In preferred and effective embodiments of the invention the conically expanded segment 34, 80,of the overflow passage, which is very short in length, has a "free expansion" cone angle expanding down~tream in the direction of flow which can range from about 40 to about 80 as measured from the center line of the truncated conical segment to the conical ~urface defining its expansion and shape.
In most preferred embodiments of the invention, the length of the segment of the overflow passage immediately upstream of the conically expanding segment should be equal to at least three times the dimension of the diameter of the inlet to the overflow passage. Furthermore, it is preferred and most desirable that the extension of the conical segment of the flow passage in the segment of this passage which is immediately downstream thereof should have a length equal to at least twice the dimension of the maximum diameter of the conical segment of the flow passage.
, ~2Zi659 r optimal results, the segments of the overflow passage immediately upstream and downstream of the conically expanding short segment thereof should have a coaxial relation.
As far as the Pxpansion ratio is concerned,for a most signif-icant conversion of kinetic energy to pressure energy in theoverflow passage 30, 82, its diameter downstream of th~ con-ically expanded portion of the flow passage should be from about 1-1/2 to 2 times its diameter immediately upstream thereof. Smaller ratios could provide some benefit but would not achieve the practical gains so advantageous in the use of a hydrocyclone as herein described.
Laboratory tests have established that when a 6" diameter hydrocyclone has an overflow tube construction such as herein described, there is an approximately 15% increase in its feed flow rate as compared to that found in the operation of a hydrocyclone of the same size having the same inlet and out-let sizes and a conventional overflow tube. This increase in flow rate is somewhat larger for smaller diameter hydrocyclones and somewhat less for larger diameter hydrocyclones. In any case, the invention does provide a sisnificant increase in flow rate. At the same time it has been found that the cleaning efficiency is likewise sianificantly improved thereby, by about 7%.
Considering the advantages and benefits of achieving hydraulic jump in the flow throu~h an overflow tube of a hydrocyclone in accordance with the present invention, it follows that one can operate a hydrocyclone using a smaller lZZ1659 diameter for the inlet ~o the overflow tube than would nor-mally be provided and achieve therein better cleaning and separating efficiency with the same overall pressure drop as would be conventionally experienced using a prior art overflow tube. By the same token, one can bave the benefit of the invention and operate a hydrocyclone with a pressure drop reduced, for example, from 35 to 25 p.s.i.g. and still get a cleaninq and separating efficiency equivalent to that found in the operation of a conventionally constructed hydro-cyclone unit wherein the-pressure drop is 35 p.s.i.g. In this latter case, the invention application provides an ad-ditional benefit, namely an approximately 20~ increase in the throughput of the hydrocyclone.
It is noted that the somewhat de~ious overflow passage which is illustrated in the invention em~odiment shown in Fig. 4 of the accompanying drawings has been found to function equally as well as the other embodiments illustrated.
While tbe foregoing sugg~sts certain limitations as to the lengths and diameters of the critical segments of the ovèrflow pas~age, there may be limited deviation therefrom without departing from the principles and basics of the teachiny herein set forth. One caution is definitely to be observed. If the expansion provided in the overflow passage by virtue of the short segment 34, 80, which induces hydraulic jump in flow therethrough, is immediately followed by a sharp turn in the overflow passage, this will be detrimental to the efficiency of the hydrocyclone structure which it services.
' i2Z~659 In summary, simple though the invention might be the advances af~orded thereby are so sisnificant that hydro-cyclones em~odying the same are not only highly advantageous for use in pulp processing systems but they inherently pro-vide means and methods of a highly improved nature which maybe applied to the cleaning of coal, the dressing of minerals, commercial extraction systems, starch processing systems and, for that matter, the removal of light particles from any liquid vehicle.
~0 r'rom the above description it will be apparent that there is thus provided a device of the character described possessing the particular features of advantage before enu-merated as desirable, but which obviously is susceptible of modification in its form, proportions, detail construction and arrangement of parts without departing from the principle involved or sacrificing any of its advantages.
~ 'hile in order to comply with the statute the invention has been described in language more or less specific as to structural features, it is to be understood that the inv~-tion is not limited to the specific features shown, but thatthe means and construction herein disclosed comprise but one of several modes of putting the invention into effect and the invention is therefore claimed in any of its forms or modifications within the legitimate and valid scope of the appended claims.
Claims (11)
PROPERTY OR PRIVILEGE IS CLAIMED ARE DEFINED AS FOLLOWS:
1. A hydrocyclone comprising a housing having a separating chamber, an inlet to said chamber and at least two outlets there-from, said inlet being constructed and arranged to deliver a slurry or other fluid mass containing solids the contents of which are to be separated, cleaned or classified, to said chamber in a substantially helical, swirling, flow pattern to cause the move-ment thereof within said chamber in counterflowing vortices inherently causing solids in the flow which are light and rela-tively small in size to move to the inner vortex of the flow and exit from a first outlet while the remainder of said flow embodying large and heavy solids seeks another outlet from said chamber, said first outlet being a longitudinally extended passage having an inlet end open to said separating chamber and a dis-charge end remote therefrom, characterized by a truncated cone bounding a relatively short segment of the length of said passage, at a location spaced downstream from said passage inlet construc-ted and arranged to convert kinetic energy in the helical, swirling vortex of flow passing therethrough to pressure energy and produce a resultant application of said converted energy to increase the "spin" velocity of said helical swirling flow of said slurry as it moves in said counterflowing vortices within said chamber, said truncated cone having its minimum diameter end upstream from its maximum diameter end and having a cone angle as measured from its center line to its outer peripheral limit in the range from about 40° to about 80°.
2. Apparatus as in claim 1 characterized in that a segment of said passage immediately upstream of said truncated cone has a diameter which corresponds, substantially, to the diameter of the upstream end of said truncated cone and a segment of said passage immediately downstream of said truncated cone has a diameter corresponding, substantially, to that of the downstream end of said truncated cone.
3. A hydrocyclone as in claim 1 characterized in that said truncated cone is interposed between and forms a continuation of segments of said passage which are respectively immediately upstream and immediately downstream thereof and said segments are arranged in a substantially coaxially aligned relation.
4. A hydrocyclone as in claim 1 characterized in that said truncated cone is interposed between and forms a continuation of an upstream segment of said passage and a further continuation thereof provided by a segment of the length of said passage which is immediately downstream of said truncated cone and the length of said upstream segment has a dimension which is at least equal to about three times the diameter of the inlet to said passage.
5. A hydrocyclone as in claim 1 characterized in that said truncated cone is interposed between and forms a continuation of segments of said passage which are respectively immediately up-stream and immediately downstream thereof and the dimension of the diameter of said downstream segment is from about 1.5 to about 2.0 times the dimension of the diameter of said upstream segment.
6. A hydrocyclone as in claim 5 characterized in that the length of said upstream segment is equal in dimension to at least about three times the diameter of the inlet to said passage.
7. A hydrocyclone as in claim 1 characterized in that said longitudinally extended passage providing said one outlet is bounded by a wall surface which is generally circular in cross-section the diameter of which is stepped along the length of said passage and said truncated cone is a portion of the length of said bounding wall surface located intermediate and spaced from its respective ends.
8. Apparatus for connection with the housing of a hydro-cyclone to define an accepts outlet from its separating chamber for receiving a substantially helical, swirling inner vortex flow therefrom comprising a body for connection to the housing, said body having therein a flow passage the inlet to which in connection thereof to the hydrocyclone housing opens to its separating chamber for receiving the inner vortex flow of accepts solids, said flow passage having a discharge end, char-acterized in that said flow passage has an upstream portion, a downstream and a truncated cone portion disposed intermediate therebetween, said upstream portion having a cross-sectional area smaller in dimension than the cross-sectional area of said downstream portion, said truncated cone portion having a min-imum diameter end opening to said upstream portion and a max-imum diameter end opening to said downstream portion, said truncated cone having a cone angle as measured from its center line to its outer peripheral limit in the range from about 40°
to about 80°.
to about 80°.
9. Apparatus as in claim 8 characterized in that said truncated cone portion is interposed between and forms a con-tinuation of said upstream and downstream portions and said up-stream portion, at the end thereof which connects with said truncated cone portion, has a length which is at least equal to about three times that of the diameter of the inlet to said flow passage.
10. Apparatus as in claim 8 characterized in that said truncated cone portion is interposed between and forms a con-tinuation of upstream and downstream portions and the dimension of the diameter of said downstream portion is from about 1.5 to 2.0 times the dimension of the diameter of said upstream portion.
11. Apparatus as in claim 8 characterized in that said flow passage is pipe-like in form the length thereof and the diameter thereof adjacent its inlet end is less than the dia-meter thereof adjacent its remote discharge end and said trun-cated cone is located intermediate the ends of said flow passage.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PCT/US1982/000605 WO1983003986A1 (en) | 1982-05-07 | 1982-05-07 | Hydrocyclone featuring hydraulic jump in overflow passage |
| US82/00605 | 1982-05-07 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA1221659A true CA1221659A (en) | 1987-05-12 |
Family
ID=22167971
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA000426450A Expired CA1221659A (en) | 1982-05-07 | 1983-04-21 | Hydrocyclone featuring hydraulic jump in overflow passage |
Country Status (4)
| Country | Link |
|---|---|
| EP (1) | EP0108058A4 (en) |
| CA (1) | CA1221659A (en) |
| FI (1) | FI834886A (en) |
| WO (1) | WO1983003986A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AU616800B2 (en) * | 1988-09-22 | 1991-11-07 | Shell Internationale Research Maatschappij B.V. | Swirl tube separator |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB8713308D0 (en) * | 1987-06-06 | 1987-07-08 | Clean Water Co Ltd | Separators |
| DE102008057339A1 (en) * | 2008-11-14 | 2010-05-20 | Voith Patent Gmbh | hydrocyclone |
| CN108970817A (en) * | 2017-07-31 | 2018-12-11 | 安徽联河股份有限公司 | It is a kind of for separating the cyclone of rice starch and rice gluten |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2816490A (en) * | 1952-09-24 | 1957-12-17 | Nichols Engineering And Res Co | Apparatus for treating liquid mixtures for separation of solid particles and gases |
| BE544291A (en) * | 1955-03-10 | 1900-01-01 | Horace Freeman | |
| US3057476A (en) * | 1959-05-29 | 1962-10-09 | Charles Augustus Mcclure | Hydrocyclones |
| US3114510A (en) * | 1961-03-01 | 1963-12-17 | Duval Sulphur & Potash Company | Sensing and control apparatus for classifiers |
| US3501014A (en) * | 1968-06-13 | 1970-03-17 | Univ Oklahoma State | Regenerative hydrocyclone |
-
1982
- 1982-05-07 WO PCT/US1982/000605 patent/WO1983003986A1/en not_active Application Discontinuation
- 1982-05-07 EP EP19820902004 patent/EP0108058A4/en not_active Withdrawn
-
1983
- 1983-04-21 CA CA000426450A patent/CA1221659A/en not_active Expired
- 1983-12-30 FI FI834886A patent/FI834886A/en not_active Application Discontinuation
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AU616800B2 (en) * | 1988-09-22 | 1991-11-07 | Shell Internationale Research Maatschappij B.V. | Swirl tube separator |
Also Published As
| Publication number | Publication date |
|---|---|
| WO1983003986A1 (en) | 1983-11-24 |
| EP0108058A4 (en) | 1985-06-26 |
| FI834886A0 (en) | 1983-12-30 |
| EP0108058A1 (en) | 1984-05-16 |
| FI834886A (en) | 1983-12-30 |
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| Date | Code | Title | Description |
|---|---|---|---|
| MKEX | Expiry |