AU746491B2 - Arrangement for combining dissimilar streams - Google Patents

Arrangement for combining dissimilar streams Download PDF

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Publication number
AU746491B2
AU746491B2 AU92112/98A AU9211298A AU746491B2 AU 746491 B2 AU746491 B2 AU 746491B2 AU 92112/98 A AU92112/98 A AU 92112/98A AU 9211298 A AU9211298 A AU 9211298A AU 746491 B2 AU746491 B2 AU 746491B2
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AU
Australia
Prior art keywords
stream
baffle
arrangement
enclosure
air
Prior art date
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Ceased
Application number
AU92112/98A
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AU9211298A (en
Inventor
Peter K. Costello
Ronald F. Gropp
Russell E. Keene
Laurent R. Parent
Margaret E. Solomon
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Kimberly Clark Worldwide Inc
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Kimberly Clark Worldwide Inc
Kimberly Clark Corp
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Publication of AU9211298A publication Critical patent/AU9211298A/en
Application granted granted Critical
Publication of AU746491B2 publication Critical patent/AU746491B2/en
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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B21/00Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/20Jet mixers, i.e. mixers using high-speed fluid streams
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/10Mixing gases with gases
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30Injector mixers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30Injector mixers
    • B01F25/31Injector mixers in conduits or tubes through which the main component flows
    • B01F25/311Injector mixers in conduits or tubes through which the main component flows for mixing more than two components; Devices specially adapted for generating foam
    • B01F25/3111Devices specially adapted for generating foam, e.g. air foam
    • B01F25/31112Devices specially adapted for generating foam, e.g. air foam with additional mixing means other than injector mixers, e.g. screen or baffles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30Injector mixers
    • B01F25/31Injector mixers in conduits or tubes through which the main component flows
    • B01F25/314Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit
    • B01F25/3141Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit with additional mixing means other than injector mixers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40Static mixers
    • B01F25/42Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/43Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
    • B01F25/431Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor
    • B01F25/4315Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor the baffles being deformed flat pieces of material

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Dispersion Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Drying Of Solid Materials (AREA)
  • Treatment Of Fiber Materials (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
  • Toys (AREA)

Description

WO 00/12202 PCT/US98/17967 ARRANGEMENT FOR COMBINING DISSIMILAR STREAMS BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an arrangement and method for combining dissimilar streams and, more particularly, to a baffle configuration for utilization within a duct or similar enclosure to increase the efficiency at which two (or more) dissimilar streams of material (for example, two air streams at different temperatures) may be combined to form a homogeneous stream.
2. Description of the Prior Art In many industrial settings it is often necessary to combine a number of different gaseous (or liquid) materials. For example, it may be necessary to mix combustion, high temperature gases from conventional burners (gas- or oil-fired) with relatively low temperature process air (as may be encountered with air dryers). Alternatively, it may be necessary to mix exhaust gas (high temperature) from the outlet of gas turbines with process air from, for example, air dryers. The structure of these arrangements typically includes a first air stream traveling through a duct (or similar enclosure), with the second stream introduced into the duct via an input port.
In order to effect a combination of such dissimilar streams, prior art arrangements typically relied upon the utilization of a "stirring motion" and turbulence downstream from the injection point of the second air stream. In -1general, such an arrangement requires a significant amount of energy (thus reducing the flow rate of the combined stream), as well as requiring a relatively long distance to ultimately combine the two streams and create a stream of homogenous properties. In an alternative prior art arrangement, deflector vanes are inserted downstream of the injection jet to induce counter rotational flows in the ducting.
Thus, a need remains in the prior art for an improved arrangement for facilitating the combination of dissimilar streams, wherein the arrangement is both energy efficient and utilizes a minimum length of additional ducting.
I0 OBJECT OF THE INVENTION It is an object of the present invention to overcome or ameliorate some of the disadvantages of the prior art, or at least to provide a useful alternative.
SUMMARY OF THE INVENTION go .o.
o• The present invention at least in a preferred embodiment relates to an arrangement and method for combining dissimilar streams and, more particularly, to a baffle configuration for utilization within a duct of similar enclosure to increase the efficiency at which two (or more) dissimilar streams of material (for i h eexample, two air streams at different temperatures) may be combined to form a homogeneous stream.
In a preferred embodiment of the invention, a tapered baffle is disposed see: within a duct upstream of an input source for a second air stream, the second air stream to be combined with a first air stream travelling through the duct. The duct is configured to comprise parallel and spaced-apart walls forming the floor and ceiling of the duct. The input port for the second stream is inserted through the floor of the duct and the baffle is tapered in a manner such that the widest part of the baffle is nearest the input port, narrowing across the width of the duct as it approaches the ceiling of the duct. A first air stream low temperature) is travelling through the duct and a second air stream high temperature) is introduced via the input port. The flow of the first stream across the baffle results in creating a low pressure area along the face of the baffle nearest the input port.
[R:\LIBD]02684.doc:JMT The second stream, introduced by the input port, then naturally flows into the low pressure area created by the baffle configuration, resulting in efficient mixing with the first stream.
In an alternate preferred embodiment of the present invention, a baffle may be configured to include a gap area across the bottom edge of the baffle, near the floor of the duct. This embodiment is particularly well-suited for arrangements where it is desirous to combine a low temperature air stream with a high temperature air stream. In particular, the gap allows for a stream of the low temperature air to pass underneath the baffle and be pulled into the low pressure region in front of the baffle so as to provide for additional cooling of the baffle structure.
The arrangement and method of at least a preferred embodiment of the present invention may be used to combine any two dissimilar materials, for example, steam and air, low humidity air and high humidity air, nitrogen and oxygen, or even two liquids (such as a clear liquid and an emulsion or suspension).
S" In particular, the ability to combine two dissimilar streams of material (such as low temperature air and high temperature air) is extremely useful in the paper and 2: textile industries. For example, in the fabrication of woven or knitted fabrics, as 20 well as certain non-woven materials, it is necessary to "air dry" the material with a homogeneous air stream (often referred to in the art as "through air drying"). In :Iii accordance with the teachings of at least a preferred embodiment of the present invention, the homogenous air stream is formed by a combination of low temperature air and high temperature air utilizing a baffle interposed between the 25 air streams.
*oo• [R:\LIBD]02684.doc:JMT 4 In yet another preferred embodiment of the present invention, a nontapered baffle may be utilized to provide for the combination of two or more streams of material. In particular, a non-tapered baffle may be used in situations where a first, high velocity stream is to be combined with a second, low velocity stream. In the prior art, if the low velocity stream were to be injected into the path of the high velocity stream, the input port of the low velocity stream could become strained, thus misdirecting the flow of low velocity material across the floor of the duct, resulting in inefficient mixing. In accordance with the teachings of at least a preferred embodiment of the present invention, a baffle configured as a nontapered plate functions to shield the input port from the path of the high velocity stream. Thus, the low velocity material is able to extend across the width of the duct, resulting in more efficient mixing downstream.
In a further preferred embodiment of the present invention, a plurality of dissimilar streams may be combined to form one, homogenous stream by utilizing .a plurality of separate baffles, each baffle being disposed upstream of one of a S•:plurality of input ports. The plurality of input ports may be disposed in any desired location with respect to the enclosure. For example, the ports may be positioned along the length of the enclosure or alternatively may be positioned.
[R:\LIBD]02684.doc:JMT WO 00/12202 PCT/US98/17967 across the width of the enclosure. Additionally, the baffle may comprise a solid piece of material or, alternatively, may include one or more perforations.
These and other embodiments of the present invention will become apparent during the course of the following discussion and by reference to the accompanying drawings.
BRIEF DESCRIPTION OF THE DRAWINGS Referring now to the drawings, where like numerals represent like parts in several views: Figure 1 illustrates a view in perspective of an exemplary embodiment of the mixing arrangement of the present invention; Figure 2 contains a view of the arrangement of Figure 1, taken along line 2-2; Figure 3 contains an alternative view of the arrangement of Figure 1, taken along line 3-3; Figure 4 illustrates an alternative embodiment of the present invention, including a gapped baffle; Figure 5 is a view of the arrangement of Figure 4 taken along line Figure 6 is an alternative view of the arrangement of Figure 4, taken along line 6-6; Figure 7 is a view of the arrangement of Figure 5, taken along line 7-7, illustrating in particular the gap area included within the exemplary baffle structure; WO 00/12202 PCT/US98/17967 Figure 8 illustrates, in a perspective view, an alternative arrangement of the present invention utilizing a plurality of baffles and associated input ports; Figure 9 contains a side view of the arrangement of Figure 8, taken along line 9-9 of Figure 8; and Figure 10 is a graph illustrating the results achieved utilizing the arrangement of the present invention as compared with a prior art arrangement, in particular, the improvement in temperature "mixing" achieved when combining low temperature air with high temperature air.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Figure 1 illustrates an exemplary mixing arrangement 10 of the present invention. As shown, the arrangement comprises a tapered baffle 12 disposed in a duct 14 such that widest edge 16 of baffle 12 is in proximity with bottom wall 18 of duct 14. Baffle 12 then tapers into a point 20 in the proximity of top wall 22 of duct 14. It is to be understood that while duct 14 of this embodiment is illustrated as comprising a rectangular cross-section, any suitable enclosure of any predetermined geometry may be utilized. Additionally, the geometry of baffle 12 may differ in particular circumstances. For the arrangement of Figure 1, baffle 12 is illustrated as comprising a conic section.
Other tapered or non-tapered configurations may be utilized and fall within the spirit and scope of the present invention.
Input port 24 protrudes through bottom wall 18 of duct 14 and is located downstream (with respect to the direction of the flow through duct 14) of baffle 12. The distance d between the center of input port 24 and baffle 12 (shown in -6- WO 00/12202 PCT/US98/17967 Figure is a matter of design, and provides either greater or lesser air pressure in the area therebetween, as a function of separation d.
In the embodiment as illustrated a first gas stream G 1 is traveling along the length of duct 14. Gas stream G 1 may comprise oxygen, nitrogen, stream, air, or any other gaseous stream. A second gas stream G 2 travels through tubing 26 and is introduced into duct 14 via input port 24. In accordance with the teachings of the present invention, the flow of first gas stream G 1 past tapered baffle 12 creates a cavity of low pressure on the downstream side 28 of baffle 12. The path of second gas stream G 2 as shown in Figure 1, thus enters the low pressure area. The natural tendency of the jet of injected gas to broaden with increasing distance from the injection point thus causes increasing amounts of second gas stream G 2 to flow outside the low pressure cavity and be swept into the flow of first gas stream G 1 and thereby be evenly distributed across the face (width) of first gas stream G 1 The turbulence created by the tapered baffle structure thus contributes to spreading the mixing action across the front of the flow of first gas stream G 1 It is to be understood that the mixing of the present invention achieved by the utilization of the tapered baffle can be further enhanced by any of the following attributes: modifying the cross section area of duct 12 so as to control the velocity of gas stream G, decreasing the cross section of duct 14 in the region of baffle 12 and input port 24 will increase the velocity of gas stream modifying the aspect ratio of duct 14 (thus controlling the width and breadth of the front of the flow of gas stream Gl); or modifying the -7- WO 00/12202 PCT/US98/17967 velocity at which second gas stream G 2 exits input port 24.
Figure 2 illustrates a side view of the arrangement described above in Figure 1. As shown in this view, input port 24 protrudes a predetermined height h through bottom surface 18 of duct 14. The center of input port 24 is illustrated as being disposed a predetermined distance d downstream from the back edge 30 of baffle 12. Both the height h and the distance d can be controlled so as to provide the most efficient mixing of the two streams, wherein these parameters will be function of the various conditions associated with the two streams temperature, composition, humidity, flow rate, etc.).
As clearly seen in this view, baffle 12 is sized such that top point 20 does not come into contact with top surface 22 of duct 14. The flow of gas stream G, around baffle 12 thus produces low pressure cavity area 32. Gas stream G 2 as it exits input port 24 thus naturally tends to enter cavity 32 and results in increased efficiency in the mixing of gas streams G 1 and G 2 As mentioned above, another factor that effects the efficiency of the arrangement of the present invention is the geometry of the baffle. Figure 3 illustrates a top view in perspective of the mixing arrangement of Figure 1. As shown, sidewall 34 of baffle 12 is formed to comprise an arc of radius r, where this angular displacement has been found to control the overall dimensions of low pressure cavity 32, as well as the actual pressure within the cavity area.
One particular environment for the utilization of the method of the present invention, as mentioned above, is the "through air" drying process associated with the fabrication of woven and non-woven fabrics, where it is often -8- WO 00/12202 PCT/US98/1 7967 necessary to combine low temperature and high temperature air streams. Figure 4 illustrates a particular embodiment of the present invention that is well-suited to such an environment. This environment is suitable for treating light-weight, soft paper products including those having a basis weight of less than 5 and greater than 200 grams per square meter. In particular, mixing arrangement comprises a baffle 52 disposed in a conduit (or similar enclosure) 54, where baffle 52 is located upstream (with respect to the direction of flow through conduit 54) a predetermined distance d (illustrated in Figure 5) from an input port 56. As shown, a first stream of low temperature air ALOW travels along the length of conduit 54 and impinges upon baffle 52 so as to create a low pressure cavity 56 in the interior region of baffle 52. A second stream of high temperature air AHIGH travels through tubing 58 and enters conduit 54 via input port 56. For this particular low temperature/high temperature embodiment of the present invention, baffle 52 includes a lower gap area formed by displacing the bottom surface 58 of baffle 52 a predetermined gap distance g (illustrated in Figure 5) from lower surface 60 of conduit 54. As also seen in Figure 4, baffle 52 includes a number of perforations 53, where these perforations serve to "cool" baffle 52 by allowing a larger quantity of low temperature air to pass therethrough. It is to be understood that the number and size of the perforations should be limited so as to not disrupt the low pressure region created by the baffle structure. Another feature of this particular embodiment is that input port 56 protrudes into conduit 54 a height h greater than the gap distance g (refer to Figure A particular advantage associated with this -9- WO 00/12202 PCT/US98/17967 arrangement is that the injection point of stream AHIGH will remain above the flow path of ALOW. Therefore, the passage of stream ALOW will not disrupt stream AHIGH, which will enter the low pressure region unimpeded.
Figure 6 illustrates a top view of arrangement 50. As illustrated in this particular embodiment, tapered baffle 52 includes a triangular geometry and comprises a pair of sidewalls 62 and 64 displaced by a predetermined angle 0.
Low temperature air stream ALOW travels past baffle 52 so as to create a low pressure region 66 between input port 56 and baffle 52. Therefore, high temperature air stream AHIGH will naturally enter this low pressure cavity and effectively mix with stream ALOW to form output air stream AMIX Figure 7 contains a perspective view of the arrangement of Figure taken along line 7-7. Evident in this view is the gap area 55 between baffle and lower surface 60 of conduit 54. As shown, only small leg portions 57,59 of baffle 52 are in contact with surface 60 (for stability purposes), allowing for a steady stream of ALOW to pass through gap area 55 and provide cooling to baffle 52.
As mentioned above, the utilization of a baffle arrangement in accordance with the present invention may be particularly advantageous in situations where it is necessary to inject a low velocity stream into the path of a high velocity stream. Figure 8 illustrates one such arrangement of the present invention that is particularly well-suited for this purpose. Additionally, Figure 8 illustrates an arrangement including a pair of baffles and associated input ports since, as discussed earlier, the technique of the present invention may be extended to WO 00/12202 PCT/US98/17967 provide for the combining of any number of dissimilar materials. Indeed, although only two exemplary baffles and associated input ports are illustrated, it is to be understood that any desired number of such baffles and associated input ports may be utilized and fall within the spirit and scope of the present invention. Additionally, in accordance with the teachings of the present invention, the multiple baffle/port arrangements may be disposed in any desired fashion within the enclosure. For example, they may be positioned along the length of the enclosure or, alternatively, across the width of the enclosure, or any suitable combination. In general, their location within the enclosure (as long as the baffle is disposed upstream of its associated input port) is not relevant to the teachings of the present invention.
Referring in particular to Figure 8, arrangement 70 includes a first baffle plate 72 and a second baffle plate 74, each baffle plate being disposed to extend across the width of an enclosure 76. A first stream of high velocity material VH (for example, a clear liquid) is traveling through enclosure 76 such that it first impinges and passes over first baffle plate 72, subsequently striking and passing over second baffle plate 74. A second stream of low velocity material VL U (for example, an emulsifier) is introduced into enclosure 76 via a first input port 78. Similarly, a third stream of low velocity material VL 2 (for example, an emulsifier of a different composition and/or velocity) is introduced into enclosure 76 via a second input port 80. In accordance with the teachings of the present invention, each input port is located a predetermined distance downstream of its associated baffle plate. As with the other embodiments -11 WO 00/12202 PCT/US98/17967 discussed above, arrangement 70 allows for the formation of low pressure areas in the region between each baffle plate and its associated input port. Thus, in this particular embodiment, the low pressure areas allow for low velocity streams VL1 and VL 2 to be injected into a sufficient volume of enclosure 76 so as to result in efficient mixing. Additionally, as shown in Figure 8, any baffle structure of the present invention may be formed as a multiple unit structure, with the capability to add or remove separate units to effect different results.
For example, a second baffle section 82 may be attached to the top portion of first baffle plate 72, where second section 82 would allow for the baffle structure to perform with even higher velocity materials. It is to be understood therefore, that the baffle size and shape may be adjusted, over time, to accommodate for various velocities of materials, where the adjustment may best be accomplished by utilizing a multiple unit baffle structure.
Figure 9 contains a cut-away side view of arrangement 70 of Figure 8, taken along line 9-9. As previously discussed, the utilization of a baffle in situations where a low velocity stream is injected into a high velocity flow is particularly advantageous. In a conventional arrangement without the baffle structure of the present invention, the force of high velocity stream V" would cause first input port 78 to bend, as shown in phantom in Figure 9. The injection path of low velocity material VL is therefore perturbed, further reducing the mixing efficiency of streams VH and VLl. Therefore, utilization of baffle plate 72 in accordance with the teachings of the present invention acts as a physical barrier between the high velocity stream and the input port, allowing the low -12- WO 00/12202 PCT/US98/17967 velocity material to be injected in the desired direction.
A numerical depiction of the effectiveness of the present invention is included in Figure 10. In particular, Figure 10 is a graph illustrating temperature variation, as a function of distance, along a chamber, such as duct 14 or conduit 54, when utilizing the arrangement of the present invention to combine to air streams of different temperatures. For the results as illustrated in Figure 9, a first stream of air having an ambient temperature of 250'F is to be combined with a second stream of air having an ambient temperature of 2440 0 F. The efficiency of the combination of the air streams may be measured by assessing the temperature variation at any point downstream of the point at which the two streams begin to combine. The graph in Figure 10 includes measurements of this temperature variation at three separate locations a first point B at a distance of 575 inches beyond the location of the input port for the high temperature stream, a second point C at a distance of 779 inches beyond the input port, and a third point D, a distance of 983 inches beyond the input port.
The temperature variations associated with a convention, prior art structure are indicated as circles in Figure 9. The improvement in mixing efficiency associated with utilization the baffle arrangement of the present invention is evident from viewing the temperature variations, indicated as triangles, measured at the same three locations B, C and D. In particular, at location B, the temperature variation dropped from 500OF to 60 0 F. At location C the variation was reduced from 320°F to 24 0 F and, lastly, at point D the variation was reduced from 1801F to only 16 0 F. It is to be understood that these data -13- WO 00/12202 PCT/US98/17967 points represent temperature variations (as a function of location across the width of the enclosure at the associated point), not the actual ambient temperature of the mixed air stream.
-14-

Claims (40)

1. An arrangement for combining a first stream of material travelling through-an enclosure with a second stream of material, said second stream of material comprising different characteristics than said first stream, said arrangement comprising: an input port for introducing said second stream into said enclosure wherein said port protrudes a predetermined height into said enclosure; and a baffle disposed within said enclosure and positioned to intersect said first stream at a location upstream of said input port, said baffle being separated from said input port by a predetermined distance, wherein the passage of said first SI stream across said baffle creates a region of low pressure between said baffle and Ssaid input port sufficient to increase the efficiency of the combining of said first and second streams.
2. The arrangement as defined in Claim 1 wherein the baffle comprises a tapered structure configured to include a relatively wide bottom portion and a relatively narrow top portion, said tapered baffle being disposed such that said relatively wide bottom portion is located nearest the input port and the tapered baffle extends across the width of the enclosure.
3. The arrangement as defined in Claim 2 wherein the baffle is tapered such that the relatively narrow top portion of said baffle does not contact the enclosure.
4. The arrangement as defined in Claim 2 wherein the tapered baffle comprises a conic section geometry. The arrangement as defined in Claim 2 wherein the tapered baffle comprises a triangular geometry.
6. The arrangement as defined in Claim 2 wherein the relatively wide bottom portion of the tapered baffle includes a gap area such that a portion of said relatively wide bottom portion is displaced a predetermined gap distance g ee from the surface of the enclosure.
7. The arrangement as defined in claim 6 wherein the input port is .e o• disposed to protrude within the enclosure a predetermined height greater than the gap associated with the tapered baffle. The arrangement as defined in Claim 7 wherein the first stream comprises relatively low temperature air and the second stream comprises relatively high temperature air, the gap in said tapered baffle thereby allowing said relatively low temperature air to pass under said baffle, enter the region of low pressure and reduce the ambient temperature of said baffle. WO 00/12202 PCT/US98/17967
9. The arrangement as defined in Claim 8 wherein the tapered baffle includes one or more perforations so as to provide additional cooling to said tapered baffle. The arrangement as defined in Claim 1 wherein the first stream comprises a first gaseous material and the second stream comprises a second gaseous material.
11. The arrangement of Claim 10 wherein the first gas is nitrogen and the second gas is oxygen.
12. The arrangement of Claim 1 wherein the first material is a first liquid and the second material is a second liquid.
13. comprises
14. comprises The arrangement of Claim 12 wherein the first liquid stream a clear liquid and the second liquid stream comprises an emulsifier. The arrangement of Claim 12 wherein the first liquid stream a clear liquid and the second liquid stream comprises a suspension. The arrangement as defined in Claim 1 wherein the baffle includes one or more perforations.
16. The arrangement as defined in claim 1 wherein the baffle includes a gap area such that an edge of said baffle nearest the input port is displaced a predetermined gap distance from the surface of the enclosure.
17. The arrangement as defined in claim 16 wherein the input port is disposed to protrude within the enclosure a predetermined height greater than the gap associated with the displacement of the edge of the baffle.
18. The arrangement as defined in Claim 1 wherein the first stream S..comprises a high velocity stream and the second stream comprises a low velocity stream.
19. The arrangement as defined in Claim 18 wherein the baffle comprises a non-tapered plate geometry. The arrangement as defined in Claim 1 wherein the baffle comprises a non-tapered plate geometry.
21. The arrangement as defined in Claim 1 wherein the baffle comprises a unitary piecepart.
22. The arrangement as defined in Claim 1 wherein the baffle comprises multiple pieceparts such that separate sections may be added or removed as desired.
23. The arrangement as -defined: in Claim 20 wherein the baffle comprises a lower plate section and an upper plate section removably attached to said lower plate section.
24. An arrangement for combining a first stream of, material traveling through an enclosure with a plurality of dissimilar streams of material, each .stream of said plurality of dissimilar streams comprising different characteristics than said first stream, said arrangement comprising: a plurality of input ports disposed to protrude into the enclosure,- each input port for introducing a separate one of the plurality of dissimilar streams; and a plurality of baffles, said plurality of baffles being associated in a one-to- one relationship with said plurality of input ports, each baffle being disposed S* .upstream from its associated input port and separated therefrom by a o* predetermined distance wherein the passage of said first stream across each baffle of said plurality of baffles creates a region of low pressure between each baffle and its associated input port sufficient to increase the efficiency of the combining of said first stream and said plurality of dissimilar streams. I WO 00/12202 PCT/US98/1 7967 The arrangement as defined in Claim 24 wherein at least one baffle of the plurality of baffles comprises a tapered structure configured to include a relatively wide bottom portion and a relatively narrow top portion, said at least one tapered baffle being disposed such that said relatively wide bottom portion is located nearest the associated at least one input port and said at least one tapered baffle extends across the width of the enclosure.
26. The arrangement as defined in Claim 25 wherein the at least one baffle is tapered such that the relatively narrow top portion does not contact the enclosure.
27. The arrangement as defined in Claim 24 wherein the plurality of input ports are disposed along the length of the enclosure.
28. The arrangement as defined in Claim 24 wherein the plurality of input ports are disposed across the width of the enclosure. d A
29. An-arrangement for mixing a first stream of relatively low tempera- ture air traveling through a duct with a second stream of relatively high temperature air, the arrangement comprising: an input port disposed to protrude into the duct, said input port for introducing the second stream into said duct; and a tapered baffle disposed in said duct to intercept the flow of said first stream, wherein said tapered baffle is located a predetermined distance upstream from said input port, said tapered baffle comprising a relatively wide bottom surface and sidewalls narrowing along their length to form a tapered top region, said baffle being disposed such that the wide bottom surface is in proximity with the portion of said duct through-which said input port protrudes, said tapered baffle then extending across the width of said duct. a a. i* 9** WO 00/12202 PCT/US98/1 7967 A method of combining a first stream of material with a second stream of material, said second stream of material comprising different characteristics than said first stream, said method comprising the steps of: a) introducing the first stream into an enclosure such that said first stream travels along the length of the enclosure; b) interrupting the flow of Said first stream using a baffle disposed within the enclosure; and c) introducing the second stream into said enclosure, said second stream being introduced at a location downstream of said baffle, the interruption of the flow of said first stream across said baffle creating a region of low pressure between said baffle and the introduction of said second stream sufficient to increase the efficiency of the combining of said first and second streams.
31. The method according to Claim 30 wherein the first stream comprises relatively low temperature air and the second stream comprises relatively high temperature air.
32. The method according to Claim 30 wherein the first stream comprises a first gaseous material and the second stream comprises a second gaseous material. T' WO 00/12202 PCT/US98/17967
33. The method according to Claim 32 wherein the first gas is nitrogen and the second gas is oxygen.
34. The method according to Claim 30 wherein the first material is a first liquid and the second material is a second liquid. The method according to Claim 30 wherein the first stream comprises a high velocity stream and the second stream comprises a low velocity stream. WO 00/12202 PCT/US98/17967
36. A method of combining a plurality of streams of dissimilar materials, said method comprising the steps of: a) introducing a first stream into an enclosure such that said first stream travels along the length of the enclosure; b) interrupting the flow of said first stream using a baffle disposed within the enclosure; and c) introducing a second stream into said enclosure, said second stream being introduced at a location downstream of said baffle, the interruption of the flow of said first stream across said baffle creating a region of low pressure between said baffle and the introduction of said second stream sufficient to increase the efficiency of the combining of said first and second streams; and d) repeating steps b) and c) for each stream remaining in the plurality of dissimilar streams until all streams have been combined. WO 00/12202 PCT/US98/17967
37. In the fabrication of woven material, a method of drying the woven material by subjecting said woven material to a stream of essentially tempera- ture invariant air comprising the steps of: a) inserting the woven material into a suitable drying apparatus; and b) applying a stream of essentially temperature invariant air to the surface of said woven material, the stream of essentially temperature invariant air formed by c) introducing a first stream of air at a first temperature into an enclosure such that said first stream travels along the length of the enclosure; d) interrupting the flow of said first stream using a baffle disposed within the enclosure; and e) introducing a second stream of air at a second temperature different than said first temperature into said enclosure, said second stream being introduced at a location downstream of said baffle, the interruption of the flow of said first stream across said baffle creating a region of low pressure between said baffle and the introduction of said second stream sufficient to increase the efficiency of the combining of said first and second streams and provide as an output the essentially temperature invariant air stream used to dry said woven material.
38. The method as defined in Claim 37 wherein the first air stream comprises a relatively low temperature and the second air stream comprises a relatively high temperature.
39. The method as defined in claim 38 wherein the first temperature is approximately 2500 F (12 1T) and the second temperature is approximately 2440OF (1338 0 C). see:. 669e 90966 .26 WO 00/12202 PCT/US98/17967 In the fabrication of knitted material, a method of drying the knitted material by subjecting said knitted material to a stream of essentially tempera- ture invariant air comprising the steps of: a) inserting the knitted material into a suitable drying apparatus; and b) applying a stream of essentially temperature invariant air to the surface of said knitted material, the stream of essentially temperature invariant air formed by c) introducing a first stream of air at a first temperature into an enclosure such that said first stream travels along the length of the enclosure; d) interrupting the flow of said first stream using a baffle disposed within the enclosure; and e) introducing a second stream of air at a second temperature different than said first temperature into said enclosure, said second stream being introduced at a location downstream of said baffle, the interruption of the flow of said first stream across said baffle creating a region of low pressure between said baffle and the introduction of said second stream sufficient to increase the efficiency of the combining of said first and second streams to provide as an output the essentially temperature invariant air stream applied to dry said knitted material.
41. The method as defined in Claim 40 wherein the first air stream comprises a relatively low temperature and the second air stream comprises a relatively high temperature.
42. The method as defined in claim 41 wherein the first temperature is approximately 250T (12 IT) and the second temperature is approximately 2440OF (13 3 0 06 06: 04 0009 0006 0 see* WO 00/12202 PCT[US98/17967
43. In the fabrication of non-woven material, a method of drying the non- woven material by subjecting said non-woven material to a stream of essentially temperature invariant air comprising the steps of: a) inserting non-woven material having a basis weight either one of less than 5 grams per square meter and greater than 200 grams per square meter into a suitable drying apparatus; and b) applying a stream of essentially temperature invariant air to the surface of said non-woven material, the stream of essentially temperature invariant air formed by c) introducing a first stream of air at a first temperature into an enclosure such that said first stream travels along the length of the enclosure; d) interrupting the flow of said first stream using a baffle disposed within the enclosure; and e) introducing a second stream of air at a second temperature different than said first temperature into said enclosure, said second stream being introduced at a location downstream of said baffle, the interruption of the flow of said first stream across said baffle creating a region of low pressure between said baffle and the introduction of said second stream sufficient to increase the efficiency of the combining of said first and second streams and provide as an output the essentially temperature invariant air stream applied to dry said non- woven material.
44. The method as defined in Claim 43 wherein the first air stream comprises a relatively low temperature and the second air stream comprises a relatively high temperature. The method as defined in claim 44 wherein the first temperature is approximately 250°F (121°C) and the second temperature is approximately 2440°F (1338 0 C).
46. An arrangement for combining a first stream of material travelling through an enclosure with a second stream of material, said arrangement substantially as herein described with reference to any one of the embodiments of 0*Soo the invention shown in the accompanying drawings. *o i 47. An arrangement for combining a first stream of material travelling through an enclosure with a plurality of dissimilar streams of material, said arrangement substantially as herein described with reference to any one of the embodiments of the invention shown in the accompanying drawings.
48. An arrangement for mixing a first stream of relatively low temperature air travelling through a duct with a second stream of relatively high temperature air, said arrangement substantially as herein described with reference to any one of the embodiments of the invention shown in the accompanying drawings.
49. A method of combining a first stream of material with a second stream of material, said method substantially as herein described with reference to any one of the embodiments of the invention shown in the accompanying drawings. A method of combining a plurality of streams of dissimilar materials, said method substantially as herein described with reference to any one of the embodiments of the invention shown in the accompanying drawings.
51. In the fabrication of woven material, a method of drying the woven material by subjecting said woven material to a stream of essentially temperature invariant air, said method substantially as herein described with reference to any one of the embodiments of the invention shown in the accompanying drawings. o.
52. In the fabrication of knitted material, a method of drying the knitted material by subjecting said knitted material to a stream of essentially temperature i invariant air, said method substantially as herein described with reference to any one of the embodiments of the invention shown in the accompanying drawings. Dated 31 January 2002 Kimberly-Clark Worldwide, Inc Patent Attorneys for the Applicant/Nominated Person SPRUSON FERGUSON 7
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Families Citing this family (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE602005021003D1 (en) 2004-02-27 2010-06-17 Haldor Topsoe As Device for mixing fluid streams
DE102006004069A1 (en) 2006-01-28 2007-09-06 Fisia Babcock Environment Gmbh Method and device for mixing a fluid with a large gas flow rate
JP4961847B2 (en) * 2006-06-12 2012-06-27 いすゞ自動車株式会社 Exhaust gas purification method and exhaust gas purification system
DE102007035226A1 (en) * 2007-07-25 2009-01-29 J. Eberspächer GmbH & Co. KG Flow guiding device and thus equipped exhaust system
EP2185274A4 (en) 2007-09-07 2012-12-05 Turbulent Energy Inc Dynamic mixing of fluids
US9708185B2 (en) 2007-09-07 2017-07-18 Turbulent Energy, Llc Device for producing a gaseous fuel composite and system of production thereof
US8715378B2 (en) 2008-09-05 2014-05-06 Turbulent Energy, Llc Fluid composite, device for producing thereof and system of use
US9310076B2 (en) 2007-09-07 2016-04-12 Turbulent Energy Llc Emulsion, apparatus, system and method for dynamic preparation
US9144774B2 (en) 2009-09-22 2015-09-29 Turbulent Energy, Llc Fluid mixer with internal vortex
US8871090B2 (en) 2007-09-25 2014-10-28 Turbulent Energy, Llc Foaming of liquids
US8844495B2 (en) 2009-08-21 2014-09-30 Tubulent Energy, LLC Engine with integrated mixing technology
FR2952311A1 (en) * 2009-11-09 2011-05-13 Renault Sa Device for mixing intake air flow with recirculated exhaust gas flow in internal combustion engine of e.g. diesel type motor vehicle, has mixing plate integrated to air duct and comprising downstream edge located upstream of axis of pipe
US8317390B2 (en) * 2010-02-03 2012-11-27 Babcock & Wilcox Power Generation Group, Inc. Stepped down gas mixing device
WO2012050858A1 (en) 2010-09-28 2012-04-19 Dow Global Technologies Llc Reactive flow static mixer with cross-flow obstructions
DE102011077645A1 (en) 2011-06-16 2012-12-20 Bosch Emission Systems Gmbh & Co. Kg Static mixer
EP2570179A1 (en) * 2011-09-16 2013-03-20 Air Liquide Deutschland GmbH Method and apparatus for dynamic gas mixture production
JP6296884B2 (en) * 2014-04-30 2018-03-20 三菱日立パワーシステムズ株式会社 Flue gas desulfurization equipment
GB2533331A (en) * 2014-12-16 2016-06-22 Daimler Ag Mixing device for an exhaust gas system
JP6377575B2 (en) * 2015-05-21 2018-08-22 住友金属鉱山株式会社 Fluid blowing apparatus and chemical reaction apparatus using the same
JP6690485B2 (en) * 2016-09-20 2020-04-28 住友金属鉱山株式会社 Chemical reactor and method for producing particles using the chemical reactor
CN108479325A (en) * 2018-05-16 2018-09-04 山东志伟环保科技有限公司 A kind of mixing arrangement of oxidation and denitration

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4498786A (en) * 1980-11-15 1985-02-12 Balcke-Durr Aktiengesellschaft Apparatus for mixing at least two individual streams having different thermodynamic functions of state
US5433596A (en) * 1993-04-08 1995-07-18 Abb Management Ag Premixing burner
US5813850A (en) * 1995-10-11 1998-09-29 Lee; Kyoung-Sik Kerosene combustion apparatus

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5233822B2 (en) * 1972-03-18 1977-08-31
US5159958A (en) * 1991-07-18 1992-11-03 Hydro Systems Company Chemical eductor with integral elongated air gap
US5409514A (en) * 1991-09-03 1995-04-25 Ragusa; Guiseppe Air filter
DE4412261C2 (en) * 1994-04-09 1996-10-17 Jonas Konrad H Device for merging at least two flow media

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4498786A (en) * 1980-11-15 1985-02-12 Balcke-Durr Aktiengesellschaft Apparatus for mixing at least two individual streams having different thermodynamic functions of state
US5433596A (en) * 1993-04-08 1995-07-18 Abb Management Ag Premixing burner
US5813850A (en) * 1995-10-11 1998-09-29 Lee; Kyoung-Sik Kerosene combustion apparatus

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