Spiral separator for fluid purification equipment

Abstract

A separation device for a fluid purification device includes at least three concentric enclosures, including an outermost enclosure and an innermost enclosure, defining at least two concentric cavities; a plurality of spiral-shaped channels formed in each of the at least two concentric cavities so that a fluid can flow through the plurality of spiral-shaped channels; a fluid inlet located in an upper section of the outermost cavity of the at least two concentric cavities and receiving a fluid, the fluid inlet corresponding to the gas outlet; a solid outlet for discharging solids contained in the fluid, the solid outlet located in a lower section of the separation device; and a liquid outlet located in the upper section of at least one inner cavity of the at least two concentric cavities and discharging a liquid contained in the fluid.

Description

[Technical field]

[0001] This invention relates to a separation device for a fluid purification system and a method for separating liquids from solids and gases using the separation device, and more particularly to a separation device including a helically shaped channel. [Background technology]

[0002]

[0002] Separation or settling devices for fluid purification are known from the prior art. They can be used for the aerobic or anaerobic purification of fluids such as wastewater. The wastewater contains liquids and also usually contains dissolved and undissolved organic and / or inorganic matter in the form of solids or solid particles.

[0003]

[0003] Anaerobic wastewater treatment is the biological treatment of wastewater without the use of air or elemental oxygen. Many applications are directed to the removal of organic pollutants in wastewater, slurries and sludges. The organic pollutants are converted by anaerobic microorganisms into gases (biogas) including methane and carbon dioxide. Separation devices known in the art make it possible to separate the liquids, solids and gases (including biogas) that make up the fluid (wastewater) from each other.

[0004]

[0004] In an example disclosed in WO 96 / 32177, which is incorporated by reference, a separation device with a settling chamber is disclosed in which the caps are mounted with their longitudinal axis at an angle to the water level, forcing the fluid, including liquid, solids and gas, fed at the bottom of the separation device to flow obliquely upwards along the bottom of the cap. Gas bubbles are collected on a ridge placed in the cap. Under the cap, a laminar flow is achieved, promoting the deposition of solids contained in the fluid.

[0005]

[0005] Another example is disclosed in WO2010 / 036107A1, which is incorporated by reference, showing a separation device used in combination with different technologies (hybrid reactor system) such as anaerobic filters and / or anaerobic lagoons. The separation device of WO2010 / 036107A1 comprises a settling chamber configured to be filled with a fluid, a liquid discharger for discharging the liquid from the settling chamber, the liquid discharger arranged close to the liquid level, a fluid inlet for supplying the liquid to the settling chamber, a particulate matter separator, and a sludge outlet for discharging the sludge-containing fluid. The fluid inlet further comprises a gas separator for separating gas from the fluid, the gas separator comprising a channel.

[0006]

[0006] Settling devices in the art, such as WO96 / 32177 or WO2010 / 036107A1, achieve a certain separation efficiency but present some structural challenges. They require a cubic or prism structure, which may lead to non-uniform distribution of fluids when used in a circular reactor tank. The settling plates or caps need to have a certain angle, which requires the separation device to have a certain size. In addition, large flat settling plates or caps may not be robust enough against overpressure or overpressure. Summary of the Invention

[0007] In accordance with the present invention, a separation apparatus is provided which overcomes at least some of the problems discussed above.

[0008] According to a first aspect, the present invention provides a separation device for a fluid purification apparatus, comprising at least three concentric enclosures, including an outermost enclosure and an innermost enclosure, defining at least two concentric cavities, a plurality of helical shaped channels formed in each of the at least two concentric cavities such that a fluid can flow through the plurality of helical shaped channels, a fluid inlet located in an upper section of the outermost cavity of the at least two concentric cavities for receiving the fluid, a solid outlet located in a lower section of the separation device for discharging solids contained in the fluid, and a liquid outlet located in the upper section of at least one inner cavity of the at least two concentric cavities for discharging liquid contained in the fluid.

[0009] Advantageously, the present invention provides a separation device with a compact structure, comprising a plurality of concentric enclosures defining a plurality of cavities, forming in said cavities a helical shaped channel allowing a fluid to pass therethrough. The helical shaped channel formed in each cavity requires a smaller projected area compared to the rectangular / square inclined settling plates as used in the prior art, and provides a more robust structure capable of withstanding overpressure and pressure in a more effective manner.

[0010]

[0010] Liquids flow through the spiral-shaped channels of the different cavities and can exit the separation device through a fluid outlet located in the upper section of at least one inner cavity during operation, while solids can exit the separation device through a solid outlet located in the lower section of the separation device during operation, where the upper section of a cavity can be understood as the upper half of the cavity, or the upper third of the cavity, or even the top opening of the cavity.

[0011]

[0011] Concentric enclosures, also referred to as concentric structures, bodies, frames, etc., may have different shapes, so long as they are concentric, i.e. have a common longitudinal axis. They may have, for example, a tubular shape, such as a cylinder defined by a circular horizontal cross-section, an elliptical-cylindrical shape defined by an elliptical horizontal cross-section, or a polygonal shape, for example, defined by a rectangular (such as a square), hexagonal, or octagonal horizontal cross-section, or any other suitable shape.

[0012]

[0012] A concentric cavity may also be referred to as a concentric chamber or space in which the helical channel is located. Concentric enclosures and concentric cavities may be referred to simply as enclosures or cavities throughout the description.

[0013] A helical shaped channel according to the present invention can connect each concentric enclosure with the next such that the only way for fluid to flow is through the helical shaped channel.

[0014]

[0014] The helical shaped channel is also referred to as a channel throughout this specification, and the helical shaped wall is also referred to as a wall.

[0015] According to one embodiment, the helical shaped channels in each concentric cavity extend parallel to one another to define a single helix. The helical shaped channels preferably extend about a vertical axis, and the channels in each concentric cavity preferably extend parallel and in contact with one another to occupy the entire space within the cavity and define a single helix.

[0016]

[0016] According to one embodiment, the lower section of the separation device includes a redirection chamber located below the at least three concentric enclosures, the redirection chamber being configured to enable fluid to switch from a downward flow through multiple spiral-shaped channels of the outermost cavity to an upward flow through multiple spiral-shaped channels of at least one inner cavity.

[0017]

[0017] The fluid enters the separation device through the upper section of the outermost cavity. In the outermost cavity, the fluid flows downwards through a spiral-shaped channel. When the fluid reaches the bottom region of the outermost cavity, i.e. when it reaches the redirection chamber, which is a bounded space placed under at least three concentric enclosures, the fluid changes direction by its own energy and flows upwards through the spiral-shaped channel of at least one inner cavity. In this at least one inner cavity, the solids, due to their higher density, fall downwards against the flow of the fluid by contacting and sliding down the walls of the channel. Thus, the walls of the channel act as separation plates, like flat and straight separation plates known in the art. The fluid becomes cleaner as it flows upwards, and the clean liquid (water) reaches the upper section of at least one inner cavity.

[0018] According to one embodiment, the lower section of the separation device is placed under at least three concentric enclosures and comprises a solid collection chamber including a redirection chamber, and the solid outlet is placed at the bottom of the solid collection chamber. The lower section refers to the section placed under the concentric enclosures. The solid collection chamber collects the solids that separate from the fluid and slide downwards through the spiral-shaped channels of the cavity. The upper end of the solid collection chamber may be connected or fixed to the bottom of the outermost enclosure, thereby forming a space called a redirection chamber in the upper part of the solid collection chamber, where the fluid that reaches the bottom of the outermost cavity can change from a downward flow to an upward flow and continue to flow upwards through the spiral-shaped channels of at least one inner cavity.

[0019]

[0019] According to one embodiment, the fluid inlet corresponds to the gas outlet. In the outermost cavity, as the liquid and solids contained in the fluid flow downwards, the (most) gas particles move upwards and exit the separation device through the gas outlet (which is the same or partially the same as the fluid inlet). Thus, a gas separation phase occurs in the outermost cavity and a solid separation phase occurs in at least one inner cavity, so that when the fluid reaches the upper section of the at least one inner cavity, it becomes a pure water-like liquid, now free or almost free of any solid and gas particles.

[0020] According to one embodiment, the top of the outermost cavity is open to define the outermost top opening, and the fluid inlet comprises an area formed by the outermost top opening. The top end of the outermost cavity may be uncovered or closed, and the separation device is preferably placed inside the reactor and its top is at or below the water level, so that the fluid in the reactor can enter the separation device from all directions, not just from the specific location where the inlet is placed. Thus, the fluid inlet may be defined as the total area defined by the open top end of the outermost cavity, also referred to as the outermost top opening. Allowing the fluid to enter the separation device from all directions has the advantage of improving flow distribution and simplifying the system design, since the specific location where the inlet is placed does not need to be considered.

[0021] According to one embodiment, the separation device further comprises a demarcation structure for separating the outermost top opening from at least one internal top opening, also referred to as the top opening of the at least one internal cavity, which ensures that the outermost top opening, which may form the fluid inlet (and may form the gas outlet), is separated from the opening of the at least one internal cavity, so that the fluid flowing in through the fluid inlet and the clean liquid flowing out through the liquid outlet do not come into contact with each other.

[0022] According to one embodiment, the boundary structure includes a boundary enclosure placed above and in contact with a second outermost concentric enclosure, and at least one internal top opening is enclosed by the boundary enclosure and the innermost enclosure, thereby forming a liquid collection section. The liquid collection section is a section for collecting liquid that is (almost) free of solids and gases, such as clean water. The liquid collection section may be located above the concentric enclosure bounded by the boundary enclosure and the innermost enclosure, and the liquid flowing upward through the spiral-shaped channel of the at least one internal cavity may reach the liquid collection section according to its natural flow.

[0023] According to one embodiment, the innermost enclosure comprises at least one collection opening in its upper section, which allows liquid in the liquid collection section to flow into the internal chamber, and the separation device further comprises at least one liquid collection tube protruding from the innermost enclosure towards the outside of the separation device to collect liquid in the internal chamber. The innermost enclosure may be higher than the other enclosures, or an additional enclosure may be attached to the top of the innermost enclosure, so that the part of the innermost enclosure that exceeds the height of the other concentric enclosures is considered as the upper section. This upper section may confine the liquid collection section, and at least one collection opening is preferably located in this section so that liquid from the liquid collection section can flow into the internal chamber.

[0024] According to one embodiment, the liquid collection section comprises at least one dividing element, so as to divide the liquid collection section into at least two compartments, and the innermost enclosure comprises at least one collection opening for each of the at least two compartments. The dividing element may comprise at least one dividing wall, which extends radially from the innermost enclosure towards and contacts the delimiting enclosure, thereby dividing the liquid collection section into at least two compartments, preferably four compartments, with at least one collection opening for each compartment, so that water can flow through the different compartments into the internal chamber.

[0025] According to one embodiment, the separating device comprises a compartment control mechanism that closes at least one of the collection openings, thereby preventing liquid from exiting said at least one compartment. The compartment control mechanism makes it possible to close the collection openings of one or more compartments, and thus to control the rate at which clean water exits the separating device.

[0026]

[0026] According to one embodiment, the multiple spiral-shaped channels are defined by a spiral-shaped wall having an inner region and an outer region relative to a vertical cross-section of the concentric structure, and the spiral-shaped wall curves upwardly from the inner region to the outer region or curves downwardly from the inner region to the outer region.

[0027]

[0027] The plurality of helical shaped channels may be defined by helical shaped walls with an upper end placed at the top of the enclosure and a lower end placed at the bottom of the enclosure, with the fluid flowing through the channel flowing from the upper end to the lower end or from the lower end to the upper end. Each wall also has two faces, a front and a back face, the front face being the face with which the solid particles mainly contact and through which they slide down. With respect to the vertical cross section (as can be clearly seen from the drawing), the inner area of ​​the wall extends close to and includes the inner edge of the wall. The helical shaped walls may connect one enclosure to the next concentric enclosure. In one embodiment, the horizontal cross section of each wall defines a line extending radially towards the center of the concentric enclosure. In such a configuration, the walls may have a flat surface extending from the upper end to the lower end. In another more preferred configuration, the walls are arranged such that the horizontal cross section of each wall does not extend radially towards the center, but has a specific inclination angle with respect to said direction. In this configuration, the wall surface from the upper end to the lower end is not flat, but is curved downward from the inner region to the outer region in an arched or concave shape, or curved upward from the inner region to the outer region in an arched or convex shape.

[0028] According to one embodiment, the spiral-shaped walls of the outermost cavity are curved downward from the inner region to the outer region, and the spiral-shaped walls of the at least one inner cavity are curved upward from the inner region to the outer region. This configuration provides the advantage of allowing a solid contacting the walls to slide downward close to the outer region in the outermost cavity, and also allowing a solid to move downward close to the inner region in at least one inner cavity.

[0029] According to one embodiment, the distance between each concentric enclosure and the next is between 25 mm and 800 mm, preferably between 50 mm and 800 mm, more preferably between 50 mm and 500 mm, more preferably between 50 mm and 200 mm. In the case of smaller separating devices, distances between 25 mm and 200 mm, preferably between 25 mm and 100 mm, are also preferred.

[0030] According to one embodiment, the at least three concentric enclosures correspond to at least three concentric tubes and the at least two concentric cavities correspond to at least two concentric rings. In a preferred embodiment of the invention, the enclosure has a tubular shape, such as a cylinder, defined by a circular horizontal cross section. In this preferred embodiment, the cavity defined thereby has a ring shape. This allows the separation device to fit into a circular reactor tank and provides a uniform fluid distribution that cannot be achieved with a separation device having a rectangular horizontal cross section. Furthermore, the cylindrical shape combined with the helical shaped channel provides a much more rigid structure of the separation device and allows the wall thickness to be reduced, since the walls forming the channels are no longer long and straight.

[0031] According to one embodiment, the separation device includes at least four concentric enclosures defining at least three concentric cavities. This structure provides one outermost cavity through which fluid can flow downwards and at least two inner cavities for fluid to flow upwards. In the concentric structure, the outermost enclosure has a larger diameter and can therefore include more channels than the inner cavities, thereby carrying more fluid. By having at least two inner cavities, the channels of the inner cavities can have more suitable dimensions and the system can provide better performance.

[0032] According to one embodiment, the solids collection chamber has a hollow inverted cone shape. If the concentric enclosure has a cylindrical shape, the solids collection chamber may have a cone shape such that the base of the cone is open and the periphery is connected to the outermost cylinder.

[0033] According to one embodiment, the separator further comprises a ventilation device located in the outer part of the lower half of the solids collecting chamber and supplying gas (biogas or air) from below the separator, thereby controlling the volume of gas generated in the reactor in which the separator is located and thus controlling the density difference between the liquids, solids and gas outside the separator and the liquids and solids inside the separator, thereby achieving a desired flow of the liquids and solids inside the separator.

[0034] According to one embodiment, the plurality of helical channels are defined by helical walls having an irregular surface. The wall surface, whether it is the front or back surface, may be smooth and not wrinkled. However, the wall surface may also be irregular, non-uniform or corrugated. This may improve gas separation.

[0035]

[0035] According to a second aspect, the present invention provides a method for separating a fluid containing liquids, gases and solids, performed by a separation apparatus comprising at least three concentric enclosures including an outermost enclosure and an innermost enclosure, the at least three concentric enclosures defining at least two concentric cavities, and a plurality of helical shaped channels formed in each of the at least two concentric channels, the method comprising the steps of receiving a fluid via an upper section of an outermost of the at least two concentric cavities, and causing the fluid to flow downwardly through the plurality of helical shaped channels of the outermost cavity. allowing the fluid to switch from a downward flow through the multiple spiral-shaped channels of the outermost cavity to an upward flow through the multiple spiral-shaped channels of the at least one inner cavity when the fluid reaches a redirection chamber located below the outermost cavity, and allowing the liquid to exit the separation device when it reaches an upper section of the at least one inner cavity where it is converted to liquid; and allowing the solids to move downward through the multiple spiral-shaped channels of the outermost cavity and through the multiple spiral-shaped channels of the at least one inner cavity and exit the separation device through the lower section of the separation device.

[0036]

[0036] Furthermore, according to one embodiment, the method further includes a step of allowing gas to move upward and exit the separation device through an upper section of the outermost cavity while the fluid flows downward through the multiple spiral-shaped channels of the outermost cavity.

[0037] According to one embodiment, receiving the fluid through the upper section of the outermost cavity includes receiving the fluid through the entire area of ​​the outermost top opening.

[0038]

[0038] According to one embodiment, the step of allowing liquid to flow out of the separation device through the upper section includes a process of allowing the liquid to reach a liquid collection section located above the at least three concentric enclosures.

[0039]

[0039] According to one embodiment, the method further includes a step of allowing liquid in the liquid collection section to flow through at least one collection opening into an internal chamber in the innermost cavity, and a step of allowing liquid to flow out of the separation device through at least one liquid collection tube connected to the innermost enclosure.

[0040]

[0040] According to one embodiment, the step of allowing the solids to flow out of the separation apparatus through the lower section of the separation apparatus includes allowing the solids to move downwardly toward a solids collection chamber located below the at least three concentric enclosures.

[0041] According to one embodiment, the method further comprises supplying gas from below the separator through a vent located on the exterior of the lower half of the solids collection chamber.

[0042]

[0042] According to one embodiment, the multiple spiral-shaped channels are each defined by a multiple spiral-shaped walls, each spiral-shaped wall including an inner region and an outer region, and the method further includes directing, in the outermost cavity, solids contained in the fluid flowing downwardly toward the outer region of the spiral-shaped wall, and in at least one inner cavity, directing solids contained in the fluid flowing upwardly toward the inner region of the spiral-shaped wall.

[0043]

[0043] According to one embodiment, the liquid collection section is divided into at least two compartments, and the method further includes a step of controlling the liquid collection section to close at least one compartment, thereby preventing liquid from flowing out of said compartment. [Brief description of the drawings]

[0044] The invention will now be described in more detail with reference to the accompanying drawings. [Figure 1A] FIG. 1A illustrates a vertical cross-section of a separation device according to one embodiment of the present invention. [Figure 1B] FIG. 1B illustrates a horizontal cross-section of a separation device according to one embodiment of the present invention. [Diagram 2] FIG. 2 shows a vertical cross-section of a separation device according to one embodiment of the present invention when placed inside a reactor tank. [Diagram 3] FIG. 3 shows a perspective view of a portion of a separation device according to one embodiment of the present invention. [Figure 4] FIG. 4 shows another perspective view of a portion of a separation device according to one embodiment of the present invention. [Diagram 5] FIG. 5 shows another perspective view of a portion of a separation device according to one embodiment of the present invention. [Figure 6A] FIG. 6A illustrates a vertical cross section of a separation device according to one embodiment of the present invention. [Figure 6B] FIG. 6B illustrates a horizontal cross-section of a separation device according to one embodiment of the present invention. [Figure 7] FIG. 7 shows an expanded view of a portion of a separation device according to one embodiment of the present invention. [Figure 8] 8 shows another perspective view of a portion of a separation device according to one embodiment of the present invention. These views are for illustrative purposes only and do not serve as a limitation on the scope or protection provided by the claims. Description of the embodiments

[0045]

[0056] The application of the purification process using the separation device according to the invention comprises a reactor tank. Examples include aerobic, anaerobic or anoxic reactors. Anaerobic granular sludge bed technology refers to a reactor concept or purification device for anaerobically treating wastewater.

[0046]

[0057] Preferably, the top, preferably the top edge or surface, of the separation device of the present invention is placed at the water level in the aerated reactor tank, with the remainder of the separation device being placed below the water level, because in such a tank, the density difference between the (aerated) outside of the separation device and the (non-aerated) inside of the separation device creates a fluid flow through the separation device, which returns settled solids or solid particles from the separation device to the same or another reactor tank in the fluid separation device. However, in another embodiment, the separation device can be placed completely below the water level or even at the bottom of the reactor.

[0047]

[0058] The reactor, such as an upflow anaerobic sludge blanket (UASB) or expanded granular sludge bed (EGSB), or an aerobic reactor, according to the invention comprises a tank with a fermentation chamber. Wastewater is distributed into the tank, in one embodiment, with appropriately spaced inlets. The wastewater passes upwards through a (n-anaerobic) sludge bed, and the microorganisms in the sludge come into contact with the wastewater substrate. In one embodiment, the anaerobic digestion process obtained in the fermentation chamber produces gases (e.g., CH4, CH5, CH6, CH7, CH8, CH9, CH10, CH11, CH12, CH13, CH24, CH30, CH45, CH46, CH47, CH48, CH49, CH50, CH51, CH52, CH53, CH54, CH55, CH56, CH57, CH58, CH59, CH66, CH67, CH68, CH69 ... 4 and CO 2 The upward movement of the released air bubbles creates turbulence in the hydraulics that provides mixing in the reactor without mechanical parts. The fluid is in continuous motion in the fermentation chamber due to the gas flow upward through the fluid towards the liquid level.

[0048]

[0059] Preferably, at the top of the reactor, the aqueous phase is separated from the sludge solids and gases in a three-phase separator (also known as a gas-liquid-solid separator), settler or separator, which is the object of the present invention.

[0049]

[0060] Although the present invention will be described generally in terms of fluids, a preferred application is wastewater, and those skilled in the art will recognize that other suitable fluids may be used.

[0050]

[0061] Before proceeding to a detailed description of the drawings, it should be noted that throughout this application, terms such as upper, lower, upper section / lower section, top / bottom, etc. are used. Although not specifically indicated, these definitions refer to the position in which the separation apparatus is in operation or ready to be in operation.

[0051]

[0062] Also, terms such as vertical cross-section and horizontal cross-section are used throughout this specification. A vertical cross-section should be understood as a cross-section made along a longitudinal plane that includes a longitudinal axis (represented by X in at least some of the figures), and a horizontal cross-section should be understood as a cross-section made along a transverse plane that includes a transverse axis (represented by Y in at least some of the figures). Like numbers refer to the same features throughout the figures.

[0052]

[0063] Figure 1A illustrates a vertical cross-section of a separation device according to one embodiment of the present invention. Figure 1B illustrates a horizontal cross-section of a separation device according to one embodiment of the present invention. Both figures provide complementary information and some features may be better understood in one figure or the other, so they are described together.

[0053]

[0064] The separation device 1 according to Figures 1A and 1B comprises a concentric structure including at least three concentric enclosures, of which there is an outermost enclosure 10 and an innermost enclosure 12. The at least three concentric enclosures define at least two concentric cavities, including an outermost cavity 11 and one or more inner cavities 13. In the embodiment of Figures 1A and 1B, the concentric enclosures correspond to concentric tubes, more specifically concentric cylinders, with a circular horizontal cross section, and the cavities correspond to rings. It should be noted, however, that although this is one possibility, one preferred embodiment, the concentric enclosures can have a polygonal shape, for example defined by a rectangular (even square) horizontal cross section, a hexagon, an octagonal horizontal cross section, or any other suitable shape.

[0054]

[0065] Moreover, the embodiment of Fig. 1A and Fig. 1B shows four concentric enclosures defining three concentric cavities. This is the preferred embodiment, with the outermost cavity 11 corresponding to the degassing section where the degassing phase can take place, and the two inner cavities 13 corresponding to the settling section where solids separation can take place. This settling section is therefore divided into two cavities. This configuration is advantageous since the length A of the circular sector defining the helical shaped channel 14, for the inner cavity 13, may otherwise be too small if only one inner cavity is used. By using at least two inner cavities 13, the number of helical shaped channels 14 in each inner cavity can be reduced while maintaining a sufficient length for A. Moreover, the angle of the helical shaped channel 14 with respect to the vertical plane is smallest in the outermost cavity and increases towards the inner cavities. If only one inner cavity was used, this angle would be too steep for the inner cavities. By using at least two inner cavities, the angle of the channel 14 within the inner cavity 13 (ie, the pitch of the helical channel) can be reduced.

[0055]

[0066] Distance B represents the width of the concentric cavities, which is the same or substantially the same as the width of the channel 14. Distance B can have a value between 25 mm and 800 mm, preferably between 50 mm and 800 mm, more preferably between 50 mm and 500 mm, and even more preferably between 50 mm and 200 mm. For smaller separation devices, distances between 25 mm and 200 mm, preferably between 25 mm and 100 mm, are also preferred. As can be seen in FIG. 1B, distance B is smaller in the outermost cavity 11 than in the second outermost cavity or intermediate cavity, which is at the same time smaller than distance B in the innermost cavity. However, this is an example and other lengths of B can be used. The values ​​of A and B for the channels in the outermost cavity 11 are determined such that their ratio and the size of the channels allow gas to move up and out of the device. On the other hand, the values ​​of A and B for the inner cavity 13 depend on the fluid properties, since their ratio and the size of the channels are determined such that they allow solids to move downwards relative to the liquid flow.

[0056]

[0067] To ensure that the water flow velocities in the two inner cavities are equal, the pressure drop in both inner cavities 13 must be equal. Pressure drop is defined as the difference in total pressure between two points in a fluid transport network, and pressure drop occurs when a fluid flows through a tube and is subjected to frictional forces caused by resistance to flow. The pressure drop depends on the friction factor, the density of water, the length from the top to the bottom of the helical channel 14, i.e., the path length the fluid must travel in the channel 14, the hydraulic diameter of the channel 14, and the velocity of the fluid.

[0057]

[0068] With this in mind, the number of channels, the pitch of the helical channel, and the diameter of the sections can be selected such that the velocities in both sections are equal.

[0058]

[0069] Embodiments are possible that include two concentric enclosures defining three concentric cavities, and also embodiments are possible that include four or more concentric enclosures defining three or more concentric cavities.

[0059]

[0070] The separation device 1 further comprises a fluid inlet 15 located in an upper section of the outermost cavity 11. The upper section is preferably the upper half or upper third, and more preferably the fluid inlet 15 is formed in a top of the outermost cavity 11 that is preferably uncovered so as to define an outermost top opening, the fluid inlet 15 including the area formed by the outermost top opening. In such a configuration, fluid within the reactor tank in which the separation device is located can enter the separation device from any direction, not just from the specific location where the inlet is located.

[0060]

[0071] The fluid inlet 15 may also act as a gas outlet; that is, as fluid flows downward through the spiral-shaped channel 14 of the outermost cavity 11, gas particles separate from the fluid, travel upward, and exit the separation device through the gas outlet (fluid inlet). A gas collection system including a tube may be used to collect the gas, or the gas may simply rise up and exit the separation device 1.

[0061]

[0072] In operation, below the concentric structure, a solids collection chamber 20 is placed, connected or added to the bottom end of the outermost enclosure 10 to define a chamber called a redirection chamber, where the fluid can use its own energy to redirect from a downward flow to an upward flow after reaching the bottom of the spiral-shaped channel 14 of the outermost cavity 11. The fluid can then flow upward through the spiral-shaped channel 14 of at least one inner cavity 13, which in this embodiment are two inner cavities. While the fluid flows downward through the channel 14 of the outermost cavity 14 and upward through the channel 14 of the inner cavity 13, the solid particles, due to their high density and friction with the surface of the channel 11, separate from the liquid, drop and settle to the bottom of the solids collection chamber 20, and then exit the solids collection chamber 20 through a solids outlet 22, preferably placed at the bottom of the solids collection chamber.

[0062]

[0073] The solids collection chamber 20 can have several shapes. However, in the embodiment of Figures 1A and 1B, it has a conical shape for improved attachment with the concentric structure, which can be achieved by attaching or engaging the periphery of a conical base to the bottom of the outermost enclosure 10. However, it should be noted that other shapes are possible as long as there is space to allow the solids collection chamber 20 to collect and remove solids from the separation device 1 and to allow fluid to exit the channels 14 of the outermost cavity 11 and flow into the channels 14 of at least one inner cavity 13.

[0063]

[0074] 1A and 1B also show a liquid collection section 30 and a liquid outlet with at least one liquid collection tube 36. The liquid collection section 30 may be surrounded or bounded by the innermost enclosure 12 and a bounding structure that separates the top opening of the outermost cavity 11 from the top opening of the inner cavity 13. This bounding structure is preferably a bounding enclosure 31 having a shape similar to the other concentric enclosures and having one end attached and disposed on top of the second outermost enclosure. This bounding enclosure can also be clearly seen in FIG. 4, which is described in more detail below.

[0064]

[0075] The innermost enclosure 12 may be solid or (partially) hollow. If it is (partially) hollow, it may define an internal chamber 35 that may contribute to the collection of liquid (clean water). The innermost enclosure 12 may have a height H1 higher than the height H of the other concentric enclosures, or alternatively, an additional enclosure may be attached to the upper section of the innermost enclosure providing a higher height defining the upper section, so that the upper section (of height H2) may act as a wall defining the boundary of the liquid collection section 30. In the upper section of the innermost enclosure 12, at least one collection opening 34 (visible in FIG. 4) may be present so that the liquid in the liquid collection section 30 flows into the internal chamber 35 and is stored therein. The liquid may then be drained by at least one liquid collection tube 36, which is connected to the innermost enclosure 12 and collects the liquid stored therein. As can be seen with reference to FIG. 4, the liquid collection section can be divided into sections.

[0065]

[0076] The helical shaped channel can be defined by helical shaped walls connecting each enclosure with the next enclosure, as in the case of Figures 1A and 1B. The helical shaped channel can also be defined by helical shaped hollow members or hollow arms with a horizontal cross section of a polygon, such as a rectangle (square), or other kind of polygon, circular or elliptical, which fit into the cavity and are attached to each other and to the enclosures that define the cavity. In a preferred embodiment, the helical shaped channel is defined by walls connecting each enclosure with the next enclosure. In another preferred embodiment, the helical shaped channel is defined by hollow arms with a horizontal cross section of a square or rectangle. These embodiments are preferred because they allow better utilization of space and therefore allow higher fluid volumes.

[0066]

[0077] In the embodiment of Figures 1A and 1B, the multiple helical shaped channels 14 are defined by helical shaped walls 19, which have upper and lower ends and which connect one enclosure to the next concentric enclosure. These helical shaped walls 19 have a front (or top) surface through which fluid flows, i.e. the surface that is mostly in contact with solids, and a back (or bottom) surface. The helical shaped walls also have, in a vertical cross section, an inner region 17 that extends along the entire length of the wall adjacent to and including the inner edge, and an outer region 18 that also extends adjacent to and including the outer edge.

[0067]

[0078] 1A and 1B, the horizontal cross section of each wall 19 defines a line extending radially toward the center of the concentric enclosure, the line having a length substantially the same as the width of the concentric cavity in which it is located (distance B). In such a configuration, the wall has a flat surface extending from its upper end to its lower end.

[0068]

[0079] Figure 2 shows a vertical cross-section of a separation device according to one embodiment of the present invention when placed inside a reactor tank. In Figure 2, the separation device 1 is placed inside a reactor tank, which may be an aerobic or anaerobic reactor.

[0069]

[0080] The separation device 1 in the embodiment of FIG. 2 is placed in the upper part, for example in the upper half, of the reactor 2, with its top at or below the fluid level 3. However, the separation device 1 can also be located elsewhere inside the reactor, and the working principle remains the same. For example, the separation device 1 can be placed near or at the bottom of the reactor. A method for separating liquids, solids and gases in a fluid is described in relation to FIG. 2.

[0070]

[0081] In step 1), a fluid such as wastewater containing liquids, solids and gas is received by the separation device 1 through a fluid inlet 15 located in the upper section of the outermost cavity 11, which in this case corresponds to the entire upper opening of the outermost cavity 11. Then, in step 2, the fluid can flow downwards through the spiral-shaped channels 14, the (most) gas contained in the fluid separates from the fluid, in part due to friction between the fluid and the surface of the walls defining the channels, which may be smooth or irregular, and the gas moves upwards and leaves the separation device through the gas outlet corresponding to the fluid inlet 15. In step 3), after the fluid reaches the bottom region of the outermost cavity 11, it reaches a redirection chamber, which is part of the solid collection chamber 20 and is a bounded space in which the fluid can be switched from a downward flow to an upward flow and flow upwards through the multiple spiral channels 14 of at least one internal cavity 13. When the solids reach the upper section of at least one inner cavity 13, converted into liquid, they can flow out of the separation device. Step 4) corresponds to allowing the solids to flow out of the separation device through the lower section of the separation device, preferably through the solid outlet 22 located at the bottom of the solid collection chamber 20, while the solids move downwards through the multiple spiral-shaped channels 14 of the outermost cavity 11 and are moved downwards through the multiple spiral-shaped channels 14 of the at least one inner cavity 13. In step 5), the liquid (clean water) that has reached the upper section flows into the liquid collection section 30, from where it can access, for example, the internal chamber 35 of the innermost enclosure 12 through at least one collection opening 34. A liquid collection tube 36 or any other liquid discharge element is connected to the innermost enclosure 12, and in step 6) the liquid stored therein can be removed. If there is no internal chamber 35, the liquid in the liquid collection section 30 can be directly connected by at least one tube.

[0071]

[0082] Figure 3 shows a perspective view of a part of a separation device according to an embodiment of the invention. In Figure 3, the top of the helical shaped channel 14 in the different concentric cavities can be seen. Also visible is a horizontal cross section of the helical wall 19 that defines the helical shaped channel 14, which extends radially towards the center of the concentric enclosure. Distance B represents the width of the concentric cavity and is the same or substantially the same as the width of the helical shaped channel 14 formed in this cavity. As mentioned above with respect to Figures 1A and 1B, distance B can have different values.

[0072]

[0083] FIG. 4 shows another perspective view of a portion of a separation device according to an embodiment of the present invention. FIG. 4 focuses on the liquid collection section 30 located above the concentric enclosure. It should be noted that the configuration shown in FIG. 4 is an example, and other configurations are possible, so that this liquid collection section 30 may have different elements than the configuration shown in FIG. 4. The embodiment of FIG. 4 shows a demarcation enclosure 31, which is added to the top of the second outermost enclosure and has a height that may be substantially the same as the additional height H2 of the innermost enclosure 12 (see FIG. 1A). The height of the demarcation enclosure 31 may also be greater than the height H2, so that liquid in the liquid collection section 30 or inside the internal chamber 35 does not spill or flow out of the separation device.

[0073]

[0084] As can be seen in the embodiment of Figure 4, the innermost enclosure 12 comprises at least one collection opening 34 in its upper section (a section of height H2 extending beyond the height of the other concentric enclosure, which may be part of the innermost enclosure or an additional enclosure attached on top of the innermost enclosure) to allow liquid in the liquid collection section 30 to flow into the internal chamber 35. At least one liquid collection tube 36 or other liquid discharge means may protrude from the innermost enclosure 12 towards the outside of the separation device 1 to collect liquid from the internal chamber 35.

[0074]

[0085] 4 shows four boundary defining elements 32 dividing the liquid collection section 30 into four compartments 33. However, it should be noted that while this is the preferred embodiment, there may be a different amount of boundary defining elements and compartments. The boundary defining elements 32 in the embodiment of FIG. 4 comprise dividing walls that extend radially from the innermost enclosure 12 to a position within the boundary defining enclosure 31, thereby dividing the liquid collection section 30 into multiple compartments 33.

[0075]

[0086] The advantage of having multiple compartments is that one or more of these compartments can be closed. This mechanism allows the velocity of the fluid in the separation device to be controlled. The innermost enclosure 12 can include multiple collection openings 34, such that at least one collection opening 34 connects each compartment to the internal chamber 35. The separation device can include a compartment control mechanism that closes or opens at least one of the collection openings 34 based on the desired velocity of the liquid in the separation device. The compartment control mechanism can include a cover or sealing structure that closes at least one of the collection openings 34. The control mechanism can be manually controlled or automatically controlled by a sensor system.

[0076]

[0087] In the embodiment of Fig. 4, the boundary defining elements 32 extend radially according to the radial distribution of the helical wall (as can be clearly seen in Fig. 1B). However, the boundary defining elements 32 can have a different shape adapted to the distribution of the helical wall. As can be seen with respect to Figs. 6 to 8, in the case where the helical wall does not extend radially, the boundary defining elements 32 have a shape adapted to the horizontal cross-section of the wall so as to effectively define a section of the liquid collection section 30.

[0077]

[0088] FIG. 5 shows another perspective view of a portion of a separation apparatus according to an embodiment of the present invention. In particular, FIG. 5 shows an enlarged view of a solids collection chamber 20, which is an example embodiment having an inverted cone shape with an open bottom and an edge area of ​​the bottom that contacts the lower end of the outermost enclosure 10. A solids outlet 22 is located at the bottom of the solids collection chamber 20. In addition, the solids collection chamber 20 may include a stopper 24, which is located below the solids outlet 22 and configured to prevent air from entering the solids collection chamber 20 while allowing solids to flow out through the solids outlet 22. It is preferable, but not limited to, that the stopper 24 be cone-shaped.

[0078]

[0089] According to one embodiment, the separator further comprises an aeration device, which is placed in the outer part of the lower half of the solids collection chamber and supplies gas (biogas or air) from below the separator. The flow of liquids and solids through the separator is driven by the density difference between the liquids, solids and gas outside the separator, and only the liquids and solids inside the separator. This density difference depends on either the gas (e.g. biogas) generating means or the aeration means required to supply oxygen to the aeration reactor in which the separator is placed. However, the generated gas volume is not necessarily the correct gas volume for efficient water and sludge flow over the separator. This can be avoided by having a dedicated aeration device to supply either air or biogas from below the separator. Preferably, the aeration device is placed in the lower half of the solids collection chamber 20, outside the solids collection chamber 20, close to or in contact with the outer surface of the solids collection chamber 20, above the solids outlet 22. The aeration device may comprise a pipe system having at least one pipe with at least one opening, preferably a plurality of openings, so that gas can be fed to the reactor through the openings, thereby controlling the amount of gas produced, controlling the density difference between the outside of the separation device and the inside of the separation device, and obtaining an efficient flow of liquids and solids through the separation device.

[0079]

[0090] Figure 6A illustrates a vertical cross-section of a separation device according to one embodiment of the present invention. Figure 6B illustrates a horizontal cross-section of a separation device according to one embodiment of the present invention. The embodiment of Figures 6A and 6B is similar to the embodiment of Figures 1A and 1B, and similar features will not be described.

[0080]

[0091] However, the helical channels 14 of the embodiment of Figures 1A and 6B have a different shape than those of Figures 6A and 1B. The multiple helical channels 14 of Figures 6A and 6B are defined by helical walls 19, but the helical walls 19 are not flat and their horizontal cross sections do not extend radially towards the center of the concentric structure. Instead, as shown in Figure 6B, which will be described in more detail later, the helical walls 19 are arranged such that the horizontal cross section of each wall 19 is inclined relative to said direction to form a specific angle α.

[0081]

[0092] Due to its shape, the helical wall 19 is not flat, but has either an inner section 17 curving downwards towards the outer section 18 to form a concave shape, or an inner section 17 curving upwards towards the outer section to form a convex shape, relative to a vertical cross section as seen in FIG. 6B. In this embodiment, solids contained in the fluid tend to move towards one section or the other of the wall 19 during the downward or upward flow of the fluid, thereby having the advantage of directing the solids to a desired location within the separation device. In a preferred embodiment, the multiple helical walls 19 of the outermost cavity 11 have an inner section 17 curving downwards towards the outer section 18, allowing the solids to move downwards as they approach the outer edge, i.e. the outermost concentric enclosure 10. This allows the solids to reach the solids separation chamber 20 closer to the conical wall, and therefore slide and settle more quickly at the bottom of the solids separation chamber 20. In a preferred embodiment, the multiple helical shaped walls 19 of at least one inner cavity 13 cause the inner region 17 to curve upwardly towards the outer region 18, allowing solids to move downwardly as they approach the inner edge, i.e., the innermost concentric enclosure 12. In an inner cavity 13 in which liquid is moving upwardly through a helical shaped channel 14, the shape of the walls 19 defining the channel 14 is such that solids will tend to move towards the center towards the inner edge, thereby dropping almost directly to the bottom of the solids collection chamber 20 taking the shortest path.

[0082]

[0093] The value of the angle α determines the radius of the curve that the helical wall 19 defines from the inner zone 17 to the outer zone 18. A larger angle α means a deeper concave-convex shape as described above. The smaller the α, the closer the cross section of the wall is to the radius of the concentric enclosure and the flatter the surface of the wall. Furthermore, if α has a positive value (as in the inner cavity of FIG. 6B), it is determined that the inner zone 17 hardens upwards towards the outer zone 18 (as seen in the inner cavity of FIG. 6A), and if α has a negative value (as in the outermost cavity of FIG. 6B), it is determined that the inner zone curves downwards towards the outer zone (as seen in the outermost cavity of FIG. 6A).

[0083]

[0094] Figure 7 shows an enlarged view of a portion of a separation device according to an embodiment of the present invention, specifically, a partial vertical cross-section showing the center of the concentric enclosure at the far right of the figure, indicated as VII in Figure 6A). In Figure 7, it can be seen more clearly that in one embodiment, the spiral-shaped walls 19 of the outermost cavity 11 have an inner section 17 that curves downwards towards the outer section 18 with respect to the vertical cross-section, and that solids, indicated as black circles in the figure, tend to move downwards as they approach the outermost concentric enclosure, while gas, indicated as white circles in the figure, tends to move upwards in the opposite direction. It can also be seen that the spiral-shaped walls 19 of at least one inner cavity 13 (in this embodiment, two inner cavities 13) curve the inner section upwards towards the outer section, allowing solids to move downwards as they approach the innermost concentric enclosure.

[0084]

[0095] Figure 8 shows another perspective view of a part of a separation device according to an embodiment of the invention. The representation in Figure 8 is very similar to that in Figure 3, but it can be seen from Figure 8 that the horizontal cross-section of the wall 19 defining the helical shaped channel 14 defines an angle α with the radial direction and therefore does not follow the radial direction as in the embodiment of Figure 3.

[0085]

[0096] These diagrams are for illustrative purposes only and do not serve as a limitation on the scope or protection defined by the claims.

[0086]

[0097] Although the invention has been described with reference to exemplary embodiments, those skilled in the art will recognize that various modifications may be made and equivalents may be substituted for the elements without departing from the scope of the invention. In addition, many modifications may be made to adapt a particular situation or material to the teachings of the invention without departing from the essential scope thereof. Therefore, it is not intended that the invention be limited to the particular embodiments disclosed, but the invention is intended to include all embodiments falling within the scope of the appended claims.

[0087]

[0098] In particular, combinations of specific features of the various aspects of the invention may be made. One aspect of the invention may be further advantageously enhanced by the addition of features that have been described in relation to another aspect of the invention.

[0088]

[0099] It is to be understood that the present invention is limited only by the appended claims and their technical equivalents. In this specification and its claims, the verb "comprise" and its conjugations are used in an open-ended sense meaning that the items following the word are included without excluding items not specifically mentioned. Furthermore, reference to an element by the indefinite article "a" or "an" does not exclude the possibility that more than one of the element is present, unless the context clearly requires that only one of the element is present. Thus, the indefinite article "a" or "an" generally means "at least one."

[0089] Explanation of symbols

[0090] Similar reference numbers used in the description to indicate similar elements (but differing only in 100) are omitted from the following list but should be considered implicitly included. 1...separation device, 2…Reactor tank, 3…Fluid level, 10…outermost enclosure, 11…Outermost cavity 12…innermost enclosure, 13…Inner cavity 14...spiral shaped channel, 15...Fluid inlet = gas outlet, 17... an inner area of ​​the spiral wall relative to a vertical cross section; 18...Outer area of ​​the spiral wall relative to the vertical cross section; 19...Spiral shaped wall, 20...solids collection chamber, 22...solid outlet, 24…Stopper, 30...liquid collection section, 31… Demarcation Enclosure, 32...Division element, 33…plot, 34...collection opening, 35...inner chamber, 36...Liquid collection tube.

Claims

1. In a separation device (1) of a fluid purification device, the separation device comprises: at least three concentric enclosures, including an outermost enclosure (10) and an innermost enclosure (12), defining at least two concentric cavities; a plurality of helical shaped channels (14) formed in each of said at least two concentric cavities such that a fluid can flow through the plurality of helical shaped channels; a fluid inlet (15) for receiving a fluid, the fluid inlet (15) being located in an upper section of the outermost cavity of the at least two concentric cavities and corresponding to the gas outlet; a solids outlet (22) for discharging solids contained in the fluid, the solids outlet (22) being located in a lower section of the separation device; a liquid outlet located in an upper section of at least one of the at least two concentric cavities, for discharging liquid contained in the fluid; Equipped with The separation device (1), wherein the lower section of the separation device comprises a redirection chamber located below the at least three concentric enclosures, the redirection chamber configured to allow the fluid to switch from a downward flow through the plurality of spiral-shaped channels (14) of the outermost cavity (11) to an upward flow through the plurality of spiral-shaped channels (14) of the at least one internal cavity (13).

2. 2. A separation device (1) according to claim 1, wherein the plurality of spiral-shaped channels (14) in each concentric cavity extend parallel to one another to define a single spiral shape.

3. 3. The separation apparatus (1) according to claim 2, wherein the lower section of the separation apparatus is located below the at least three concentric enclosures and comprises a solids collection chamber (20) including the turning chamber, and the solids outlet (22) is located at the bottom of the solids collection chamber.

4. A separation device (1) as described in any one of claims 1 to 3, wherein the top of the outermost cavity is open to define an outermost top opening, and the fluid inlet (15) comprises an area formed by the outermost top opening.

5. 5. The separating device (1) of claim 4, further comprising a demarcation structure for separating the outermost top opening from at least one inner top opening.

6. 6. The separation device (1) of claim 5, wherein the boundary definition structure comprises a boundary definition enclosure (31) positioned above and in contact with a second outermost concentric enclosure, and the at least one internal top opening is confined by the boundary definition enclosure and the innermost enclosure (12), thereby forming a liquid collection section (30).

7. The separation device (1) of claim 6, wherein the upper section of the innermost enclosure (12) is provided with at least one collection opening (34) for allowing liquid in the liquid collection section (30) to flow into an internal chamber (35), and further comprises at least one liquid collection tube (36) protruding from the innermost enclosure (12) toward the outside of the separation device to collect liquid in the internal chamber (35).

8. 8. The separation device (1) according to claim 6 or 7, wherein the liquid collection section (30) comprises at least one dividing element (32) dividing the liquid collection section into at least two compartments (33), and the innermost enclosure (12) comprises at least one collection opening (34) for each of the at least two compartments (33).

9. 9. The separating device (1) according to claim 8, comprising a compartment control mechanism for closing said at least one collection opening (34) to prevent liquid from exiting the corresponding compartment (33).

10. The separation device (1) according to any one of claims 1 to 9, wherein the plurality of spiral-shaped channels (14) are defined by a spiral-shaped wall (19) having, with respect to a vertical cross-section, an inner section (17) and an outer section (18), the spiral-shaped wall curving upwards from the inner section towards the outer section, thereby forming an arched or concave shape, or curving downwards from the inner section towards the outer section, thereby forming an arched or convex shape.

11. 11. The separation device (1) according to claim 10, wherein the spiral-shaped walls (19) of the outermost cavity (11) are curved downward from the inner section (17) towards the outer section (18) and the spiral-shaped walls (19) of at least one inner cavity (13) are curved upward from the inner section (17) towards the outer section (18).

12. A separating device (1) according to any one of the preceding claims, wherein the distance (B) between each concentric enclosure and the next is between 50 mm and 800 mm.

13. The separation device (1) according to any one of the preceding claims, wherein the at least three concentric enclosures correspond to at least three concentric tubes having a cylindrical shape and the at least two concentric cavities correspond to at least two concentric rings.

14. A separation device (1) according to claim 3 or any one of claims 4 to 13 when dependent on claim 3, wherein the solids collection chamber (20) has a hollow inverted cone shape.

15. 1. A method for separating a fluid comprising liquids, gases and solids, comprising:

1. A method performed by a separation device (1) comprising at least three concentric enclosures, including an outermost enclosure (10) and an innermost enclosure body (12), defining at least two concentric cavities, and a plurality of helical shaped channels (14) formed in each of the at least two concentric channels, comprising: receiving a fluid through an upper section of an outermost cavity (11) of said at least two concentric cavities; causing the fluid to flow downward through the plurality of helical channels (14) of the outermost cavity (11) and causing gas contained in the fluid to move upward through the plurality of helical channels (14) of the outermost cavity (11) and exit the separation device through an upper section of the outermost cavity (11); when the fluid reaches a redirection chamber located below the outermost cavity (11), it switches from a downward flow through the plurality of spiral-shaped channels (14) of the outermost cavity (11) to an upward flow through the plurality of spiral-shaped channels (14) of at least one inner cavity (13), and when it reaches an upper section of the at least one inner cavity converted into liquid, the liquid flows out of the separation device; allowing solids to move downwardly through the plurality of helical shaped channels (14) of the outermost cavity (11) and the plurality of helical shaped channels (14) of the at least one inner cavity (13) and exit the separation device through a lower section of the separation device; A method comprising:

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