Patent Grant
11660607
The present invention relates to the field of centrifugal separation, and more specifically to centrifugal separators comprising separation discs.
Centrifugal separators are generally used for separation of liquids and/or solids from a liquid mixture or a gas mixture. During operation, fluid mixture that is about to be separated is introduced into a rotating bowl and due to the centrifugal forces, heavy particles or denser liquid, such as water, accumulates at the periphery of the rotating bowl whereas less dense liquid accumulates closer to the central axis of rotation. This allows for collection of the separated fractions, e.g. by means of different outlets arranged at the periphery and close to the rotational axis, respectively.
Separation discs are stacked in the rotating bowl at a mutual distance to form interspaces between themselves, thus forming surface-enlarging inserts within the bowl. Separation discs of metal are used in connection with relatively robust and large-sized centrifugal separators for separating liquid mixtures and the separation discs themselves are thus of relatively large size and are exposed to both high centrifugal and liquid forces. The liquid mixture to be separated in the centrifugal rotor is conducted through the interspaces, wherein the liquid mixture is separated into phases of different densities during operation of the centrifugal separator. The interspaces are provided by spacing members arranged on the surface of each separation disc. There are many ways of forming such spacing members. They may be formed by attaching separate members in the form of narrow strips or small circles of sheet metal to the separation disc, usually by spot welding them to the surface of the separation disc.
In order to maximize the separating capacity of the centrifugal separator, there is a desire to fit as many separation discs as possible into the stack within a given height in the separator. More separation discs in the stack means more interspaces in which the liquid mixture can be separated. However, as the separation discs are made thinner, they will exhibit a loss in rigidity and irregularities in their shape may begin to appear. The separation discs are furthermore compressed in the stack inside the centrifugal rotor to form a tight unit. Thin separation discs may thereby flex and/or because of their irregular shaping give rise to unevenly sized interspaces in the stack of separation discs. Accordingly, in certain parts of the interspaces (e.g. far away from a spacing member), the mutually adjacent separation discs may be completely compressed against each other to leave no interspaces at all. In other parts of the interspaces (e.g. in the vicinity of a spacing member) the separation discs will not flex much and accordingly provide an adequate height.
A disc comprising spot-shaped spacing members for decreasing the risk of unevenly sized interspaces in the stack is disclosed in WO2013020978. The disc in this disclosure comprises spot-shaped spacing members having spherical or cylindrical shape as seen in the direction of their height.
Further, the flow of the phases in the interspaces between the discs is of great importance. Thus, there is a need in the art for alternative designs for separation discs that facilitate the use of thin discs that at the same time provides a good flow of the phases between the discs during separation.
A main object is to provide a separation disc that aids in guiding separated sludge along the surface of the disc during operation.
A further object of the present invention is to provide a separation disc for a centrifugal separator that decreases the risk of unevenly sized interspaces in a stack.
A further object is to provide a disc that allows for the use of thin separation discs in a disc stack.
An object is also to provide a disc stack and a centrifugal separator comprising such separation discs.
As a first aspect of the invention there is provided a separation disc for a centrifugal separator, the disc being adapted to be comprised in a stack of separation discs inside a centrifugal rotor for separating a fluid mixture, wherein the separation disc has a truncated conical shape with an inner surface and an outer surface and a plurality of spacing members extending a height (H) from at least one of the inner surface and the outer surface, wherein
the plurality of spacing members are for providing interspaces between mutually adjacent separation discs in a stack of separation discs, and
wherein the separation disc further comprises at least one elongated rib extending from the inner surface to a height (h) that is less than the height (H) to which the plurality of spacing members extend, and
wherein the at least one elongated rib extends from a first position on the inner surface to a second position on the inner surface, wherein the second position is at a radial distance that is larger than the radial distance of the first position, and
wherein the relation between the height of the elongated ribs (h) and the spacing members (H) is h/H>0.7.
The separation disc may e.g. comprise a metal or be of metal material, such as stainless steel.
The separation disc may further comprise a plastic material or be of a plastic material.
The separation disc may be injection molded.
The separation disc may further also be adapted to be compressed in a stack of separation discs inside a centrifugal rotor for separating a liquid mixture.
A truncated conical shape refers to a shape that is frustoconical, i.e. having the shape of a frustum of a cone, which is the shape of a cone with the narrow end, or tip, removed. The axis of the truncated conical shape thus defines the axial direction of the separation disc, which is the direction of the height of the corresponding conical shape or the direction of the axis passing through the apex of the corresponding conical shape.
The inner surface is thus the surface facing the axis whereas the outer surface is the surface facing away from the axis of the truncated cone. The spacing-members may be provided only on the inner surface, only at the outer surface or on both the inner and outer surface of the truncated conical shape.
Half of the opening angle of the frustoconical shape is usually defined as the “alpha angle”. As an example the separation disc may have an alpha angle between 25° and 45°, such as between 35° and 40°.
A spacing member is a member on the surface of a disc that spaces two separation discs apart when they are stacked on top of each other, i.e. defining the interspace between the discs. The spacing members may be arranged on the disc so that they support both the radial outer portion of the disc and the radial inner portion of the disc. In other words, the spacing members may be distributed both on the radially outer half of surface of the disc and on the radially inner half of the surface of the disc.
The height H of the spacing members is the height perpendicular to the surface.
The spacing members may extend to a height H that is less than 0.8 mm from the surface of the separation disc. As an example, the spacing members may extend to a height that is less than 0.60, such as less than 0.50 mm, such as less than 0.40 mm, such as less than 0.30 mm, such as less than 0.25 mm, such as less than 0.20 mm, from the surface of the separation disc.
The separation disc further comprises at least one elongated rib that extends on the inner surface a height h that is less than height H of the spacing members.
Thus, the elongated ribs are of such height that they do not form part of any spacing member and they do not bear any weight in a disc stack of separation discs, but are instead provided for guiding means.
The elongated rib has thus a length that is larger than its width. The length may be in a radial direction. An elongated rib may extend a distance (d) on the surface that is more than the height (h) above the surface, such has more than twice the height such as more than five times the height, such as more than ten times the height.
The elongated ribs or strips have a length that is above 10 mm, such above 20 mm, such as above 50 mm, such as above 100 mm.
Further, the elongated ribs extend radially outward, i.e. from a first to a second position, wherein the second position is radially outside the first position. Thus, the separation disc may comprise a central opening and an outer perimeter, and the elongated rib may extend in a direction from the central opening towards the outer perimeter.
The relation of h/H is at least 0.7, meaning that the height of the elongated ribs is at least 70% of the height of the spacing members. Thus, the elongated ribs may be of such height that they during operation of a centrifugal separator comprising a stack of such separation discs extend out into the geostrophic flow between two adjacent separation discs, i.e. extend out from any formed Ekman layers at the surface of the separation disc.
In embodiments of the first aspect of the invention, the relation between the height of the elongated ribs (h) and the height of the spacing members (H) is h/H≥0.7. In embodiments of the first aspect of the invention, the relation between the height of the elongated ribs (h) and the height of the spacing members (H) may be 0.75≤h/H≤0.95, such as 0.80≤h/H≤0.90.
The thickness of the separation disc may be less than 0.60 mm, such as less than 0.50 mm, such as less than 0.45 mm, such as less than 0.40 mm, such as less than 0.35 mm, such as less than 0.30 mm.
Furthermore, the separation disc may have a diameter that is more than 200 mm, such as more than 300 mm, such as more than 350 mm, such as more than 400 mm, such as more than 450 mm, such as more than 500 mm, such as more than 530 mm.
The first aspect of the invention is based on the insight that the elongated strips do not have to bear any load in a compressed stack but may instead function solely as guiding means. For example, in a compressed stack of separation discs, the separation is performed in the interspace between two adjacent discs. The heavier phase, such as sludge, is transported along the surface of the upper disc, i.e. along the “roof” of the interspace, whereas a separated less dense phase is transported along the surface of the lower disc, i.e. along the “floor” of the interspace. Thus, with elongated strips having a lower height that the spacing members and arranged on the inner surface of the disc, these elongated strips will aid in guiding sludge along the “roof” of the interspace but will not interfere with the phase transported along the “floor” of the interspace.
In embodiments of the first aspect of the invention, also the spacing members extend from the inner surface.
Thus, both the spacing members and the elongated ribs may extend from the inner surface, such as solely from the inner surface.
In embodiments of the first aspect of the invention, the separation disc comprises at least four elongated ribs.
As an example, the separation disc may comprise at least 8, such as at least 12, such as at least 18 elongated ribs.
Furthermore, the separation disc may comprise 4-60 elongated ribs, such as 4-50, such as 8-40, such as 12-30, elongated ribs on the inner surface.
The elongated ribs may be equally spaced throughout the circumference of the separation disc.
In embodiments of the first aspect of the invention, the at least one elongated rib is straight and has an extension in the radial direction.
The radial direction is thus from the axis of rotation (x) radially toward an outer perimeter of the disc, such as from a central opening towards the outer perimeter of the separation disc. The at least one elongated rib may extend in a straight radial direction or in a straight direction that forms an angle with the radius of the separation disc. A straight elongated rib may thus be arranged to guide a phase along a straight path on the surface of the separation disc. The elongated ribs may have an extension that is predominantly in the radial direction.
In embodiments of the first aspect of the invention, the at least one elongated rib is curved. The extension of the curved ribs may be predominantly in the radial direction.
Thus, at least one elongated rib may be curved. A curved elongated rib may be curved when viewed as a projection onto a plane that is perpendicular to the axis of rotation (X).
Thus, the ribs may extend in curved paths and form at least at the radially outer surrounding portions of the separation disc an angle with the generatrices of the separation disc. As a consequence of the curved form of the elongated ribs also a separated phase may be guided by the elongated ribs along paths which are curved in a corresponding way.
The radial length of the elongated ribs may vary on a disc or all elongated ribs may have the same length. The radial length may for example be more than 10%, such as more than 25% of the radial length of the disc, i.e. the length between central opening and the outer perimeter.
In embodiments of the first aspect of the invention, the at least one elongated rib extend a length that is more than 50% of the radial extension of the inner surface of the disc.
For example, the at least one elongated rib extend a length that is more than 75% of the radial extension of the inner surface of the disc.
The at least one elongated rib may extend radially along substantially the whole radial extension of the inner surface of the disc, meaning that the ribs may extend across substantially the whole of the conical portion of the separation disc and end up in the vicinity of the radially outer surrounding edge of the separation disc.
In embodiments of the first aspect of the invention, the at least one elongated rib has a width at the surface of the separation disc that is below 2 mm.
Thus, the width of at least one elongated rib may be below 1.5 mm, such as below 1 mm.
The elongated ribs may be in the form of separate pieces of narrow strips or circular blanks of sheet metal, which are attached to the surface of the separation disc. As an alternative or complement, elongated ribs may also be integrally formed with the material of the separation disc.
In embodiments of the first aspect of the invention, the spacing members and the at least one elongated rib are integrally formed in one piece with the material of the separation disc. For example, the spacing members and the elongated ribs may be integrally formed on the inner surface of the disc.
Thus, all elevations of the separation disc may be formed by the material of the separation disc itself
In embodiments of the first aspect of the invention, the at least one elongated rib is wider at the surface than at the portion at the height (h) to which the elongated rib extends, as seen in a cross-section that is perpendicular to the direction in which the elongated rib extends on the surface.
Thus, the elongated rib may form a ridge at the surface that has a tapering cross-section from the surface and out. The cross-section may be tip-shaped. As an example, the tip-shaped cross-section may have a geometric shape that tapers smoothly from the flat base at the surface to a tip, i.e. to an apex a certain height above the base. The apex may be directly above the centroid of the base. However, the apex may also be located at a point that is not above the centroid so that the tip-shaped spacing members have the form of an oblique cone or an oblique pyramid. The “tip” of the tip-shaped cross-section may have a tip radius which is less than the height h. The tip may thus be rounded.
Further, the portion at the height (h) to which the elongated rib extends may be flat, i.e. more or less parallel to the surface.
It may be advantageous for the flow dynamics between the separation discs to have an elongated rib that is wider at the surface and then becomes thinner as it extends from the surface. In other words, an elongated rib having such a shape may to a lesser degree obscure the flow of a fluid between the separation discs if compared to an elongated rib that has a substantially constant cross-section.
In embodiments of the first aspect of the invention, the plurality of spacing members comprise a plurality of spot-formed spacing members.
It may be advantageous to combine the elongated ribs with spot-formed spacing members since the spot-formed spacing members introduce little obstruction of flow while still bearing the load in a compressed stack as compared to traditional elongated spacing members. Thus, a combination of spot-formed spacing members and elongated strips that are lesser in height gives a very low obstruction of the flow between the discs while still being able to guide a separated heavy phase or particles along the surface of the separation disc.
A spot-formed spacing member may extend to a width which is less than 5 mm along the surface of the separation disc. The width of the base of the spot-formed spacing member may refer to or correspond to the diameter of the spot-formed spacing member at the surface. If the base at the surface has an irregular shape, the width of the spot-formed spacing member may correspond to the largest extension of the base at the surface.
As an example, the base of the spot-formed spacing member may extend to a width which is less than 2 mm along the surface of the separation disc, such as to a width which is less than 1.5 mm along the surface of the separation disc, such as to a width which is about or less than 1 mm along the surface of the disc.
Thus, due to a small size compared to the “conventional” large-sized spacing members in the form of e.g. elongated strips, the spacing members may be provided in greater number without blocking or significantly impeding the flow of fluid mixture between the discs in a stack of separation discs.
The spot-formed spacing members may have spherical or cylindrical shape as seen in the direction of their height.
As an example, the spot-formed spacing members have a tip-shaped cross-section.
Thus, the plurality of spot-formed spacing members may comprise spot-formed spacing members that are tip-shaped and taper from the base at the surface of the separation disc towards a tip extending a certain height from the surface.
The spot-formed spacing members may be tip-shaped at least in a cross-section of the spacing member and the cross-section, or the spacing member as a whole, thus tapers from the base at the surface towards a tip, which extends a certain height from the surface. The height of a tip-shaped spacing member is the height perpendicular to the surface.
The spot-formed spacing members may be tip-shaped in at least one cross-section, such as the cross-section perpendicular to the radius of the disc. Thus, the spot-formed spacing members may form small ridges that extend on the surface. The ridges may for example extend in a radial direction of the separation disc, i.e. substantially along a direction of flow of fluid mixture along the separation disc.
The spot-formed spacing members may be tip-shaped in more than one cross-section.
The spot-formed spacing members may be tip-shaped as a whole, i.e. each cross section of a spot-formed spacing member is tip-shaped. Thus, the spot-formed and tip-shaped spacing members may e.g. have the form of a cone, i.e. be cone-shaped, or the form of a pyramid, depending on the form of the base along the surface. The base at the surface may thus have the form as a cross, a circle, an ellipse, a square or have a rectangular shape.
As an example, the tip-shaped spacing members may have the form of a cone or a pyramid, i.e. have a geometric shape that tapers smoothly from the flat base at the surface to the tip, i.e. to an apex a certain height above the base. The apex may be directly above the centroid of the base. However, the apex may also be located at a point that is not above the centroid so that the tip-shaped spacing members have the form of an oblique cone or an oblique pyramid.
If spot-formed and tip-shaped spacing members are introduced on the surfaces of the thin metal separation discs, then equidistant spaces in a stack comprising thin separation discs may be achieved. Hence, the separating capacity of the centrifugal separator can in this way be further increased by fitting a greater number of the thinner metal separation discs into the stack. The invention will in this way facilitate the use of separation discs as thin as possible to maximize the number of separation discs and interspaces within a given stack height. Furthermore, the tip-shaped and spot-formed spacing member lead to less contact area between a spacing member of a disc and an adjacent disc, thus leading to a larger surface area of the discs in a stack being available for separation. Further, a small contact area decreases the risk of dirt or impurities being stuck within a disc stack during operation of a centrifugal separator, i.e. decreases the risk of contamination.
Also, the equidistant spaces in between the separation discs contribute to decreasing the risk of dirt or impurities being stuck within the disc stack during operation of the centrifugal separator. Moreover, the equidistant spaces provide for improved separation performance in the centrifugal separator. Since the interspaces formed between the separation discs are equidistant, the separation performance is substantially the same all over the separation area formed within the disc stack, and thus, closer to a theoretically calculated separation performance of the relevant centrifugal separator. Whereas in a prior art disc stack, wherein the separation discs are deformed during operation of the centrifugal separator and thus, form uneven interspaces between the discs, the separation performance varies within the disc stack, and therefore, is farther from the theoretically calculated separation performance of the relevant centrifugal separator.
As an example, spot-formed spacing members may extend from the surface of the separation disc in a direction that forms an angle with the surface which is less than 90 degrees. Both spot-formed spacing members having spherical or cylindrical shape as seen in the direction of their height and spot-formed spacing members being tip-shaped, may extend from the surface of the separation disc in a direction that forms an angle with the surface which is less than 90 degrees.
Furthermore, spot-formed spacing members may extend from the surface of the separation disc in substantially the axial direction of the truncated conical shape of the separation disc. Both spot-formed spacing members having spherical or cylindrical shape as seen in the direction of their height and spot-formed spacing members being tip-shaped, may extend from the surface of the separation disc in substantially the axial direction of the truncated conical shape of the separation disc.
Moreover, the tip of the spot-formed spacing members may have a tip radius which is less than the height to which the spot-formed spacing members extend from the surface.
As an example, the tip of the spot-formed spacing members may have a tip radius which is less than half the height, such as less than a quarter of the height, such as less than a tenth of the height, to which the spot-formed spacing members extend from the surface. With such a “sharp” tip, the spot-formed spacing member may more easily adhere to the surface of an adjacent disc in a disc stack, and a sharp tip also decreases blockage or obstruction of the flow of fluid mixture between the discs in a stack of separation discs.
The plurality of separation discs comprising spot-formed spacing members may comprise spacing members having different shape. Thus, a single disc may comprise spot-formed spacing members having different shapes, and the plurality of discs may comprise different discs having spot-formed spacing members of different shapes, i.e. some discs may have only spherical spot-formed spacing members whereas some discs may have only tip-shaped spot-formed spacing members.
However, the plurality of discs comprising spot-formed spacing members may also comprise separation discs having the same type of spot-formed spacing members.
In embodiments of the first aspect of the invention, a majority of the plurality of discs comprising spot-formed spacing members are of the same kind in terms of thickness, diameter, shape and number of spot-formed spacing members.
Further, a majority of the spot-formed spacing members may be distributed on the surface of the separation disc at a mutual distance which is less than 20 mm.
As an example, the spot-formed spacing members may be distributed on the surface of the separation disc at a mutual distance which is less than 15 mm, such as about or less than 10 mm.
The spot-formed-spacing members may be evenly distributed on the surface, distributed in clusters, or distributed on the surface at different mutual distance, e.g. to form areas of the disc in which the density of spot-formed spacing members is higher compared to the density of spot-formed spacing members on the rest of the same surface of the disc.
The inner or outer surface of the separation disc may have a surface density of the spot-formed spacing members that is above 10 spacing members/dm2, such as above 25 spacing members/dm2, such as above 50 spacing members/dm2, such as above 75 spacing members/dm2, such as about or above 100 spacing members/dm2.
Further, the inner or outer surface of the separation disc may have a surface density of the spot-formed spacing members that is above 10 spacing members/dm2, such as above 25 spacing members/dm2, such as above 50 spacing members/dm2, such as above 75 spacing members/dm2, such as about or above 100 spacing members/dm2, and the separation disc having a thickness that is less than 0.40 mm, such as less than 0.30 mm.
However, the whole inner or outer surface does not have to be covered with the spot-formed spacing members. Consequently, in embodiments of the first aspect of the invention, the inner or outer surface of the separation disc comprises at least one area of at least 1.0 dm2 having a density of the spot-formed spacing members that is above 10 spacing members/dm2, such as above 25 spacing members/dm2, such as above 50 spacing members/dm2, such as above 75 spacing members/dm2, such as about or above 100 spacing members/dm2.
In embodiments of the first aspect of the invention, the separation disc further comprises at least one through hole in the truncated surface or formed by at least one cut-out at the outer periphery of separation disc. Such through holes or cut-outs may form axial rising channels in a stack of separation discs that may facilitate feeding and distributing fluid mixture, such as a liquid, into the interspaces in the stack of separation discs.
As a second aspect of the invention, there is provided a stack of separation discs adapted to be comprised inside a centrifugal rotor for separating a liquid mixture, comprising axially aligned separation discs having a truncated conical shape with an inner surface and an outer surface,
and wherein the axially aligned separation discs comprises a plurality of discs having spacing members and at least one elongated rib according to the first aspect above arranged so that the elongated rib on a separation disc is not in contact with an adjacent separation disc.
The terms and definitions used in relation to the second aspect are the same as discussed in relation to the first aspect above.
The stack of separation discs may be aligned on an aligning member, such as on a distributor. Thus, in embodiments of the second aspect of the invention, the stack further comprises a distributor onto which the separation discs are aligned to form a stack.
The stack of separation discs may be adapted to be compressed with a force that is above 8 tons.
In embodiments of the second aspect of the invention, the plurality or number of separation discs having spacing members and at least one elongated rib according to the first aspect above may be more than 50% of the total number of separation discs in the stack of separation discs, such as more than 75% of the total number of separation discs in the stack of separation discs, such as more than 90% of the total number of separation discs in the stack of separation discs. As an example, all discs of the disc stack may be discs having spacing members and at least one elongated rib according to the first aspect above.
In embodiments of the second aspect of the invention, the plurality of discs having spacing members and at least one elongated rib according to the first aspect above are arranged so that a majority of the spacing members of a disc are displaced compared to the spacing members of an adjacent disc. Further, also the elongated ribs of a separation disc may be displaced compared to the elongated ribs of an adjacent separation disc.
A spacing member or elongated rib being “displaced” compared to a spacing member or elongated rib on an adjacent disc refers to the discs being arranged so that the spacing member or elongated ribs are not at the same position as a spacing member or elongated rib on an adjacent disc. Thus, a spacing member being displaced does not abut an adjacent disc at a position where the adjacent disc has a spacing member.
Hence, the discs having spacing members and at least one elongated rib according to the first aspect above may be arranged so that the spacing members or elongated ribs of a disc are not axially aligned with a spacing member or elongated rib of an adjacent disc. Thus, the spacing members may be radially displaced in relation to the spacing members of adjacent discs as seen in an axial plane through the axis of rotation, and/or the spacing members may be circumferentially displaced in relation to the spacing members of adjacent discs as seen in a radial plane through the axis of rotation. Also, the elongated ribs may be radially displaced in relation to the elongated ribs of adjacent discs as seen in an axial plane through the axis of rotation, and/or the elongated ribs may be circumferentially displaced in relation to the elongated ribs of adjacent discs as seen in a radial plane through the axis of rotation.
Displacement of spacing members or elongated ribs may be achieved by a disc being turned in the circumferential direction compared to an adjacent disc, such as turned through a predetermined angle in a circumferential direction. Thus, some or each separation disc may be gradually turned through an angle in the circumferential direction as the separation discs are being stacked on top of each other to form the stack.
As an example, a spacing member of a disc may be displaced in relation to a corresponding spacing member of an adjacent disc a circumferential distance and/or a radial distance that is between 2-15 mm, such as between 3-10 mm, such as about 5 mm. Also the elongated ribs may be displaced a circumferential distance as described above.
As an example, a spacing member of a disc may be displaced in relation to a corresponding spacing member of an adjacent disc a circumferential distance that is about half of the mutual distance between spacing members of the disc. Also the elongated ribs may be displaced a circumferential distance as described above.
Furthermore, displacement of spacing members and/or elongated ribs may also be achieved by using separation discs having different patterns of spacing members and/or elongated ribs so that the spacing members of a disc are not axially aligned with the spacing members of an adjacent disc and/or the elongated ribs of a disc are not axially aligned with the elongated ribs of an adjacent disc, when the discs are stacked on top of each other, such as stacked onto a distributor.
As an example, all spacing members and/or all elongated ribs of a disc may be displaced compared to the spacing members and/or the elongated ribs of an adjacent disc.
A stack in which the spacing members are displaced, i.e. in which the spacing members are not axially aligned on top of each other, is advantageous in that it may provide better support for thin discs, i.e. the thin discs in a stack have more points of support compared to if the discs are arranged so that the spacing members are aligned on top of each other in the disc stack. Thus, a stack in which the spacing members are displaced facilitates the use of thin discs in the stack.
Furthermore, a stack in which the spacing members are displaced may be advantageous in that it allows for easy manufacturing or assembly of the disc stack, i.e. the spacing members allows even interspaces between discs in the stack even if the spacing members are not axially aligned. In other words, in a disc stack, the spacing members have the ability to bear the large compression forces in a compressed stack without having to be aligned on top of each other. This is thus different from the conventional idea of forming a disc stack, in which conventional elongated spacing members on the discs are axially aligned on top of each other in mutually adjacent separation discs throughout the stack of separation discs, or in other words, the spacing elements are in the prior art arranged in axially straight lines throughout the stack of separation discs, in order to bear all the compression forces in the compressed stack.
However, the discs in the stack may also be arranged so that the spacing members and the elongated ribs are axially aligned.
Thus, in embodiments of the second aspect of the invention, the discs having spacing members are arranged so that a majority or all of the spacing members of a disc are axially aligned with the spacing members of an adjacent disc.
In embodiments of the second aspect of the invention, the discs having spacing members and elongated ribs according to the first aspect above are arranged so that the elongated ribs a disc are axially aligned with the elongated ribs of an adjacent disc.
In embodiments of the second aspect of the invention, the discs having spacing members and elongated ribs according to the first aspect above are arranged so that the elongated ribs a disc are axially aligned with the elongated ribs of an adjacent disc whereas a majority or all of the spacing members of a disc are displaced compared to the spacing members of an adjacent disc.
In embodiments of the second aspect of the invention, the stack comprises more than 100 separation discs, such as more than 150, such as more than 200, such as more than 250, such as more than 300 separation discs.
In embodiments of the second aspect of the invention, a majority of all discs in the stack are the discs having the spacing members and elongated ribs according to the first aspect above.
As an example, the stack may comprise more than 100 separation discs and more than 90% of those separation discs may be separation discs having spacing members and elongated ribs according to the first aspect above.
As an example, the stack may comprise more than 150 separation discs and more than 90% of those separation discs, such as all separation discs, may be separation discs having spacing members and elongated ribs according to the first aspect above.
As an example, the stack may comprise more than 200 separation discs and more than 90% of those separation discs, such as all separation discs, may be separation discs having spacing members and elongated ribs according to the first aspect above.
As an example, the stack may comprise more than 250 separation discs and more than 90% of those separation discs, such as all separation discs, may be separation discs having spacing members and elongated ribs according to the first aspect above.
As an example, the stack may comprise more than 300 separation discs and more than 90% of those separation discs, such as all separation discs, may be separation discs having spacing members and elongated ribs according to the first aspect above.
The separation discs having spacing members and elongated ribs according to the first aspect above in the disc stacks as exemplified above may have a diameter that is more than 300 mm and comprise more than 300 spot-formed spacing members, such as more than 1000 spot-formed spacing members, such as more than 1300 spot-formed spacing members, or they may have a diameter that is more than 350 mm and comprise more than 500 spot-formed spacing members, such as more than 1400 spot-formed spacing members, such as more than 1800 spot-formed spacing members, or they may have a diameter that is more than 400 mm and comprise more than 600 spot-formed spacing members, such as more than 1700 spot-formed spacing members, such as more than 2200 spot-formed spacing members, or they may have a diameter that is more than 450 mm and comprise more than 700 spot-formed spacing members, such as more than 1900 spot-formed spacing members, such as more than 2800 spot-formed spacing members, or they may have a diameter that is more than 500 mm and comprise more than 900 spot-formed spacing members, such as more than 2700 spot-formed spacing members, such as more than 3600 spot-formed spacing members, or they may have a diameter that is more than 530 mm and comprise more than 1000 spot-formed spacing members, such as more than 3000 spot-formed spacing members, such as more than 4000 spot-formed spacing members
Consequently, the stack may comprise more than 300 separation discs having a diameter that is more than 500 mm and more than 90% of those separation discs, such as all separation discs, may be separation discs having spacing members and elongated ribs according to the first aspect above and comprise more than 3000 spot-formed spacing members, such as more than 4000 spot-formed spacing members.
In embodiments of the second aspect of the invention, the stack of separation discs is arranged so that the spot-formed spacing members are the major load-bearing elements in the stack of separation discs.
This means that a majority of the compression forces are held by spot-formed spacing members in the disc stack.
In embodiments of the second aspect of the invention, the plurality of discs having spacing members and elongated ribs according to the first aspect above is free of discs having spacing members other than the spot-formed spacing members for creating interspaces between the discs in the stack.
Thus, the plurality of discs having spacing members and elongated ribs according to the first aspect above, and also the whole disc stack, may comprise solely spot-formed spacing members as load-bearing elements.
In embodiments of the second aspect of the invention, the stack of separation discs further comprises at least one axial rising channel formed by at least one through hole in the truncated surface or formed by at least one cut-out at the outer periphery of a plurality or all separation discs in the stack.
As discussed in relation to the first aspect above, such axial rising channels may facilitate feeding and distributing fluid mixture, such as a liquid, into the interspaces in the stack of separation discs.
As a third aspect of the invention, there is provided a centrifugal separator for separation of at least two components of a fluid mixture which are of different densities, which centrifugal separator comprises
The terms and definitions used in relation to the third aspect are the same as discussed in relation to the other aspects above.
The centrifugal separator is for separation of a fluid mixture, such as a gas mixture or a liquid mixture. The stationary frame of the centrifugal separator is a non-rotating part, and the spindle and is supported by the frame by at least one bearing device, such as by at least one ball-bearing.
The centrifugal separator may further comprise a drive member arranged for rotating the spindle and the centrifuge rotor mounted on the spindle. Such a drive member for rotating the spindle and centrifuge rotor may comprise an electrical motor having a rotor and a stator. The rotor may be provided on or fixed to the spindle so that it transmits driving torque to the spindle and hence to the centrifuge rotor during operation.
Alternatively, the drive member may be provided beside the spindle and rotate the spindle and centrifuge rotor by a suitable transmission, such as a belt or a gear transmission.
The centrifuge rotor is adjoined to a first end of the spindle and is thus mounted to rotate with the spindle. During operation, the spindle thus forms a rotating shaft. The first end of the spindle may be an upper end of the spindle. The spindle is thus rotatable around the axis of rotation (X).
The spindle and centrifuge rotor may be arranged to rotate at a speed of above 3000 rpm, such as above 3600 rpm.
The centrifuge rotor further encloses a separation space in which the separation of the fluid mixture takes place. Thus, the centrifuge rotor forms a rotor casing for the separation space. The separation space comprises a stack of separation discs as discussed in relation to the second aspect of the invention above and the stack is arranged centrally around the axis of rotation. Such separation discs thus form surface enlarging inserts in the separation space.
The separator inlet for fluid mixture, i.e. feed, that is to be separated may be a stationary pipe arranged for supplying the feed to the separation space. The inlet may also be provided within a rotating shaft, such as within the spindle.
The first separator outlet for discharging a first separated phase from the separation space may be a first liquid outlet.
The second separator outlet for discharging a second separated phase from the separation space may be a second liquid outlet. Thus, the separator may comprise two liquid outlets, wherein the second liquid outlet is arranged at a larger radius from the rotational axis as compared to the first liquid outlet. Thus, liquids of different densities may be separated and be discharged via such first and second liquid outlets, respectively. The separated liquid of lowest density may be discharged via the first separator outlet whereas the separated liquid phase of higher density may be discharged via the second separator outlet, respectively.
During operation, a sludge phase, i.e. mixed solid and liquid particles forming a heavy phase, may be collected in an outer peripheral part of the separation space. Therefore, the second separator outlet for discharging a second separated phase from the separation space may comprise outlets for discharging such a sludge phase from the periphery of the separation space. The outlets may be in the form of a plurality of peripheral ports extending from the separation space through the centrifuge rotor to the rotor space between the centrifuge rotor and the stationary frame. The peripheral ports may be arranged to be opened intermittently, during a short period of time in the order of milliseconds, to enable discharge of a sludge phase from the separation space to the rotor space. The peripheral ports may alternatively be in the form of nozzles that are constantly open during operation to allow a constant discharge of sludge.
However, the second separator outlet for discharging a second separated phase from the separation space may be a second liquid outlet, and the centrifugal separator may further comprise a third separator outlet for discharging a third separated phase from the separation space.
Such a third separator outlet comprise outlets for discharging a sludge phase from the periphery of the separation space, as discussed above, and may be in the form of a plurality of peripheral ports arranged to be opened intermittently or in the form of nozzles that are constantly open during operation to allow a constant discharge of sludge.
The centrifugal separator according to the third aspect of the invention is advantageous in that it allows for operation with high flow rates of feed, i.e. mixture to be separated.
In certain separator applications, the separation fluid during the separation process is kept under special hygienic conditions and/or without any air entrainment and high shear forces, such as when the separated product is sensitive to such influence. Examples of that kind are separation of dairy products, beer and in biotechnology applications. For such applications, so called hermetic separators have been developed, in which the separator bowl or centrifuge rotor is completely filled with liquid during operation. This means that no air or free liquid surfaces is meant to be present in the rotor.
In embodiments of the first aspect of the invention, at least one of the separator inlet, first separator outlet or second separator outlet is mechanically hermetically sealed.
Hermetic seals reduce the risk of oxygen or air getting into the separation space and contact the liquid to be separated.
Accordingly, in embodiments of the third aspect of the invention, the centrifugal separator is for separating dairy products, such as separating milk into cream and skimmed milk
In embodiments of the third aspect of the invention, the stack of separation discs comprises at least 200, such as at least 300 separation discs having a diameter of at least 400 mm, and wherein the plurality of discs having spot-formed spacing members comprise at least 2000 spot-formed spacing members on each disc.
As an example, the stack of separation discs may comprise more than 300 separation discs and more than 90% of those separation discs, such as all separation discs, may have a diameter of at least 500 mm and may be separation discs having spot-formed spacing members comprising at least 4000 spot-formed spacing members on each disc.
Examples of separation discs, stacks of separation discs as well as a centrifugal separator according to the present disclosure will be further illustrated by the following description with reference to the accompanying drawings.
However, as an alternative, it is to be understood that outer surface 3 could be provided with the spot-formed spacing members 4 whereas inner surface 2 could be free of spot-formed spacing members 4 and also free of other spacing members.
There are also a number of cut-outs 13 at the inner periphery 6 of the separation disc 1 in order to facilitate stacking on e.g. a distributor.
It is to be understood that a majority or all spot-formed spacing members 4 on a separation disc may extend in the same direction, i.e. a majority or all spot-formed spacing members 4 on a separation disc may extend in a direction that is substantially perpendicular to the surface or a majority or all spot-formed and tip-shaped spacing members 4 on a separation disc may extend in a direction that forms an angle with the surface, i.e. like the examples shown in
Furthermore, the tip 9 of a tip-shaped and spot-formed spacing member has a tip radius Rtip, and is further shown in more detail in
In other words, the separation discs of the disc stack 1 are arranged so that a spot-formed and spacing member 4a of a separation disc 1a does not abut adjacent disc 1b at a position where the adjacent disc 1b has spot-formed spacing member 4b. This is also illustrated in
However, the separation discs 1 of the disc stack 10 may be provided on the distributor 11 so that a majority of the spacing members of a disc are axially aligned with the 8 spacing members of an adjacent disc. This is illustrated in
The centrifugal separator 14 comprises a rotating part arranged for rotation about an axis of rotation (X2) and comprises rotor 17 and spindle 16. The spindle 16 is supported in a stationary frame 15 of the centrifugal separator 14 in a bottom bearing 24 and a top bearing 23. The stationary frame 15 surrounds rotor 17.
The rotor 17 forms within itself a separation chamber 18 in which centrifugal separation of e.g. a liquid mixture to takes place during operation. The separation chamber 18 may also be referred to as a separation space 18.
The separation chamber 18 is provided with a stack 10 of frusto-conical separation discs 1 in order to achieve effective separation of the fluid to be separated in the interspaces 28 between the discs 1. The stack 10 of truncated conical separation discs 1 are examples of surface-enlarging inserts. These discs 1 are fitted centrally and coaxially with the rotor 17 and also comprise through holes which form axial channels 25 for axial flow of liquid when the separation discs 1 are fitted in the centrifugal separator 14. The separation discs 1 are as discussed in the examples above and comprises both spot-formed spacing members and elongated ribs integrally formed on the inner surface of each disc.
In
The rotor 17 has extending from it a liquid light phase outlet 33 for a lower density component separated from the liquid mixture, and a liquid heavy phase outlet 34 for a higher density component, or heavy phase, separated from the liquid mixture. The outlets 33 and 34 extend through the frame 15. The outlets 33, 34 may also be referred to as separator outlets 33, 34. In certain applications, the separator 14 only contains a single liquid outlet, such as only liquid outlet 33. This depends on the liquid material that is to be processed. The rotor 15 is further provided with a third outlet for discharge of sludge that has accumulated at the periphery of the separation chamber 18. The sludge outlet is in the form of a plurality of peripheral ports 19 that extend from the separation chamber 18 through the rotor casing to a surrounding space 20 outside the centrifuge rotor 17. The peripheral ports 19 may be intermittently openable during a short time period, e.g. in the order of milliseconds, and permit total or partial discharge of sludge from the separation space, using a conventional intermittent discharge system as known in the art.
The centrifugal separator 1 is further provided with a drive motor 21. This motor 21 may for example comprise a stationary element 22 and a rotatable element 26, which rotatable element surrounds and is connected to the spindle 16 such that it transmits driving torque to the spindle 16 and hence to the rotor 17 during operation. The drive motor 21 may be an electric motor. Furthermore, the drive motor 21 may be connected to the spindle 16 by transmission means. The transmission means may be in the form of a worm gear which comprises a pinion and an element connected to the spindle 16 in order to receive driving torque. The transmission means may alternatively take the form of a propeller shaft, drive belts or the like, and the drive motor may alternatively be connected directly to the spindle.
A central duct 27 extends through the spindle 16, which takes the form of a hollow, tubular member. The central duct 27 forms in this embodiment an inlet duct for supplying the liquid mixture for centrifugal separation to the separation space 18 via the inlet 29 of the rotor 17. The inlet duct may also be referred to as a separator inlet. Introducing the liquid material from the bottom provides a gentle acceleration of the liquid material. The spindle 16 is further connected to a stationary inlet pipe 30 at the bottom end of the spindle 16 such that liquid material to be separated may be transported to the central duct 27 by transporting means.
A first mechanical hermetic seal 32 is arranged at the bottom end of the spindle 16 to seal the hollow spindle 16 to the stationary inlet pipe 30. The hermetic seal 32 is an annular seal that surrounds the bottom end of the spindle 16 and the stationary pipe 30. Further, also the liquid light phase outlet 33 and the liquid heavy phase outlet 34 may be hermetically mechanically sealed. As an alternative, centripetal pumps, such as paring discs, may be arranged at outlets 33 and 34 to aid in transporting separated phases out from the separator.
During operation of the separator in
The path of the liquid material to be separated through the spindle 16 to the separation space 18 is illustrated by arrows “B” in
Depending on the density, different phases in the liquid is separated in the interspaces 28 between the separation discs of the stack 10 fitted in the separation space 18. Heavier components in the liquid move radially outwards between the separation discs, whereas the phase of lowest density moves radially inwards between the separation discs and is forced through outlet 33 arranged at the radial innermost level in the separator. The liquid of higher density is instead forced out through outlet 34 that is at a radial distance that is larger than the radial level of outlet 33. Thus, during separation, an interphase between the liquid of lower density and the liquid of higher density is formed in the separation space 18. Solids, or sludge, accumulate at the periphery of the separation space 18 and may be emptied intermittently from the separation space by opening of sludge outlets, i.e. the peripheral ports 19, whereupon sludge and a certain amount of liquid is discharged from the separation space by means of centrifugal force. The opening and closing of the peripheral ports 19 are controlled by means of a sliding bowl bottom 35 which is movable between an open and closed position along a direction parallel to the axis of rotation (X2).
In the embodiment of
The invention is not limited to the embodiments disclosed but may be varied and modified within the scope of the claims set out below. The invention is not limited to the type of separator as shown in the Figures. The term “centrifugal separator” also comprises centrifugal separators with a substantially horizontally oriented axis of rotation and separator having a single liquid outlet.
| Number | Date | Country | Kind |
|---|---|---|---|
| 17168960 | May 2017 | EP | regional |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/EP2018/061012 | 4/30/2018 | WO |
| Publishing Document | Publishing Date | Country | Kind |
|---|---|---|---|
| WO2018/202611 | 11/8/2018 | WO | A |
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| 20210107014 A1 | Apr 2021 | US |
