FEED SPACER FOR REDUCING DIFFERENTIAL PRESSURE OF REVERSE OSMOSIS ELEMENT, AND FORMATION NOZZLE

Abstract

Provided is a feed spacer for reducing differential pressure of a reverse osmosis element, the feed spacer forming the reverse osmosis element, the feed spacer comprising a plurality of strands disposed in a mesh shape having predetermined intersection points, and wherein a vertical cross section of each of the strands has a rhombic shape such that a pressure loss of in the feed spacer is minimized by an effective flow of raw water at an interface of a reverse osmosis membrane, and a nozzle for forming the feed spacer.

Claims

1. A feed spacer for reducing differential pressure in a reverse osmosis element, comprising a plurality of strands disposed in a mesh shape having predetermined intersection points, wherein a vertical cross section of each of the strands has a rhombic shape.

2. The feed spacer of claim 1, wherein the strands form a mesh having a two-layer structure, wherein a first set of strands form a first layer, and a second set of strands are disposed on the first layer forming a second layer.

3. The feed spacer of claim 1, wherein an angle at one side of the intersection point of the strands is 80° or smaller.

4. The feed spacer of claim 1, wherein lengths between the intersection points of the strands all are equal to one another, and a thickness of the feed spacer is constant.

5. The feed spacer of claim 4, wherein a differential pressure in the reverse osmosis element decreases as a ratio of the length between the intersection points of the strands to the thickness of the feed spacer increases.

6. A nozzle for forming a feed spacer for reducing differential pressure in a reverse osmosis element, wherein the nozzle forms the feed spacer of claim 1.

7. The nozzle of claim 6, wherein the nozzle has a dual structure comprising an outer nozzle and an inner nozzle.

8. The nozzle of claim 6, wherein the nozzle has one or more rhombic slots.

9. The nozzle of claim 8, wherein a length between the slots is adjustable.

10. The nozzle of claim 8, wherein a size of the slot is adjustable.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0021] FIG. 1 is a perspective view of a strand according to an exemplary embodiment of the present invention.

[0022] FIG. 2 is a perspective view of a feed spacer for reducing differential pressure in a reverse osmosis element according to the exemplary embodiment of the present invention.

[0023] FIG. 3 is a cross-sectional view of a nozzle 100 for forming a feed spacer for reducing differential pressure in a reverse osmosis element according to the exemplary embodiment of the present invention.

DETAILED DESCRIPTION

[0024] Hereinafter, the present invention will be described in detail with reference to the accompanying drawings. Here, repeated descriptions and detailed descriptions of publicly-known functions and configurations, which can unnecessarily obscure the subject matter of the present invention, will be omitted. Exemplary embodiments of the present invention are provided to completely explain the present invention to a person with ordinary skill in the art. Therefore, shapes and sizes of elements illustrated in the drawings can be exaggerated for a more apparent description.

[0025] Throughout the specification, unless explicitly described to the contrary, the word “comprise” or “include” and variations, such as “comprises”, “comprising”, “includes” or “including”, will be understood to imply the inclusion of stated constituent elements, not the exclusion of any other constituent elements.

[0026] Hereinafter, exemplary embodiments are proposed to help understand the present invention. However, the following exemplary embodiments are provided just for more easily understanding the present invention, and the contents of the present invention are not limited by the exemplary embodiments.

[0027] FIG. 1 is a perspective view of a strand according to an exemplary embodiment of the present invention, and FIG. 2 is a perspective view of a feed spacer for reducing differential pressure in a reverse osmosis element according to the exemplary embodiment of the present invention.

[0028] A reverse osmosis element can be configured by stacking a plurality of reverse osmosis membranes, a plurality of feed spacers, and a plurality of transmissive spacers and can surround a water collecting pipe. The feed spacer is positioned between the reverse osmosis membranes and maintains a constant interval between the reverse osmosis membranes. The feed spacer can serve to block a surface of the reverse osmosis membrane in order to filter out contaminants contained in raw water introduced through the reverse osmosis membrane. Therefore, in order to enable contaminants contained in the raw water to flow without being collected, the feed spacer can have a mesh shape made by a plurality of strands arranged to have predetermined intersection points. In this case, a material of the strand can be any one of, but not particularly limited to, polyethylene (PE), polyvinyl chloride (PVC), polyester, polypropylene (PP), and a mixture of two or more polymers. In addition, the strand can have a vertical cross section having a rhombic shape. The rhombic shape can have a smaller area than a circular or quadrangular shape when the thickness remains the same. Therefore, a flow path in the feed spacer including the strands each having the vertical cross section having the rhombic shape can be increased, such that flow resistance against the reverse osmosis element can be reduced, thereby reducing differential pressure.

[0029] The mesh shape of the feed spacer according to the present invention can have a two-layer structure. First, some strands are disposed in parallel at predetermined intervals in a direction inclined with respect to a flow direction of raw water. Thereafter, the remaining strands are disposed in parallel at predetermined intervals on the previous strands in a reversely inclined direction symmetrical to the inclined direction in order to form the intersection points. The mesh shape can be a parallelogrammatic shape having identical sides based on positions of the disposed strands. In this case, an angle θ of the parallelogram with respect to the flow direction of the raw water is 80° or less. The flow of raw water is not separated from the strands well. The flow of raw water is separated after the raw water flows along the strands for a comparatively long period of time, and then the flow of raw water spreads. When flow diffusion of the raw water is large, the raw water is uniformly supplied to the interface of the reverse osmosis membrane, and the flows of the raw water are mixed, such that the ion polarization can be reduced, and the flow resistance of the raw water can be reduced, thereby reducing the differential pressure in the reverse osmosis element. When the angle θ of the parallelogram exceeds 80°, the flow of raw water is easily separated from the strands, and the flow of raw water is hardly spread.

[0030] Meanwhile, since the feed spacer has the mesh shape with the parallelogrammatic shape having the identical sides, lengths l and g of the portions of the strands between the intersection points p are equal to one another. A thickness of a layer of the strand has a constant value of h/2, and a thickness of the feed spacer, which is made by positioning the strands in two layers, has a constant value of h. The length l or g between the intersection points p between the strands can be, but is not particularly limited to, 2 to 5 mm. If the length l or g is smaller than 2 mm, the ion polarization is inhibited, but a pressure loss is increased in the feed spacer. In contrast, if the length l or g is larger than 5 mm, a pressure loss is decreased in the feed spacer, but the ion polarization occurs, which can result in a deterioration in performance of the reverse osmosis element. The thickness h of the feed spacer can be, but not particularly limited to, 0.5 to 2.0 mm. If the thickness h is smaller than 0.5 mm, the flow path can be clogged with foreign substances contained in the raw water or power required for a pump for pumping the raw water can be increased. In contrast, if the thickness h is larger than 2.0 mm, an area of the reverse osmosis membrane of the reverse osmosis element is decreased, which can result in a decrease in performance of the reverse osmosis membrane. As described above, the differential pressure in the feed spacer can be reduced since a pressure loss is decreased as a value of a ratio (l/h) of the length I or g between the intersection points p between the strands to the thickness h of the feed spacer is increased within the range of the length l or g between the intersection points p between the strands and the range of the thickness h of the feed spacer.

[0031] FIG. 3 is a cross-sectional view of a nozzle 100 for forming a feed spacer for reducing differential pressure in a reverse osmosis element according to the exemplary embodiment of the present invention.

[0032] The nozzle 100 for forming a feed spacer for reducing differential pressure in a reverse osmosis element can include an outer nozzle 10, an inner nozzle 20, and slots 30.

[0033] The nozzle 100 for forming a feed spacer for reducing differential pressure in a reverse osmosis element according to the present invention can form the feed spacer for reducing differential pressure in a reverse osmosis element according to the present invention by discharging any one of polyethylene (PE), polyvinyl chloride (PVC), polyester, polypropylene (PP), and a mixture of two or more polymers which are used as the material of the strand.

[0034] The nozzle 100 for forming a feed spacer for reducing differential pressure in a reverse osmosis element can have a dual structure including the outer nozzle 10 and the inner nozzle 20. The plurality of slots 30 is positioned at a portion where the outer nozzle 10 and the inner nozzle 20 are in contact with each other, and each of the plurality of slots 30 is used to form a cross section of the strand. When the outer nozzle 10 and the inner nozzle 20 engage with each other and rotate, distances between the plurality of slots 30 can be adjusted, and thus the length l or g between the intersection points p between the strands can also be adjusted. Further, the slot 30 can be designed to have a rhombic shape, thereby forming the strand. An area of the strand to be formed also varies depending on a size of the slot 30, and the thickness h of the feed spacer can increase as the size of the slot 30 increases.

Comparative Example 1

[0035] Differential pressure was measured in a feed spacer which was made by a nozzle of a type having a quadrangular shape and had a mesh in which an angle θ of a parallelogram was 90° with respect to a flow direction of raw water.

Comparative Example 2

[0036] Differential pressure was measured in a feed spacer which was made by a nozzle of a type having a circular shape and had a mesh in which an angle θ of a parallelogram was 90° with respect to a flow direction of raw water.

Comparative Example 3

[0037] Differential pressure was measured in a feed spacer which was made by a nozzle of a type having a quadrangular shape and had a mesh in which an angle θ of a parallelogram was 75° with respect to a flow direction of raw water.

Comparative Example 4

[0038] Differential pressure was measured in a feed spacer which was made by a nozzle of a type having a quadrangular shape and had a mesh in which an angle θ of a parallelogram was 75° with respect to a flow direction of raw water.

Example 1

[0039] Differential pressure was measured in a feed spacer which was made by a nozzle of a type having a rhombic shape and had a mesh in which an angle θ of a parallelogram was 75° with respect to a flow direction of raw water.

Example 2

[0040] Differential pressure was measured in a feed spacer which was made by a nozzle of a type having a rhombic shape and had a mesh in which an angle θ of a parallelogram was 80° with respect to a flow direction of raw water.

TABLE-US-00001 TABLE 1 Θ L = g Differential Nozzle (°) (mm) l/h Pressure (psi) Type Comparative 90 2.90 3.37 3.94 Quadrangle Example 1 Comparative 90 3.70 4.30 2.33 Circle Example 2 Comparative 75 2.92 3.40 2.96 Quadrangle Example 3 Comparative 75 3.52 4.09 2.79 Quadrangle Example 4 Example 1 75 4.63 5.38 1.83 Rhombus Example 2 80 3.80 4.49 2.03 Rhombus

[0041] In order to measure a change in differential pressure in the feed spacer, the elements including the Comparative Examples and the Examples were used. In this case, the element is a standard element with a diameter of 8 inches, and an effective membrane area is 37 m.sup.2. Further, the raw water containing NaCl of 2,000 ppm flows at a raw water pressure of 225 psi to the element, and the differential pressure is a value measured when an average flow rate (an arithmetic mean of a flow rate of raw water and a flow rate of permeable water) is 44 GPM.

[0042] The vertical cross sections of the strands formed by the types of nozzles according to the Examples and the Comparative Examples are equal to the shapes of the types of nozzles. Therefore, referring to Table 1, the strands according to Comparative Examples 1 to 4 had the vertical cross sections having the quadrangular shape and the circular shape in the related art, and in Examples 1 and 2, the strands having the vertical cross sections having the rhombic shapes according to the present invention were used.

[0043] First, when comparing Comparative Examples 1 and 3, the nozzle types have the same quadrangular shape, and the angle θ of the parallelogram of the mesh with respect to the flow direction of the raw water is 90° in Comparative Example 1 and 75° in Comparative Example 3. In this case, the differential pressure was 3.94 psi in Comparative Example 1 and 2.96 psi in Comparative Example 3. Therefore, it can be ascertained that the differential pressure in the feed spacer is reduced when the angle θ is 80° or smaller.

[0044] When comparing Comparative Example 3 and Example 1, the angles θ of the parallelogram with respect to the flow direction of the raw water are the same as each other and are 75°. In Comparative Example 3, the ratio (l/h) of the length l between the intersection points between the strands to the thickness of the feed spacer is 3.40 when the length l is 2.92 mm. In Example 1, the ratio (l/h) of the length l between the intersection points between the strands to the thickness of the feed spacer is 5.38 when the length l is 4.63 mm. In this case, the differential pressure was 2.96 psi in Comparative Example 3 and 1.83 psi in Example 1. Therefore, it can be ascertained that the differential pressure of the feed spacer decreases when the ratio (l/h) of the length l between the intersection points between the strands to the thickness of the feed spacer increases.

[0045] When comparing Comparative Example 4 and Example 2, Comparative Example 4 and Example 2 have similar ratios (l/h) of the length l between the intersection points between the strands to the thickness of the feed spacer, and the vertical cross section of the strand is a quadrangular shape in Comparative Example 4 and a rhombic shape in Example 2. In addition, the angle θ of the parallelogram in Comparative Example 4 is 75°, and the angle θ of the parallelogram in Example 2 is 80° which is a value increased from the angle in Comparative Example 4. In this case, the differential pressure was 2.79 psi in Comparative Example 4 and 2.03 psi in Example 2. Therefore, it can be ascertained that when the vertical cross section of the strand has a rhombic shape, the differential pressure in the feed spacer is decreased even though the angle θ of the parallelogram of the mesh with respect to the flow direction of the raw water is increased.

[0046] That is, it can be ascertained that the use of the design of the strand having the rhombic shape according to the present invention reduces the differential pressure in the feed spacer. In addition, it can be ascertained that the differential pressure in the feed spacer is decreased when the angle θ between the intersection points between the strands is 80° or smaller and the ratio (l/h) of the length I between the intersection points between the strands to the thickness of the strand is increased.

[0047] While the present invention has been described above with reference to the exemplary embodiments, it can be understood by those skilled in the art that the present invention can be variously modified and changed without departing from the spirit and scope of the present invention disclosed in the claims.