CA1144056A - Continuous packed bed wash column - Google Patents
Continuous packed bed wash columnInfo
- Publication number
- CA1144056A CA1144056A CA000330643A CA330643A CA1144056A CA 1144056 A CA1144056 A CA 1144056A CA 000330643 A CA000330643 A CA 000330643A CA 330643 A CA330643 A CA 330643A CA 1144056 A CA1144056 A CA 1144056A
- Authority
- CA
- Canada
- Prior art keywords
- ice crystals
- packed bed
- aqueous solution
- slurry
- washfront
- 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
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/22—Treatment of water, waste water, or sewage by freezing
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D9/00—Crystallisation
- B01D9/004—Fractional crystallisation; Fractionating or rectifying columns
- B01D9/0045—Washing of crystals, e.g. in wash columns
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D9/00—Crystallisation
- B01D9/02—Crystallisation from solutions
- B01D9/04—Crystallisation from solutions concentrating solutions by removing frozen solvent therefrom
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Crystallography & Structural Chemistry (AREA)
- Organic Chemistry (AREA)
- Water Supply & Treatment (AREA)
- Environmental & Geological Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Hydrology & Water Resources (AREA)
- Physical Water Treatments (AREA)
- Non-Alcoholic Beverages (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Meat, Egg Or Seafood Products (AREA)
- Centrifugal Separators (AREA)
Abstract
ABSTRACT OF THE DISCLOSURE
Process for separating the ice crystals contained in a slurry of an aqueous solution and ice crystals from said aqueous solution and washing said ice crystals with an aqueous wash liquid, whereby a packed bed of ice crystals is created which is subjected to a continuous translatory movement, while a washfront is being created within said packed bed of ice crystals between said aqueous solution and said aqueous wash liquid, said aqueous solution and said aqueous wash liquid adjacent to said washfront being sub-stantially stagnant, a stable washfront being created lying in a straight plane perpendicular to said translatory movement of said packed bed of ice crystals.
Process for separating the ice crystals contained in a slurry of an aqueous solution and ice crystals from said aqueous solution and washing said ice crystals with an aqueous wash liquid, whereby a packed bed of ice crystals is created which is subjected to a continuous translatory movement, while a washfront is being created within said packed bed of ice crystals between said aqueous solution and said aqueous wash liquid, said aqueous solution and said aqueous wash liquid adjacent to said washfront being sub-stantially stagnant, a stable washfront being created lying in a straight plane perpendicular to said translatory movement of said packed bed of ice crystals.
Description
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This invention relates generally to a continuous process and apparatus for separating the ice crystals con-tained in a slurry of an aqueous solution and ice crystals from said aqueous solution and washing said ice crystals with an aqueous wash liquid. Normally this aqueous wash liquid will be water, but multi stage processes are possible whereby the wash liquid in any particular stage is the aqueous solution withdrawn from a succeeding stage. This kind of slurry occurs in industrial processes whereby either the aqueous solution is recovered as a product and the ice crystals are rejected, or conversely, whereby the ice crystals are recovered as a product and the aqueous solution is rejected. A process of -the first kind in the food industry is the freeze concen-tration of aqueous liquids such as fruit, juices, beer, wine and coffee extract. A process of the second kind is the freeze concentration of sea water to produce fresh water; in this process the brine is rejected and the ice crystals are recovered and melted.
A continuous packed bed wash column is described in U.S.P. 3,587,859 (Probstein), specifically for producing fresh water from sea water. In this wash column a porous bed of particles ice crystals is formed and the liquid medium brine is caused to flow outwardly from the column at a screened opening positioned intermediate its ends. A wash liquid is introduced at one end of the column to displace the liquid medium from the interstices between the particles as the porous bed moves continuously through the column.
Control means are provided to control the relationship among the liquid pressures at the ends of the porous bed and the pressure at such screened opening so as to maximize the rate at which the particles can be removed at the output end of .~
i6 the column.
In operating this kind of apparatus the two main difficulties are freezing of the screen producing breakdown of the operation and losses occurring by the mixing of the aqueous solution between the ice crystals and the wash liquid. These losses are exacerbated by the phenomenon of channeling. This phenomenon entails the formation of "channels" in the bed of ice crystals, through which wash liquid escapes. When e.g. liquld foodstuffs are being concentrated the concentration is partly undone, and in the case of sea water desalination fresh water is lost, as it mingles with the concentrated brine which is being rejected.
Moreover wash liquid reaching the screen has the tendency to produce clogging. The wash liquid has a higher freezing point than the concentrated solution. The screen is cooled by this concentrated solution and the wash liquid coming in contact with the screen will freeze and, as said, produce clogging, eventually bringing the process to a halt.
The difficulties associated with freezing up of the 20 screen have been well described in U.S.P. 3,885,399 and 3,992,900 (Campbell, assigned to Avco Corp.). Reference is made specially to column 1, lines 23-57 (USP 3,992,900). To avoid this clogging in these patents a two stage process has been proposed using two wash columns as described in U.S.P.
3,587,859, previously mentioned. U.S.P. 3,885,399 and 3,992,900 are proof to the fact that hitherto there was no solution to the problem of avoiding wash liquid reaching the screen, which among other things boils down to the problem of preventing channeling in the packed bed.
The serious difficulties encountered by channeling and freezing up of the screen are moreover clearly expostu-`
lated in a recent study of Gers~on Grossmann (AICHE Journal, Vol. 22, No. 6, November 1976, pg. 1033-1042). In order to get a clear picture of these problems and their implications, special reference is made to pg. 1033 and pg. 1034 top.
By practice of the present invention all these difficulties may be mitigated and in specific embodiments eliminated completely, which goes to say to provide a method and apparatus whereby freezing up and channeling may be efficiently avoided and substantially zero loss operation is assured.
For a clear understanding of the inventive concept of the present invention the following discussion is appropriate about the Pro~stein wash column, mentioned above.
We specifically call attention to Fig. 1 of U.S.P.
3,587,859 and to Fig. 1 and 2 of the Grossman publication.
The counter washer normally consists of a vertical column with a screen in the middle part of its wall. Accord-ing to U.S.P. 3,587,859 (column 1, line 41; column 4, lines 17-18) the ice particles form a plug.
The aqueous concentrate is said to flow up through the lower leg of this plug and out through the screen. The pressure of the aqueous concentrate itself is utilized to provide the driving force for moving the ice particles upward (see U.S.P. 3,587,859 column 1, lines 44-45), which goes to say that the drag of the concentrate on the plug causes the latter to move up against the friction on the walls and the restraining forces at the top. These restraining forces at the top originate e.g. frorn the drag of the bed against the wash liquid, and the scraper which is used to disintegrate the plug and feed out the particles created by that disinte-gration.
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Ideally in processes according to this prior art only a small amount of wash liquid should flow down through the upper leg of the ice plug and out through the screen (which incidentally would in itself tend to clog the screen), but the balance is upset as soon as channeling occurs.
The situation as depicted in U.S.P. 3,587,859 and the publication of G~ossman shows a "brine crown" which is in fact the ~ashfront or in other words the interface between the concentrate and the wash liquid - which is strongly curved and also flow lines of the concentrate which are strongly curved. This is unavoidable in the set up according to the prior art at issue. The curvature of the wash front itself and of the flow lines in its neighbourhood correlate with differences in the density (porosity) of the packed bed, (when we look at it in a cross section perpendicular to the axis).
In this connection attention should be drawn to the American Reissue 23.810 ~specifically Fig. 1, and column 2 lines 47-50). Packed ice crystals are pushed through a zone (c) where liquid is being withdrawn, a "transition zone"
(b) and a water-ice zone (a). In this set-up it is in the transition zone (b) where the curved washfront may be supposed to be formed (if a proper "front" is formed at all).
Stabilization of a curved washfront has, however, proved to be difficult. To circumvent these difficulties it has been proposed in U.S.P. 2,854,494 to force a pulsating reflux stream of wash liquid through the packed bed of ice crystals.
Supposedly a "shake-up" of the transition zone should help to counteract difficulties such as channeling, discussed above.
According to the present invention a sharp and stable washfront is only possible if such measures are taken , .
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that this washfront ~the interface between the concentrate and the wash liquid) lies in a flat plane, perpendicular to the direction in which the packed bed is moving.
Thus according to the present invention there is provided a process for separating the ice crystals contained in a slurry of an aqueous solution and ice crystals from said aqueous solution and washing said ice crystals with an aqueous wash liquid, whereby a packed bed of ice crystals is created which is subjected to a continuous translatory movement, while a washfront is being created within said bed of ice crystals between said aqueous solution and said aqueous wash liquid, characterized in that said aqueous solution and said aqueous wash liquid adjacent to said wash-front are substantially stagnant, and a stable washfront is being created lying in a straight plane perpendicular to said translatory movement of said packed bed of ice crystals.
Generally this will encompass a process for sepa-rating the ice crystals contained in a slurry of an aqueous solution and ice crystals from said aqueous solution and washing said ice crystals with an aqueous wash liquid, comprising sequentialiy the following steps:
a) continuously introducing said slurry in a first cylindri-cal zone;
b) in said first cylindrical zone continuously withdrawing part of said aqueous solution from said slurry, producing a packed bed of ice crystals, and causing said packed bed to adopt a homogeneous porosity throughout its cross section;
c) causing said packed bed to move continuously through a second cylindrical zone, said second zone containing a stagnant layer of said aqueous solution in a first section and a substantially stagnant layer of wash liquid in a second section, contiguous to said first section, thus creating a washfront between said first and said second section;
d) continuously disintegrating said continuously advancing packed bed and feeding out the product of that dis-integration.
Across the washfront there will be a "jump" in temperature as the aqueous solution between the ice crystals, being more concentrated than the wash liquid, will have a lower temperature than that wash liquid. In the normal case that the wash liquid is water, the temperature will of course be 0C, so the ice crystals in the aqueous solution will have a temperature below 0C. In coming into contact with the wash liquid, some wash liquid entering between the ice crystals will freeze, and in doing this generally cement these crystals together. In this way at the washfront a solid porous ice plug is formed. Thus first a thickened slurry has to be created, measures have to be taken to allow for a homogeneous build up of the thickened slurry to a packed bed and measures to impart to it a translatory movement. Most important is that before reaching the wash-front ice crystals have been caused to distribute themselves evenly throughout the cross section of the packed bed. In principle it may be possible to use the drag of the flowing aqueous solution to move the packed bed and nevertheless assure a homogeneous build up of this bed arriving at the interface between the aqueous solution and wash liquid, (the washfront). Drag may transport the ice crystals in the zone where the aqueous solution is withdrawn. The ice crystals accumulating there may push others along. At the washfront homogeneity may be attained if that washfront is located far enough from the place where the aqueous solution has been withdrawn, notwithstanding the fact that at the place of withdrawal of aqueous solution originally an in homogeneous build up of the thickened slurry is obtained, e.g. in the case of a wall filter. This thickened and originally in-homogeneous slurry must however have opportunity or be caused to homogenize. It has to be homogeneous taken over its cross section when arriving at the washfront. This is necessary to avoid radial differences in resistance against liquid flow.
If these differences exist the washfront will not be flat but in some way or another curved.
Another possible set up is the following. The slurry is introduced at the bottom of a vertical cylinder.
The bottom is provided with a screen, through which aqueous solution is withdrawn. A stirrer-scraper connected with a shaft through the bottom of the cylinder and actuated by a motor keeps the screen clean and homogenizes the thickened slurry. The slurry may be introduced sideway or through the (hollow) shaft of the stirrer-scraper. Also the screen through which the aqueous solution is withdrawn need not be in the bottom but can be e.g. in the wall of the cylinder near to the bottom. The ice crystals accumulating in the lower part of the cylinder push others up, forming a packed bed. The liquid in the lower part of the cylinder is aqueous solution, the liquid in the upper part wash liquid. The interface between the aqueous solution and the wash liquid is the washfront, this washfront being kept at approximately constant level by adjusting the pressure of the incoming slurry and the pressure of the wash liquid. This may be done in the manner more fully described in the under following.
-In the top of the cylinder a scraper may be located to disintegrate the washed out packed bed and feed out the product of this disintegration. This also will be more fully described in the underfollowing. The disintegration may also be accomplished by melting.
In an alternative and preferred arrangement the zone where the aqueous solution is withdrawn from the slurry may contain hollow perforated (screened) vanes attached to a -rotatable shaft, through which the aqueous solution is withdrawn. ~These vanes may be attached to the shaft in such a way that they are freely rotatable around small axles perpendicular to the shaft, which goes to say that they are free to take on a tilt depending on the processual factors at hand, such as the rotational speed of the shaft and the drag of the aqueous solution being withdrawn through these hollow vanes. In this case the vanes do not provide the energy to push the crystals ahead but the moving force resides in the drag of the aqueous solution being withdrawn. The crystals accumulating by the withdrawal of the aqueous solution push others along. If the shart, to which the screened hollow vanes are attached and freely movable, is not rotated, they will take on a position parallel to the axis of the wash column, pointing to the feed out end, especially if the vanes are screened at both sides. It is however advantageous to rotate the shaft. This will greatly help in counteracting any tendency to the formation of inhomogeneities by the passage of the thickened slurry along the screen.
Another preferred measure according to the present invention is the use of mechanical means to impart a trans-latory movement to the thickened slurry of ice crystals, andin doing so create a steadily advancing packed bed of these ~4~S~i crystals. This may e.g. be accomplished by using tilted vanes, attached to a rotatable shaft, in such a way that they have a fixed tilt. Again the screen to withdraw the aqueous solution may be located in these vanes, if these are hollow.
By using mechanical means to move the packed bed, this movement is to a large extent made independent from the pressures of the incoming aqueous solution, the outgoing aqueous solution and the wash liquid and their respective differences. By rotation of the fixed tilted vanes the filtering layer adjacent to the filter will be continuously renewed in such a way that homogeneity is assured.
To facilitate a homogeneous build up of the packed bed in radial direction, (which is as already said, particu-larly important when it reaches the washfront), an annular structure of that bed may be recommendable, especially in the case of large diameters of the wash column and when the withdrawal of aqueous solution from the slurry is accomplish-ed through a screen positioned in the direction of movement of the packed bed (e.g. a filter in the wall of the cylinder).
We shall then have to use an apparatus consisting of a cylinder coaxially arranged within another cylinder with larger diameter. The difference in diameter and the distance between the screen and the washfront have to be chosen in such a way that under working conditions the packed bed has a homogeneous build up at the washfront.
This implies that generally when the aqueous solution is withdrawn through a screen in the wall of one or both of the cylinders which together define the annular space in which the packed bed is created, this annular space has to be rather narrow, e.g. 2 to 5 cm. It will be clear that withdrawal of the aqueous solution through a screen in the g _ ~4~5~
wall of the column will tend to favour the creation of in-homogeneities in the packed bed. This tendency is the better counteracted the narrower -~he annular ring is (in connection with the foregoing we refer to the Canadian Patent Appli-cation nr. 294.723).
In the case that the aqueous solution is withdrawn through a screen more or less perpendicular to the trans-latory movement of the packed bed (as already described) the annulus may be considerably wider. E.g. when we use tilted vanes and the inside diameter of the outer cylinder is 100 cm, the annulus may be 20 cm wide. The tendency for an inhomogeneous build up of the packed bed is much less.
In using an annular structure for the packed bed, the mechanical means (such as tilted vanes), used to impart a translatory movement to the packed bed, in the direction of the axis of the cylindrical wash column, and scraper means used to disintegrate the packed bed after this has passed through the washfront, may be attached to the inner cylinder.
In this case the inner cylinder has to rotate.
It is also possible to have the inner cylinder stand still. In this case the mechanical means to forward the packed bed, and the scraper means (if applied) have to be actuated separately. This will be described in more detail in an under following example. The inner cylinder may however also be attached to the same shaft as the mechanical means to forward the packed bed. An optimal possibility of process control may, as the case may be, be obtained by providing the inner cylinder, the mechanical forwarding means and the scraper means with separate actuating mechanisms, so that their respective rotational speeds can be varied at will .
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When using the tilted vanes as the mechanical means to propel the packed bed along it may also be advantageous to make the tilt of these vanes adjustable. This enhances the possibility to control the process, as may be dictated by the particular circumstances at hand.
Disintegration of the packed bed of ice crystals after passing the washfront, may be accomplished by melting.
Particularly good results have however been obtained by the use of scrapers. Scrapers for this purpose are in themselves 10 known. Reference is made e.g. to U.S.P. 3,872,009 and in the under following example a somewhat different construction will be described. As alread,v mentioned the restraining force counteracting the translatory movement of the bed of ice crystals will generally pack the bed so firmly that under influence of the temperature jump at the washfront the ice crystals will be cemented together, creating a solid porous ice plug. It has been found in several instances that this ice plug will consist for about two thirds- of solid ice and for about one third of interconnected pores, but this relation may vary according to conditions. The washfront, while actually standing still, moves relative to the packed bed through these pores. In this way the bed is washed "internally". The position of the washfront within the wash colurnn may be kept substantially fixed by a sensing device with feedback on the position of that washfront/ This may be e.g. accomplished by two closely spaced temperature sensors at different sides of the washfront. This will be described more in detail in the underfollowing.
The present invention also encompasses an apparatus for implementing the process described above. According to the present invention there is thus provided an apparatus for separating the ice crystals contained in a slurry of an aqueous solution and ice crystals, from said solution and washing said ice crystals at a washfront with an aqueous wash liquid, comprising in operative cooperation:
a) enclosure means defining a first cylindrical space;
b) means for feeding in said slurry in said cylindrical space;
c) means for withdrawing solution from said slurry in said cylindrical space while retaining sald ice crystals, producing a thickened slurry;
d) enclosure means defining a second cylindrical space;
e) means adapted to transfer said thickened slurry from said first cylindrical space to a feed-in side of said second cylindrical space;
f) means for causing said thickened slurry to move continu-ously through said second cylindrical space to a feed-out side; -g) means for maintaining a stagnant layer of said aqueous solution in said second cylindrical space at its feed-out .
side; .
h) means for causing said thickened slurry to homogenize throughout in radial direction before reaching the washfront, producing a homogeneously packed bed of ice crystals;
i) at the feed-out end of said second cylindrical space means for continuously disintegrating said packed bed of ice crystals and feed-out the product of disintegration.
The most preferred embodiments of the invention comprise those whereby an annular structure of the washcolumn is combined with rotating hollow vanes with a fixed tilt through which the aqueous solution is withdrawn from the slurry and whereby the scraper means at the one side and the tilted vanes at the other side are provided with separate actuating means. Generally this will imply that the scraper means will be given a higher rotational speed than the tilted vanes.
The present invention will now be further described by way of the following Example and with reference to the accompanying drawings, in which:
Fig. 1 represents the various processual fonctions out of which the process according to the invention is composed;
Fig. 2 serves to illustrate one of the preferred embodiments of the invention;
Fig. 3 is a top view of the cross section along III-III in Fig. 2;
Fig. 4 is a cross section of a hollow vane along IV-IV in Fig. 3;
Referring to Fig. 1, at (1) the slurry of ice crystals is supplied, (2) represents the withdrawal of the aqueous solution, which is fed out at (3) leaving a thickened slurry. The function of homogenization is represented by (4), and the function of formation of a packed bed by (5).
Movement of the packed bed through a stagnant layer of aqueous solution is represented at (6), arriving at the washfront (7). The bed then moves through the substantially stagnant layer of wash liquid (8), whereby it normally con-solidates to a solid porous block of icer whereafter disinte-gration is taklng place at (9), whereas at (10) the product of disintegratlon is slushed away and fed out at (11). Some of the functions (2), (4), (5) and (6) may be performed simultaneously in particular embodiments of the invention, which have been described above. E.g. when using an appa-ratus with an annular space and hollow vanes with a fixed tilt through which the aqueous solution is withdrawn, the functlons (2), (4) and (5) may occur practically at the same time.
Speaking most generally however, the important thing is, that when the thickened slurry arrives at the washfront it is homogeneously packed, so as to form a flat, not curved washfront perpendicular to the axis of the wash-column.
Referring now to Fig. 2, the hull of the apparatusis cut out lengthwise to show the inside in side view. At (17)we see a cylindrical hull, with a bottom plate (18) and a cover plate (19). An inner cylindrical body is shown at (20). This body is- attached to a shaft (21), in its turn attached to the strip (22j, bolted to the cover plate (19).
Another cylindrical body is shown at (23) attached to the shaft (24), carrying the toothed wheel (25). This wheel (25) cooperates with the toothed wheel (26), which is actuated by the motor (27). The body (23) carries the hollow tilted vanes (28), at their upper surface provided with the screen (29). The vanes are represented here more or less simpli-fied, for the rest we refer to Fig. 3 and Fig. 4.
The inside of the hollow vanes (28) communicates with the duct (29') through which liquid can be withdrawn.
The body (23) also carries pins (30), while the hull (17) carries vertical vanes (31).
A disc (32) provided with knives (33) and slots (34) acts as a scraper. The disc (32) is attached to the cylindrical body (35), attached to the toothed wheel (37), cooperating with the toothed wheel (38). The motor (39) ~', ;, 5~
actuates the toothed wheel (38).
The slurry enters at (40) and is kept well stirred by the pins (30) cooperating with the vanes (31), to prevent settling of the crystals. Aqueous solution is withdrawn through the screen (29) and leaves through the hollow vanes (28) and the duct (29'), leaving a thickened slurry at the surface of the screen (29). This thickened slurry is packed and pushed through the annular space (41) by rotation of the body (23) with the vanes (28). The dotted line (42) repre-sents the washfront, being the dividing plane between thespace (41), in which the liquid is an aqueous solution and the space (36), in which the liquid is wash liquid (normally water). The temperature sensing devices (57) and (58) keep the movement of the washfront within narrow limits. These will register a certain temperature difference that exists between aqueous solution and the wash liquid. If the wash-front moves up or down this temperature difference will disappear and an electric impulse from the control unit (59) will actuate the valve (60) opening or closing it more, as the case may be.
The space (36) will in most cases be filled by a porous solid ice plug, which will be disintegrated by rotation of the disc (32) with the knives (33). The parti-cles created by the disintegration, passing through the slots (34), will enter the space (43). Wash liquid will be pumped around by the pump (44). It will enter the space (43) at (45), flushing out the ice particles at (46). The ice parti-cles are melted by the melter (47). When the washfront remains at a fixed place the quantity of water leaving the system through the valve (60) will equal the quantity of ice which is fed out by the scraper (32). If the washfront moves `~ ~
down the valve (60) is opened somewhat more, so that somewhat more water is withdrawn and visa versa. In this way the balance is restored.
In Fig. 3, we see, at (29), the screen of one of the hollow tilted vanes, the edge of which is shown at (28).
Between two tilted vanes the space (48) can be detected through which the slurry passes. The vanes are attached to the annular cylindric body (23), in which a circular groove (49) is present. The inside of the hollow tilted vanes is connected to the circular groove (49) by channels (50). The annular cylindrical body (23) is attached to the shaft (51) by the protruding ridge (52). The shaft (51) is provided with a central channel (29') which is connected to the circu-lar groove (49) by the channel (53).
From Fig. 4 it can be seen that the bottom (54) of the vane is provided lengthwise with ridges (55), which serve to support the screen (29). The ridges (55) are provided with holes (56) for the passage of the aqueous solution. The vane is attached to the cyllndrical body (23), provided with the channel (50) and the groove (49) where the liquid of all the vanes is collected. The shaft to which the cylindrical body (23) is attached is shown at (51) with the central channel (29') to drain away the aqueous solution.
It will be obvious that the apparatus as described and other related embodiments with hollow vanes can serve as a continuous slurry thickener when the disintegrating device is left out.
It will also be obvious that the apparatus accord-ing to the invention can be used quite generally for systems in which one component can be crystallized out of a liquid multicomponent system and may be separated out of this system in a wash column.
5~
This invention relates generally to a continuous process and apparatus for separating the ice crystals con-tained in a slurry of an aqueous solution and ice crystals from said aqueous solution and washing said ice crystals with an aqueous wash liquid. Normally this aqueous wash liquid will be water, but multi stage processes are possible whereby the wash liquid in any particular stage is the aqueous solution withdrawn from a succeeding stage. This kind of slurry occurs in industrial processes whereby either the aqueous solution is recovered as a product and the ice crystals are rejected, or conversely, whereby the ice crystals are recovered as a product and the aqueous solution is rejected. A process of -the first kind in the food industry is the freeze concen-tration of aqueous liquids such as fruit, juices, beer, wine and coffee extract. A process of the second kind is the freeze concentration of sea water to produce fresh water; in this process the brine is rejected and the ice crystals are recovered and melted.
A continuous packed bed wash column is described in U.S.P. 3,587,859 (Probstein), specifically for producing fresh water from sea water. In this wash column a porous bed of particles ice crystals is formed and the liquid medium brine is caused to flow outwardly from the column at a screened opening positioned intermediate its ends. A wash liquid is introduced at one end of the column to displace the liquid medium from the interstices between the particles as the porous bed moves continuously through the column.
Control means are provided to control the relationship among the liquid pressures at the ends of the porous bed and the pressure at such screened opening so as to maximize the rate at which the particles can be removed at the output end of .~
i6 the column.
In operating this kind of apparatus the two main difficulties are freezing of the screen producing breakdown of the operation and losses occurring by the mixing of the aqueous solution between the ice crystals and the wash liquid. These losses are exacerbated by the phenomenon of channeling. This phenomenon entails the formation of "channels" in the bed of ice crystals, through which wash liquid escapes. When e.g. liquld foodstuffs are being concentrated the concentration is partly undone, and in the case of sea water desalination fresh water is lost, as it mingles with the concentrated brine which is being rejected.
Moreover wash liquid reaching the screen has the tendency to produce clogging. The wash liquid has a higher freezing point than the concentrated solution. The screen is cooled by this concentrated solution and the wash liquid coming in contact with the screen will freeze and, as said, produce clogging, eventually bringing the process to a halt.
The difficulties associated with freezing up of the 20 screen have been well described in U.S.P. 3,885,399 and 3,992,900 (Campbell, assigned to Avco Corp.). Reference is made specially to column 1, lines 23-57 (USP 3,992,900). To avoid this clogging in these patents a two stage process has been proposed using two wash columns as described in U.S.P.
3,587,859, previously mentioned. U.S.P. 3,885,399 and 3,992,900 are proof to the fact that hitherto there was no solution to the problem of avoiding wash liquid reaching the screen, which among other things boils down to the problem of preventing channeling in the packed bed.
The serious difficulties encountered by channeling and freezing up of the screen are moreover clearly expostu-`
lated in a recent study of Gers~on Grossmann (AICHE Journal, Vol. 22, No. 6, November 1976, pg. 1033-1042). In order to get a clear picture of these problems and their implications, special reference is made to pg. 1033 and pg. 1034 top.
By practice of the present invention all these difficulties may be mitigated and in specific embodiments eliminated completely, which goes to say to provide a method and apparatus whereby freezing up and channeling may be efficiently avoided and substantially zero loss operation is assured.
For a clear understanding of the inventive concept of the present invention the following discussion is appropriate about the Pro~stein wash column, mentioned above.
We specifically call attention to Fig. 1 of U.S.P.
3,587,859 and to Fig. 1 and 2 of the Grossman publication.
The counter washer normally consists of a vertical column with a screen in the middle part of its wall. Accord-ing to U.S.P. 3,587,859 (column 1, line 41; column 4, lines 17-18) the ice particles form a plug.
The aqueous concentrate is said to flow up through the lower leg of this plug and out through the screen. The pressure of the aqueous concentrate itself is utilized to provide the driving force for moving the ice particles upward (see U.S.P. 3,587,859 column 1, lines 44-45), which goes to say that the drag of the concentrate on the plug causes the latter to move up against the friction on the walls and the restraining forces at the top. These restraining forces at the top originate e.g. frorn the drag of the bed against the wash liquid, and the scraper which is used to disintegrate the plug and feed out the particles created by that disinte-gration.
~ "
~14~5~
Ideally in processes according to this prior art only a small amount of wash liquid should flow down through the upper leg of the ice plug and out through the screen (which incidentally would in itself tend to clog the screen), but the balance is upset as soon as channeling occurs.
The situation as depicted in U.S.P. 3,587,859 and the publication of G~ossman shows a "brine crown" which is in fact the ~ashfront or in other words the interface between the concentrate and the wash liquid - which is strongly curved and also flow lines of the concentrate which are strongly curved. This is unavoidable in the set up according to the prior art at issue. The curvature of the wash front itself and of the flow lines in its neighbourhood correlate with differences in the density (porosity) of the packed bed, (when we look at it in a cross section perpendicular to the axis).
In this connection attention should be drawn to the American Reissue 23.810 ~specifically Fig. 1, and column 2 lines 47-50). Packed ice crystals are pushed through a zone (c) where liquid is being withdrawn, a "transition zone"
(b) and a water-ice zone (a). In this set-up it is in the transition zone (b) where the curved washfront may be supposed to be formed (if a proper "front" is formed at all).
Stabilization of a curved washfront has, however, proved to be difficult. To circumvent these difficulties it has been proposed in U.S.P. 2,854,494 to force a pulsating reflux stream of wash liquid through the packed bed of ice crystals.
Supposedly a "shake-up" of the transition zone should help to counteract difficulties such as channeling, discussed above.
According to the present invention a sharp and stable washfront is only possible if such measures are taken , .
, ' s~
that this washfront ~the interface between the concentrate and the wash liquid) lies in a flat plane, perpendicular to the direction in which the packed bed is moving.
Thus according to the present invention there is provided a process for separating the ice crystals contained in a slurry of an aqueous solution and ice crystals from said aqueous solution and washing said ice crystals with an aqueous wash liquid, whereby a packed bed of ice crystals is created which is subjected to a continuous translatory movement, while a washfront is being created within said bed of ice crystals between said aqueous solution and said aqueous wash liquid, characterized in that said aqueous solution and said aqueous wash liquid adjacent to said wash-front are substantially stagnant, and a stable washfront is being created lying in a straight plane perpendicular to said translatory movement of said packed bed of ice crystals.
Generally this will encompass a process for sepa-rating the ice crystals contained in a slurry of an aqueous solution and ice crystals from said aqueous solution and washing said ice crystals with an aqueous wash liquid, comprising sequentialiy the following steps:
a) continuously introducing said slurry in a first cylindri-cal zone;
b) in said first cylindrical zone continuously withdrawing part of said aqueous solution from said slurry, producing a packed bed of ice crystals, and causing said packed bed to adopt a homogeneous porosity throughout its cross section;
c) causing said packed bed to move continuously through a second cylindrical zone, said second zone containing a stagnant layer of said aqueous solution in a first section and a substantially stagnant layer of wash liquid in a second section, contiguous to said first section, thus creating a washfront between said first and said second section;
d) continuously disintegrating said continuously advancing packed bed and feeding out the product of that dis-integration.
Across the washfront there will be a "jump" in temperature as the aqueous solution between the ice crystals, being more concentrated than the wash liquid, will have a lower temperature than that wash liquid. In the normal case that the wash liquid is water, the temperature will of course be 0C, so the ice crystals in the aqueous solution will have a temperature below 0C. In coming into contact with the wash liquid, some wash liquid entering between the ice crystals will freeze, and in doing this generally cement these crystals together. In this way at the washfront a solid porous ice plug is formed. Thus first a thickened slurry has to be created, measures have to be taken to allow for a homogeneous build up of the thickened slurry to a packed bed and measures to impart to it a translatory movement. Most important is that before reaching the wash-front ice crystals have been caused to distribute themselves evenly throughout the cross section of the packed bed. In principle it may be possible to use the drag of the flowing aqueous solution to move the packed bed and nevertheless assure a homogeneous build up of this bed arriving at the interface between the aqueous solution and wash liquid, (the washfront). Drag may transport the ice crystals in the zone where the aqueous solution is withdrawn. The ice crystals accumulating there may push others along. At the washfront homogeneity may be attained if that washfront is located far enough from the place where the aqueous solution has been withdrawn, notwithstanding the fact that at the place of withdrawal of aqueous solution originally an in homogeneous build up of the thickened slurry is obtained, e.g. in the case of a wall filter. This thickened and originally in-homogeneous slurry must however have opportunity or be caused to homogenize. It has to be homogeneous taken over its cross section when arriving at the washfront. This is necessary to avoid radial differences in resistance against liquid flow.
If these differences exist the washfront will not be flat but in some way or another curved.
Another possible set up is the following. The slurry is introduced at the bottom of a vertical cylinder.
The bottom is provided with a screen, through which aqueous solution is withdrawn. A stirrer-scraper connected with a shaft through the bottom of the cylinder and actuated by a motor keeps the screen clean and homogenizes the thickened slurry. The slurry may be introduced sideway or through the (hollow) shaft of the stirrer-scraper. Also the screen through which the aqueous solution is withdrawn need not be in the bottom but can be e.g. in the wall of the cylinder near to the bottom. The ice crystals accumulating in the lower part of the cylinder push others up, forming a packed bed. The liquid in the lower part of the cylinder is aqueous solution, the liquid in the upper part wash liquid. The interface between the aqueous solution and the wash liquid is the washfront, this washfront being kept at approximately constant level by adjusting the pressure of the incoming slurry and the pressure of the wash liquid. This may be done in the manner more fully described in the under following.
-In the top of the cylinder a scraper may be located to disintegrate the washed out packed bed and feed out the product of this disintegration. This also will be more fully described in the underfollowing. The disintegration may also be accomplished by melting.
In an alternative and preferred arrangement the zone where the aqueous solution is withdrawn from the slurry may contain hollow perforated (screened) vanes attached to a -rotatable shaft, through which the aqueous solution is withdrawn. ~These vanes may be attached to the shaft in such a way that they are freely rotatable around small axles perpendicular to the shaft, which goes to say that they are free to take on a tilt depending on the processual factors at hand, such as the rotational speed of the shaft and the drag of the aqueous solution being withdrawn through these hollow vanes. In this case the vanes do not provide the energy to push the crystals ahead but the moving force resides in the drag of the aqueous solution being withdrawn. The crystals accumulating by the withdrawal of the aqueous solution push others along. If the shart, to which the screened hollow vanes are attached and freely movable, is not rotated, they will take on a position parallel to the axis of the wash column, pointing to the feed out end, especially if the vanes are screened at both sides. It is however advantageous to rotate the shaft. This will greatly help in counteracting any tendency to the formation of inhomogeneities by the passage of the thickened slurry along the screen.
Another preferred measure according to the present invention is the use of mechanical means to impart a trans-latory movement to the thickened slurry of ice crystals, andin doing so create a steadily advancing packed bed of these ~4~S~i crystals. This may e.g. be accomplished by using tilted vanes, attached to a rotatable shaft, in such a way that they have a fixed tilt. Again the screen to withdraw the aqueous solution may be located in these vanes, if these are hollow.
By using mechanical means to move the packed bed, this movement is to a large extent made independent from the pressures of the incoming aqueous solution, the outgoing aqueous solution and the wash liquid and their respective differences. By rotation of the fixed tilted vanes the filtering layer adjacent to the filter will be continuously renewed in such a way that homogeneity is assured.
To facilitate a homogeneous build up of the packed bed in radial direction, (which is as already said, particu-larly important when it reaches the washfront), an annular structure of that bed may be recommendable, especially in the case of large diameters of the wash column and when the withdrawal of aqueous solution from the slurry is accomplish-ed through a screen positioned in the direction of movement of the packed bed (e.g. a filter in the wall of the cylinder).
We shall then have to use an apparatus consisting of a cylinder coaxially arranged within another cylinder with larger diameter. The difference in diameter and the distance between the screen and the washfront have to be chosen in such a way that under working conditions the packed bed has a homogeneous build up at the washfront.
This implies that generally when the aqueous solution is withdrawn through a screen in the wall of one or both of the cylinders which together define the annular space in which the packed bed is created, this annular space has to be rather narrow, e.g. 2 to 5 cm. It will be clear that withdrawal of the aqueous solution through a screen in the g _ ~4~5~
wall of the column will tend to favour the creation of in-homogeneities in the packed bed. This tendency is the better counteracted the narrower -~he annular ring is (in connection with the foregoing we refer to the Canadian Patent Appli-cation nr. 294.723).
In the case that the aqueous solution is withdrawn through a screen more or less perpendicular to the trans-latory movement of the packed bed (as already described) the annulus may be considerably wider. E.g. when we use tilted vanes and the inside diameter of the outer cylinder is 100 cm, the annulus may be 20 cm wide. The tendency for an inhomogeneous build up of the packed bed is much less.
In using an annular structure for the packed bed, the mechanical means (such as tilted vanes), used to impart a translatory movement to the packed bed, in the direction of the axis of the cylindrical wash column, and scraper means used to disintegrate the packed bed after this has passed through the washfront, may be attached to the inner cylinder.
In this case the inner cylinder has to rotate.
It is also possible to have the inner cylinder stand still. In this case the mechanical means to forward the packed bed, and the scraper means (if applied) have to be actuated separately. This will be described in more detail in an under following example. The inner cylinder may however also be attached to the same shaft as the mechanical means to forward the packed bed. An optimal possibility of process control may, as the case may be, be obtained by providing the inner cylinder, the mechanical forwarding means and the scraper means with separate actuating mechanisms, so that their respective rotational speeds can be varied at will .
, ., ~,.
s~
When using the tilted vanes as the mechanical means to propel the packed bed along it may also be advantageous to make the tilt of these vanes adjustable. This enhances the possibility to control the process, as may be dictated by the particular circumstances at hand.
Disintegration of the packed bed of ice crystals after passing the washfront, may be accomplished by melting.
Particularly good results have however been obtained by the use of scrapers. Scrapers for this purpose are in themselves 10 known. Reference is made e.g. to U.S.P. 3,872,009 and in the under following example a somewhat different construction will be described. As alread,v mentioned the restraining force counteracting the translatory movement of the bed of ice crystals will generally pack the bed so firmly that under influence of the temperature jump at the washfront the ice crystals will be cemented together, creating a solid porous ice plug. It has been found in several instances that this ice plug will consist for about two thirds- of solid ice and for about one third of interconnected pores, but this relation may vary according to conditions. The washfront, while actually standing still, moves relative to the packed bed through these pores. In this way the bed is washed "internally". The position of the washfront within the wash colurnn may be kept substantially fixed by a sensing device with feedback on the position of that washfront/ This may be e.g. accomplished by two closely spaced temperature sensors at different sides of the washfront. This will be described more in detail in the underfollowing.
The present invention also encompasses an apparatus for implementing the process described above. According to the present invention there is thus provided an apparatus for separating the ice crystals contained in a slurry of an aqueous solution and ice crystals, from said solution and washing said ice crystals at a washfront with an aqueous wash liquid, comprising in operative cooperation:
a) enclosure means defining a first cylindrical space;
b) means for feeding in said slurry in said cylindrical space;
c) means for withdrawing solution from said slurry in said cylindrical space while retaining sald ice crystals, producing a thickened slurry;
d) enclosure means defining a second cylindrical space;
e) means adapted to transfer said thickened slurry from said first cylindrical space to a feed-in side of said second cylindrical space;
f) means for causing said thickened slurry to move continu-ously through said second cylindrical space to a feed-out side; -g) means for maintaining a stagnant layer of said aqueous solution in said second cylindrical space at its feed-out .
side; .
h) means for causing said thickened slurry to homogenize throughout in radial direction before reaching the washfront, producing a homogeneously packed bed of ice crystals;
i) at the feed-out end of said second cylindrical space means for continuously disintegrating said packed bed of ice crystals and feed-out the product of disintegration.
The most preferred embodiments of the invention comprise those whereby an annular structure of the washcolumn is combined with rotating hollow vanes with a fixed tilt through which the aqueous solution is withdrawn from the slurry and whereby the scraper means at the one side and the tilted vanes at the other side are provided with separate actuating means. Generally this will imply that the scraper means will be given a higher rotational speed than the tilted vanes.
The present invention will now be further described by way of the following Example and with reference to the accompanying drawings, in which:
Fig. 1 represents the various processual fonctions out of which the process according to the invention is composed;
Fig. 2 serves to illustrate one of the preferred embodiments of the invention;
Fig. 3 is a top view of the cross section along III-III in Fig. 2;
Fig. 4 is a cross section of a hollow vane along IV-IV in Fig. 3;
Referring to Fig. 1, at (1) the slurry of ice crystals is supplied, (2) represents the withdrawal of the aqueous solution, which is fed out at (3) leaving a thickened slurry. The function of homogenization is represented by (4), and the function of formation of a packed bed by (5).
Movement of the packed bed through a stagnant layer of aqueous solution is represented at (6), arriving at the washfront (7). The bed then moves through the substantially stagnant layer of wash liquid (8), whereby it normally con-solidates to a solid porous block of icer whereafter disinte-gration is taklng place at (9), whereas at (10) the product of disintegratlon is slushed away and fed out at (11). Some of the functions (2), (4), (5) and (6) may be performed simultaneously in particular embodiments of the invention, which have been described above. E.g. when using an appa-ratus with an annular space and hollow vanes with a fixed tilt through which the aqueous solution is withdrawn, the functlons (2), (4) and (5) may occur practically at the same time.
Speaking most generally however, the important thing is, that when the thickened slurry arrives at the washfront it is homogeneously packed, so as to form a flat, not curved washfront perpendicular to the axis of the wash-column.
Referring now to Fig. 2, the hull of the apparatusis cut out lengthwise to show the inside in side view. At (17)we see a cylindrical hull, with a bottom plate (18) and a cover plate (19). An inner cylindrical body is shown at (20). This body is- attached to a shaft (21), in its turn attached to the strip (22j, bolted to the cover plate (19).
Another cylindrical body is shown at (23) attached to the shaft (24), carrying the toothed wheel (25). This wheel (25) cooperates with the toothed wheel (26), which is actuated by the motor (27). The body (23) carries the hollow tilted vanes (28), at their upper surface provided with the screen (29). The vanes are represented here more or less simpli-fied, for the rest we refer to Fig. 3 and Fig. 4.
The inside of the hollow vanes (28) communicates with the duct (29') through which liquid can be withdrawn.
The body (23) also carries pins (30), while the hull (17) carries vertical vanes (31).
A disc (32) provided with knives (33) and slots (34) acts as a scraper. The disc (32) is attached to the cylindrical body (35), attached to the toothed wheel (37), cooperating with the toothed wheel (38). The motor (39) ~', ;, 5~
actuates the toothed wheel (38).
The slurry enters at (40) and is kept well stirred by the pins (30) cooperating with the vanes (31), to prevent settling of the crystals. Aqueous solution is withdrawn through the screen (29) and leaves through the hollow vanes (28) and the duct (29'), leaving a thickened slurry at the surface of the screen (29). This thickened slurry is packed and pushed through the annular space (41) by rotation of the body (23) with the vanes (28). The dotted line (42) repre-sents the washfront, being the dividing plane between thespace (41), in which the liquid is an aqueous solution and the space (36), in which the liquid is wash liquid (normally water). The temperature sensing devices (57) and (58) keep the movement of the washfront within narrow limits. These will register a certain temperature difference that exists between aqueous solution and the wash liquid. If the wash-front moves up or down this temperature difference will disappear and an electric impulse from the control unit (59) will actuate the valve (60) opening or closing it more, as the case may be.
The space (36) will in most cases be filled by a porous solid ice plug, which will be disintegrated by rotation of the disc (32) with the knives (33). The parti-cles created by the disintegration, passing through the slots (34), will enter the space (43). Wash liquid will be pumped around by the pump (44). It will enter the space (43) at (45), flushing out the ice particles at (46). The ice parti-cles are melted by the melter (47). When the washfront remains at a fixed place the quantity of water leaving the system through the valve (60) will equal the quantity of ice which is fed out by the scraper (32). If the washfront moves `~ ~
down the valve (60) is opened somewhat more, so that somewhat more water is withdrawn and visa versa. In this way the balance is restored.
In Fig. 3, we see, at (29), the screen of one of the hollow tilted vanes, the edge of which is shown at (28).
Between two tilted vanes the space (48) can be detected through which the slurry passes. The vanes are attached to the annular cylindric body (23), in which a circular groove (49) is present. The inside of the hollow tilted vanes is connected to the circular groove (49) by channels (50). The annular cylindrical body (23) is attached to the shaft (51) by the protruding ridge (52). The shaft (51) is provided with a central channel (29') which is connected to the circu-lar groove (49) by the channel (53).
From Fig. 4 it can be seen that the bottom (54) of the vane is provided lengthwise with ridges (55), which serve to support the screen (29). The ridges (55) are provided with holes (56) for the passage of the aqueous solution. The vane is attached to the cyllndrical body (23), provided with the channel (50) and the groove (49) where the liquid of all the vanes is collected. The shaft to which the cylindrical body (23) is attached is shown at (51) with the central channel (29') to drain away the aqueous solution.
It will be obvious that the apparatus as described and other related embodiments with hollow vanes can serve as a continuous slurry thickener when the disintegrating device is left out.
It will also be obvious that the apparatus accord-ing to the invention can be used quite generally for systems in which one component can be crystallized out of a liquid multicomponent system and may be separated out of this system in a wash column.
Claims (11)
1. Process for separating the ice crystals contained in a slurry of an aqueous solution and ice crystals from said aqueous solution and washing said ice crystals with an aqueous wash liquid, whereby a packed bed of ice crystals is created which is subjected to a continuous translatory movement, while a washfront is being created within said packed bed of ice crystals between said aqueous solution and said aqueous wash liquid, characterized in that said aqueous solution and said aqueous wash liquid adjacent to said washfront being sub-stantially stagnant, a stable washfront is being created lying in a straight plane perpendicular to said translatory movement of said packed bed of ice crystals.
2. Process according to claim 1 comprising sequentially the following steps:
a) continuously introducing said slurry in a first cylindri-cal zone;
b) in said first cylindrical zone continuously withdrawing part of said aqueous solution from said slurry producing a packed bed of ice crystals, and causing said packed bed to adopt a homogeneous porosity throughout its cross section;
c) causing said packed bed to move continuously through a second cylindrical zone, said second zone containing a stagnant layer of said aqueous solution in a first section and a substantially stagnant layer of wash liquid in a second section, contiguous to said first section, thus creating a washfront between said first and said second section;
d) continuously disintegrating said continuously advancing packed bed and feeding out a product resulting from that disintegration.
a) continuously introducing said slurry in a first cylindri-cal zone;
b) in said first cylindrical zone continuously withdrawing part of said aqueous solution from said slurry producing a packed bed of ice crystals, and causing said packed bed to adopt a homogeneous porosity throughout its cross section;
c) causing said packed bed to move continuously through a second cylindrical zone, said second zone containing a stagnant layer of said aqueous solution in a first section and a substantially stagnant layer of wash liquid in a second section, contiguous to said first section, thus creating a washfront between said first and said second section;
d) continuously disintegrating said continuously advancing packed bed and feeding out a product resulting from that disintegration.
3. Process according to claim 2 whereby the packed bed is caused to move through said second cylindrical zone by tilted vanes attached to a shaft coaxial with said cylindrical zones.
4. Process according to claim 3 whereby said aqueous solution is withdrawn from said slurry by perforations in the surface of said tilted vanes.
5. Process according to claim 2 or 3 whereby the first and second cylindrical zones have an annular structure.
6. Process according to claim 2 or 3 whereby said dis-integration is accomplished by scraping said packed bed with a rotating disc provided with slots and knives.
7. Apparatus for separating the ice crystals contained in a slurry of an aqueous solution and ice crystals, from said solution and washing said ice crystals with an aqueous wash liquid, comprising in operative cooperation:
a) enclosure means defining a first cylindrical space, b) means for feeding in said slurry in said first cylindrical space;
c) means for withdrawing solution from said slurry in said cylindrical space while retaining said ice crystals, producing a thickened slurry;
d) enclosure means defining a second cylindrical space;
e) means adapted to transfer said thickened slurry from said first cylindrical space to a feed-in side of said second cylindrical space;
f) means for causing said thickened slurry to move continu-ously through said second cylindrical space to a feed out side;
g) means for maintaining a stagnant layer of said aqueous solution in said second cylindrical space at its feed out side;
h) means for causing said thickened slurry to homogenize throughout its cross section before reaching the washfront, producing a homogeneously packed bed of ice crystals;
i) at the feed out end of said second cylindrical space means for continuously desintegrating said packed bed of ice crystals and feed out the product of desintegrating
a) enclosure means defining a first cylindrical space, b) means for feeding in said slurry in said first cylindrical space;
c) means for withdrawing solution from said slurry in said cylindrical space while retaining said ice crystals, producing a thickened slurry;
d) enclosure means defining a second cylindrical space;
e) means adapted to transfer said thickened slurry from said first cylindrical space to a feed-in side of said second cylindrical space;
f) means for causing said thickened slurry to move continu-ously through said second cylindrical space to a feed out side;
g) means for maintaining a stagnant layer of said aqueous solution in said second cylindrical space at its feed out side;
h) means for causing said thickened slurry to homogenize throughout its cross section before reaching the washfront, producing a homogeneously packed bed of ice crystals;
i) at the feed out end of said second cylindrical space means for continuously desintegrating said packed bed of ice crystals and feed out the product of desintegrating
8. Apparatus according to claim 7 whereby the means mentioned under f) for causing said thickened slurry to move continuously through said second cylindrical space comprise tilted vanes attached to a rotatable shaft coaxial with said cylindrical spaces.
9. Apparatus according to claim 8 whereby each of said vanes is hollow, having an inner space and its surface perforated, said inner space being connected to a duct in said rotatable shaft, in such a way as to enable the withdrawal of solution from said slurry of ice crystals, and feeding it out.
10. Apparatus according to one of the claims 7-9 whereby said cylindrical spaces, mentioned in claim 7 have an annular structure.
11. Apparatus according to claim 7 whereby said means, mentioned under i), for continuously desintegrating said packed bed of ice crystals, are scraping means comprising a rotatable disc provided with slots and knives.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB27792/78 | 1978-06-23 | ||
| GB7827792 | 1978-06-23 |
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| CA1144056A true CA1144056A (en) | 1983-04-05 |
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| CA000330643A Expired CA1144056A (en) | 1978-06-23 | 1979-06-22 | Continuous packed bed wash column |
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| BR (1) | BR7903889A (en) |
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| NL8105872A (en) * | 1981-12-28 | 1983-07-18 | Douwe Egberts Tabaksfab | WASHING COLUMN. |
| NL8202517A (en) * | 1982-06-22 | 1984-01-16 | Tno | DEVICE FOR COMPACTING A SUSPENSION. |
| NL8202518A (en) * | 1982-06-22 | 1984-01-16 | Tno | METHOD AND APPARATUS FOR COUNTERFLOW TREATMENT OF SUSPENDED PARTICLES WITH A LIQUID |
| NL8402536A (en) * | 1984-08-17 | 1986-03-17 | Tno | METHOD FOR SEPARATING SUSPENSION LIQUID FROM SUSPENSION SOLID PARTICLES AND WASHING OF THE OBTAINED COMPACT BED OF SOLID PARTICLES WITH COUNTERFLOW WASHING LIQUID. |
| NL8600461A (en) * | 1986-02-24 | 1987-09-16 | Percy Cohen Henriquez | STATIC WASHING COLUMN. |
| DE10036880A1 (en) * | 2000-07-28 | 2002-02-07 | Basf Ag | Control of a washing column in a melt crystallization process |
| DE10242746B4 (en) | 2002-09-13 | 2010-07-01 | Evonik Degussa Gmbh | Washing device, a process for cleaning a laundry and the use of the washing device |
| EP1876147A1 (en) * | 2006-07-05 | 2008-01-09 | Bp Exploration Operating Company Limited | Desalination process |
| EP2130572A1 (en) * | 2008-06-06 | 2009-12-09 | Nederlandse Organisatie voor toegepast- natuurwetenschappelijk onderzoek TNO | Rotating knife, washing column, and method for disintegrating a crystal bed in a washing column |
| US8771622B2 (en) | 2010-05-04 | 2014-07-08 | Solvay Chemicals, Inc. | Impurities removal from waste solids in the production of soda ash, sodium bicarbonate and/or other derivatives |
| CN112774244B (en) * | 2020-12-30 | 2022-09-23 | 江苏楷益智能科技有限公司 | Scraper type surface crystallizer |
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| DE1215605B (en) * | 1958-11-15 | 1966-04-28 | Carrier Corp | Method and device for obtaining drinking water from a salt solution |
| GB1111933A (en) * | 1966-01-07 | 1968-05-01 | Atomic Energy Authority Uk | Improvements in or relating to desalination |
| US3587859A (en) * | 1968-07-30 | 1971-06-28 | Ronald F Probstein | Method of separating solid particles from a slurry with wash column separators |
| JPS5441559B1 (en) * | 1971-05-22 | 1979-12-08 | ||
| US3813892A (en) * | 1971-08-23 | 1974-06-04 | Avco Corp | Water purification system |
| JPS4974171A (en) * | 1972-10-20 | 1974-07-17 | ||
| US3992170A (en) * | 1975-03-20 | 1976-11-16 | Dravo Corporation | Method and apparatus for melting ice in saline water conversion systems |
| FR2334627A1 (en) * | 1975-12-09 | 1977-07-08 | Saksir Fernand | Desalination by freezing seawater and washing the ice - to dissolve surface salts avoids problems of highly corrosive deposits |
| GB1555357A (en) * | 1976-10-15 | 1979-11-07 | Douwe Egberts Koninlijke Tabak | Apparatus and process for the separation of crystals and mother liquor |
| GB1589477A (en) * | 1977-01-12 | 1981-05-13 | Douwe Egberts Tabaksfab | Freeze concentration apparatus |
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- 1979-06-06 ZA ZA792809A patent/ZA792809B/en unknown
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| CH643150A5 (en) | 1984-05-30 |
| FR2433966B1 (en) | 1985-07-19 |
| AU518789B2 (en) | 1981-10-22 |
| AU4811479A (en) | 1980-01-03 |
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| NL178392C (en) | 1986-03-17 |
| ZA792809B (en) | 1980-06-25 |
| SE7905314L (en) | 1979-12-24 |
| DE2923854A1 (en) | 1980-01-10 |
| BR7903889A (en) | 1980-02-20 |
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| GB2023564A (en) | 1980-01-03 |
| IT1162744B (en) | 1987-04-01 |
| GB2023564B (en) | 1982-09-08 |
| IT7923784A0 (en) | 1979-06-21 |
| JPS558895A (en) | 1980-01-22 |
| DE2923854C2 (en) | 1988-02-04 |
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