FRACTAL FLOW DEVICES AND METHODS OF USE
20170354903 · 2017-12-14
Assignee
Inventors
Cpc classification
C02F1/006
CHEMISTRY; METALLURGY
G01N30/468
PHYSICS
B01D15/22
PERFORMING OPERATIONS; TRANSPORTING
B01D15/1842
PERFORMING OPERATIONS; TRANSPORTING
International classification
Abstract
A fractal flow device comprising at least one fractal pack. The at least one fractal pack comprises at least two fractal cells, where each fractal cell comprises a fractal distributor, a chamber adjacent the fractal distributor, and a fractal collector adjacent the chamber. Methods of using the fractal flow device are also disclosed.
Claims
1. A fractal flow device, comprising: at least one fractal pack, the at least one fractal pack comprising: at least two fractal cells, each fractal cell comprising a fractal distributor, a chamber adjacent the fractal distributor, and a fractal collector adjacent the chamber.
2. The fractal flow device of claim 1, wherein the fractal distributor, the chamber, and the fractal collector are in fluid communication with one another.
3. The fractal flow device of claim 1, wherein each of the fractal distributor and the fractal collector comprises a fractal pattern.
4. The fractal flow device of claim 1, wherein the at least two fractal cells are configured in a horizontal direction.
5. The fractal flow device of claim 4, wherein the at least two fractal cells comprise shoulders configured to position the at least two fractal cells in a horizontal direction.
6. The fractal flow device of claim 1, wherein the at least two fractal cells are configured in a vertical direction.
7. The fractal flow device of claim 1, wherein each of the fractal distributor and the fractal collector comprises at least one fractal plate comprising a fractal pattern.
8. The fractal flow device of claim 7, wherein the fractal patterns of the fractal distributor and the fractal collector are the same.
9. The fractal flow device of claim 7, wherein the fractal patterns of the fractal distributor and the fractal collector are different.
10. The fractal flow device of claim 7, wherein the fractal distributor and the fractal collector comprise the same number of fractal plates.
11. The fractal flow device of claim 7, wherein the at least one fractal plate of the fractal distributor or of the fractal collector comprises at least one fractal plate inlet, at least one fractal plate outlet, and at least one channel in fluid communication with the at least one fractal plate inlet and the at least one fractal plate outlet.
12. The fractal flow device of claim 11, wherein the fractal distributor comprises an outlet density of greater than approximately 64 outlets/ft.sup.2.
13. The fractal flow device of claim 7, wherein the fractal distributor comprises three fractal plates, a first fractal plate comprising one fractal plate inlet and four fractal plate outlets, a second fractal plate comprising four fractal plate inlets and sixteen fractal plate outlets, and a third fractal plate comprising sixteen fractal plate inlets and two hundred fifty six fractal plate outlets.
14. The fractal flow device of claim 7, wherein the fractal collector comprises three fractal plates, a first fractal plate comprising two hundred fifty six fractal plate inlets and sixteen fractal plate outlets, a second fractal plate comprising sixteen fractal plate inlets and four fractal plate outlets, and a third fractal plate comprising four fractal plate inlets and one fractal plate outlet.
15. The fractal flow device of claim 1, wherein the chamber comprises a fluid processing medium.
16. The fractal flow device of claim 15, wherein the fluid processing medium comprises an ion exchange resin.
17. The fractal flow device of claim 1, wherein the at least one fractal pack is configured for series operation, parallel operation, primary/secondary series operation, simulated moving bed operation, or carousel-type fluid operation.
18. The fractal flow device of claim 1, further comprising a fastening element securing the at least two fractal cells of the at least one fractal pack.
19. The fractal flow device of claim 1, wherein the fastening element comprises end plates, a support head, a hydraulic press, a hydraulic jack, or bolts.
20. A method of using a fractal flow device, comprising: introducing a fluid stream to a fractal flow device, the fluid stream comprising multiple components and the fractal flow device comprising at least one fractal pack, the at least one fractal pack comprising: at least two fractal cells, each fractal cell comprising a fractal distributor, a chamber adjacent the fractal distributor, and a fractal collector adjacent the chamber; flowing the fluid stream through the at least one fractal pack; and separating at least one component from the fluid stream to produce a product stream.
21. The method of claim 20, wherein flowing the fluid stream through the at least one fractal pack comprises flowing the fluid stream through the at least two fractal cells in parallel.
22. The method of claim 20, wherein flowing the fluid stream through the at least one fractal pack comprises flowing the fluid stream through at least two fractal packs in series.
23. The method of claim 20, further comprising flowing the fluid stream through a fractal predistributor before flowing the fluid stream through the at least one fractal pack.
24. The method of claim 20, wherein flowing the fluid stream through the at least one fractal pack comprises uniformly distributing the fluid stream through a chamber containing a bed of fluid processing medium.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0010]
[0011]
[0012]
[0013]
[0014]
[0015]
[0016]
DETAILED DESCRIPTION
[0017] A fractal flow device having at least one fractal pack is disclosed. The fractal pack provides increased capacity to the fractal flow device without increasing pressure within the fractal flow device during its use and operation. The increased capacity is achieved without substantially increasing the size or weight of the fractal flow device. The fractal flow device is, thus, compact and there is no increase in volume (i.e., equipment footprint) occupied by the fractal flow device. The fractal flow device may include a single fractal pack or multiple fractal packs that are configured in parallel or in series depending on the desired application of the fractal flow device. The fractal pack includes fractal cells that are configured in parallel or series depending on the desired application of the fractal flow device. The fractal flow device is used to separate a component(s) of a multicomponent fluid stream.
[0018] As used herein, the term “fractal” means and includes a pattern (i.e., shape or geometry) that can be repeatedly divided into small parts or repeatedly multiplied into larger parts that are the same or similar to the original pattern (i.e., shape or geometry). The fractal flow device of the disclosure includes at least one component having a fractal pattern, such as one or more of a fractal plate, a fractal distributor, a fractal collector, a fractal cell, or a fractal pack.
[0019] As shown in
[0020] As shown in
[0021] As shown in
[0022] The fractal distributor 130 includes one or more fractal plates 205. For simplicity, the fractal plates are referred to herein as fractal plate 205 or fractal plates 205, while specific fractal plates are referred to herein as fractal plates 205a, 205b, 205c, etc. As shown in
[0023] The fractal plates 205 of the fractal distributor 130 are aligned with one another so that the fluid stream passes into the fractal plate inlet(s) 335, through the channel(s) 355, and exits the fractal plate outlet(s) 345 of the fractal plate 205 before passing into the fractal plate inlet(s) 335, through the channel(s) 355, and exits the fractal plate outlet(s) 345 of the next fractal plate 205. The fractal distributor 130 may be configured and formed as described in U.S. Pat. No. 6,616,327 to Kearney et al. and U.S. Pat. No. 7,390,408 to Kearney et al. The fractal plates 205 of the fractal distributor 130 may be positioned adjacent to one another such that fractal distribution from large to progressively smaller scales occurs as the fluid stream passes through the fractal distributor 130. By including one or more fractal plates 205 having the same fractal pattern 215, the fractal distributor 130 has a relatively small width (i.e., thickness) relative to its length or height. The height to width ratio of the fractal plates 205 may range from about 2:1 to about 20:1 or greater.
[0024] The fractal distributor 130 may include an outlet density sufficient to provide reduced turbulence or internal mixing of the fluid stream as the fluid stream passes into the chamber 140. The outlet density may be increased as desired by recursively multiplying the fractal pattern 215 on a smaller and smaller scale. As used herein, the term “outlet density” means and includes the number of outlets in the unit cross-sectional area of the fractal plate 205 directly adjacent to the chamber 140. By way of example only, the fractal distributor 130 may have an outlet density of greater than or equal to approximately 64 outlets/ft.sup.2, such as greater than or equal to approximately 100 outlets/ft.sup.2, greater than or equal to approximately 200 outlets/ft.sup.2, greater than or equal to approximately 500 outlets/ft.sup.2, or greater than or equal to approximately 1024 outlets/ft.sup.2. The greater the outlet density of the fractal plate 205 directly adjacent to the chamber 140, the more uniform distribution of the fluid stream into the chamber 140.
[0025] As illustrated in
[0026] The chamber 140 of the fractal cell 120 includes an opening 180 for containing a fluid processing medium (not shown), such as an ion exchange resin or other separation medium, an adsorption medium, an absorption medium, a catalyst medium, or a reactive medium. As shown in
[0027] The fractal collector 150 of the fractal cell 120 also includes one or more fractal plates 205. While the embodiment of the fractal collector 150 in
[0028] In one embodiment, the fractal collector 150 has the same number of fractal plates 205 as the fractal distributor 130. The fractal pattern 215 on the fractal plates 205 of the fractal collector 150 is also substantially similar to the fractal pattern 215 on the fractal plates 205 of the fractal distributor 130. However, the order in which the fractal plates 205 of the fractal collector 150 are configured is reversed such that the fractal plate 205 having the greatest number of fractal plate inlets 335 is directly adjacent to the chamber 140. In other words, the last fractal plate 205 of the fractal collector 150 (i.e., the fractal plate 205g, which is distal to the chamber 140) has the lowest outlet density. The outlet density may be decreased as desired by recursively dividing the fractal pattern 215 on a larger and larger scale. The fractal plates 205 of the fractal collector 150 may be positioned adjacent to one another such that fractal distribution from small to progressively larger scales occurs as the fluid stream passes through the fractal collector 150.
[0029] By way of example only and as shown in
[0030] Shoulders 465 on side surfaces of the fractal plates 205 of the fractal distributor 130, chamber 140, and the fractal plates 205 of the fractal collector 150 may be used to position the fractal cells 120 adjacent to one another, as shown in
[0031] The fractal plates 205 of the fractal distributor 130 and fractal collector 150 may be formed from any compatible material onto which the fractal pattern 215 is to be formed. The material may also be compatible with the components of the fluid stream. For instance, the material, such as a plastic material or a metal material, may be resistant to corrosive, acidic, or basic components in the fluid stream. The plastic material may include, but is not limited to, polypropylene, polymethylmethacrylate (PMMA), polytetrafluoroethylene, and the metal material may include, but is not limited to, stainless steel. Since the fractal flow device 100 may be operated at a lower pressure than conventional equipment, the material of the fractal distributor 130 and the fractal collector 150 may be selected from materials not used in the conventional equipment due to this reduced structural requirement. The chamber 140 may be formed from the same or a similar material. The material of the fractal distributor 130, the chamber 140, and the fractal collector 150 may also be compatible with operating temperatures at which the fractal flow device 100 is utilized, such as from room temperature (from about 20° C. to about 25° C.) to about 85° C. The material of the fractal distributor 130, the chamber 140, and the fractal collector 150 may also be compatible with operating pressures at which the fractal flow device 100 is utilized, such as less than or equal to about 4 bar (less than or equal to about 400 kPa). By way of example only, the fractal distributor 130, chamber 140, and fractal collector 150 may be formed of PMMA.
[0032] The dimensions of the fractal plates 205 of the fractal distributor 130 and fractal collector 150 and of the chamber 140 may be selected depending on the desired capacity of the fractal flow device 100. By way of example only, each of the length and height of the fractal plates 205 and chamber 140 may independently range from approximately 2 inches to approximately 48 inches. The thickness (i.e., width) of the fractal plates 205 may range from approximately 0.1 inch to approximately 3 inches. The thickness (i.e., width) of the chamber 140 may be larger to accommodate the fluid processing medium, such as from approximately 0.2 inch to approximately 6 inches. In one embodiment, the fractal plates 205 are 12.25-inch square and 1 inch thick. The chamber 140 is 12.25-inch square and 2 inches thick.
[0033] The fractal flow device 100 also includes connector elements, such as tubing, piping, openings, etc., that provide fluid communication between the components of the fractal flow device 100. For instance, the fluid stream may pass between the fractal plate inlets 335, channels 355, and fractal plate outlets 345 of the fractal cells 120 and the chamber 140, which are located within (i.e., internally) the fractal cells 120. The fluid stream may pass from the fractal distributor 130, through the chamber 140, and into the fractal collector 150 by tubing or openings within the fractal cells 120. Alternatively, the fluid stream may pass between the components of the fractal cells 120 through externally located tubing (not shown). Thus, the fractal cells 120 of the fractal pack 110 may be in fluid communication through external connector elements or internal connector elements. The fractal flow device 100 also includes connector elements that introduce the fluid stream into the fractal flow device 100 and collect the fluid stream as the fluid stream exits the fractal flow device 100. While not illustrated in the drawings, a simple configuration of connector elements may be used in which tubing is connected to the fractal cell inlets 160 and fractal cell outlets 170 of each of the fractal cells 120 of
[0034] Connector elements that are located external to the fractal pack 110 may also be used in more complex embodiments of the fractal flow device 100. The connector elements may distribute the fluid stream through a single fractal pack 110 (see
[0035] In embodiment of the fractal flow device 100′ illustrated in
[0036] In yet another embodiment and as illustrated in
[0037] In yet another embodiment and as illustrated in
[0038] The fractal flow devices 100, 100′, 100″, 100′″ according to the embodiments hereof may be used to separate or purify a component from a multicomponent fluid stream. For instance, the fractal flow devices 100, 100′, 100″, 100′″ may be used to decolorize or otherwise purify a fluid stream containing multiple components. Alternatively, the fractal flow devices 100, 100′, 100″, 100′″ may be used to demineralize a fluid stream containing multiple components. By way of example only, the fractal flow devices 100, 100′, 100″, 100′″ may be used in the water treatment, food and sweeteners, chemicals, biomass, renewables, pharmaceutical, mining, or petroleum industries.
[0039] During use and operation of the fractal flow devices 100, 100′, 100″, 100′″ according to the embodiments hereof, the fluid stream enters the fractal plates 205 of the fractal distributor 130 of a first fractal cell and is distributed into multiple fluid streams. The fluid streams are uniformly distributed into the fluid processing medium of the chamber 140 of the first fractal cell 120. As the fluid streams flow through the chamber 140, the components in the fluid streams are separated depending on interactions with the fluid processing medium used in the chamber 140. After passing through the chamber 140, the distributed fluid streams flow through the fractal plates 205 of the fractal collector 150 of the first fractal cell 120 and exit the first fractal cell 120 as a single processed fluid stream. The fluid stream is similarly processed in parallel through a second and subsequent fractal cell(s) 120 such that a single processed fluid stream exits each of the second and subsequent fractal cells 120 of the fractal flow devices 100, 100′, 100″, 100′″. The processed fluid stream of each fractal cell 120 is combined into a product stream in which the desired component is separated from other components of the fluid stream.
[0040] By utilizing fractal packs 110 in the fractal flow devices 100, 100′, 100″, 100′″, increased capacity, reduced footprint, reduced pressure increases, and increased flow rates may be achieved. The capacity of the fractal flow devices 100, 100′, 100″, 100′″ according to the embodiments hereof may be tailored as desired by increasing or decreasing the number of fractal cells 120 in each fractal pack 110 and/or by increasing or decreasing the number of fractal packs 110 in the fractal flow devices 100, 100′, 100″, 100′″. Since the fractal packs 110 include multiple fractal cells 120 positioned adjacent to one another, each of which includes the fractal distributor 130, chamber 140, and fractal collector 150, the fractal pack 110 may be easily modified to achieve the desired capacity by including more or fewer fractal cells 120 depending on the intended application. By utilizing such a modular design, the fractal packs 110 provide increased capacity to the fractal flow devices 100, 100′, 100″, 100′″ without having to increase the diameter of the fractal plates 205 or other components of the fractal flow devices 100, 100′, 100″, 100′″. Thus, the necessity of redesigning the fractal flow devices 100, 100′, 100″, 100′″ for every desired change in capacity is avoided and the fractal flow devices 100, 100′, 100″, 100′″ may be easily expanded in an economical fashion.
[0041] The footprint of the fractal flow devices 100, 100′, 100″, 100′″ according to embodiments hereof may also be maintained at substantially the same size because the capacity of the fractal flow devices 100, 100′, 100″, 100′″ can be increased or decreased simply by adding or removing, respectively, fractal packs 110 or fractal cells 120. Thus, increasing the capacity of the fractal flow devices 100, 100′, 100″, 100′″ does not increase the overall size of the fractal flow devices 100, 100′, 100″, 100′″ as is needed with conventional equipment. Since the increased processing capacity is provided by the additional fractal cells 120 and/or fractal packs 110, the same processing area is provided in a volume that occupies a small footprint and the fractal cells 120 and/or fractal packs 110 provide a flexible and efficient use of space. Also, no additional mechanical support for the fractal flow devices 100, 100′, 100″, 100′″ is needed because the size and weight of the fractal plates 205 or other components of the fractal flow devices 100, 100′, 100″, 100′″ are not increased as the desired capacity increases. In contrast, when additional capacity is needed with conventional equipment, the conventional equipment must be redesigned by increasing the diameter of the plates, which increases pressures within the conventional equipment, increases the footprint of the conventional equipment, and increases the size and weight of the conventional equipment.
[0042] By utilizing the fractal packs 110, pressure increases in the fractal flow devices 100, 100′, 100″, 100′″ are also reduced or eliminated because the diameter of the fractal plates 205 or other components of the fractal flow devices 100, 100′, 100″, 100′″ does not need to be correspondingly increased. Increased flow rates of the fluid stream through the fractal pack 110 are also possible relative to the flow rate through conventional equipment due to the large decrease in linear velocity of the fluid stream and large decrease in pressure drop across the chamber 140. In addition, fluid channeling and turbulence, which are common problems with conventional equipment as flow rates increase, are not observed with the fractal flow devices 100, 100′, 100″, 100′″ according to the embodiments hereof.
[0043] After being apprised of the instant disclosure, one of ordinary skill in the art will be readily able to make and use the invention.
[0044] While the disclosure is susceptible to various modifications and alternative forms, specific embodiments have been shown by way of example in the drawings and have been described in detail herein. However, the disclosure is not intended to be limited to the particular forms disclosed. Rather, the disclosure is to cover all modifications, equivalents, and alternatives falling within the scope hereof as defined by the following appended claims and their legal equivalents.