US3782694A - Apparatus and method for mixing materials - Google Patents

Apparatus and method for mixing materials Download PDF

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US3782694A
US3782694A US00289821A US3782694DA US3782694A US 3782694 A US3782694 A US 3782694A US 00289821 A US00289821 A US 00289821A US 3782694D A US3782694D A US 3782694DA US 3782694 A US3782694 A US 3782694A
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streams
segment
stream
tubular member
minor
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C Shano
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WESTERN CONTROLS Inc
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    • 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
    • B01F25/421Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions by moving the components in a convoluted or labyrinthine path
    • B01F25/422Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions by moving the components in a convoluted or labyrinthine path between stacked plates, e.g. grooved or perforated plates

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  • ABSTRACT A method and apparatus is disclosed wherein a material or fluid stream is directed along a longitudinal axis of an elongated segmented tubular member.
  • the stream is divided into halves, and each half is directed against a transverse wall of one of the segments wherein the half streams are again divided into quarter streams while simultaneously directed transversely of the tubular member.
  • the quarter streams are directed through passageways in the segment and are subsequently recombined with each quarter stream being combined with a quarter stream from a different half stream. Simultaneous with the recombination, the newly formed half streams are again directed longitudinally of the tubular member.
  • the present invention relates to mixing apparatus and methods, and particularly to a method and apparatus for receiving fluid streams, each of a different material, and recombining the streams into a single homogeneous stream.
  • FIG. 1 is a perspective view of apparatus constructed in accordance with the teachings of the present invention for mixing two fluids.
  • FIG. 2 is a cross-sectional view of a portion of FIG. 1, taken along line 22.
  • FIG. 3 is a cross-sectional view of FIG. 2, taken along line 3-3.
  • FIG. 4 is a cross-sectional view of a portion of FIG. 3, taken along line 44.
  • FIG. 5 is a plan view of a modified segment for use in the method and apparatus of the present invention.
  • FIG. 6 is a cross-sectional view of FIG. 5, taken along line 6-6.
  • FIG. 7 is.a schematic view of the apparatus of the present invention, showing the application of the invention to the mixing of three fluids.
  • FIG. 8 is a schematic diagram useful for describing the mixing operation of the apparatus of the present invention.
  • conduits l0 and 11 are each connected to a different source (not shown) of fluid, said fluids to be mixed.
  • the conduits 10 and 11 are connected in any conventional means, such as a Y coupling 12, thus superficially combining the two fluids in conduit 14.
  • Conduit 14 is connected to the apparatus of the present invention 15 which is shown in cross section in FIG. 2.
  • the fluids, superficially mixed in the conduit 14, enter the mixing apparatus 15 longitudinally thereof.
  • the mixing apparatus incorporates a cylindrical housing 20 which is internally threaded at either end to receive end fittings 22 and 24 which, in turn, are connected to an input conduit 14 and an output conduit 26 respectively.
  • the housing 20 in the embodiment chosen for illustration, is cylindrical but it will be obvious to those skilled in the art that a rectangular or other cross section may be used, although with somewhat less efficiency.
  • the housing supports a plurality of segments 30, each segment being identical with the others.
  • the segments are interfitted with each succeeding segment so as to form a fluid-tight segmented cylinder through which the fluids pass, as will be described more fully hereinafter.
  • the interfitted segments 30 may be spaced from the ends of the housing 20 by suitable spacers 31 and 32.
  • Each of the segments may conveniently be molded of plastic, or, in the event the apparatus is used in a heat exchanging environment, may be of an appropriately formed metal or other high heat conductivity metal.
  • the segment 30 shown therein may be seen to include a transverse wall 35 which, if not provided with openings therethrough, would interrupt the flow of fluid through the segment.
  • the transverse wall 35 is provided with two openings 37 and 38 positioned diametric with respect to each other.
  • a dividing partition 40 extends upwardly from the transverse wall 35; the dividing partition 40 forms passageways 42, 43, 44, and 45, each of said passageways extending transversely to the longitudinal axis of the housing 20.
  • Each segment 30 is provided with a detent 47 and an extension 48 (see FIG.
  • each segment while identical to all other segments, is rotated with respect to the succeeding segment since the extension 48 is positioned 90 about the axis of the housing 20 from the detent in that segment. Therefore, as the segments are stacked, the extensions 48 prevent the segments from nesting unless they are rotated 90 with respect to each other.
  • the segments are formed so as to stack and snap together to fonn a self-sealing structure that may be used without the housing 20, although the housing 20 adds structural strength to the assembly.
  • the openings 37 and 38 in the transverse wall 35 are oriented with the passageways 50, 51, 52, and 53 of the next succeeding segment.
  • the next preceding segment would have its openings oriented with the passageways 42, 43, 44, and 45.
  • fluid exiting from the preceding segment into the segment shown in FIG. 3 would be in the form of two streams flowing longitudinally of the housing 20, the first of which would flow directly into the segment 30 and be divided by the partition 40 into two streams, one flowing in the passageway 42 and the other flowing in the passageway 43; the second of the streams entering the segment 30 would be divided by the partition 40 into two streams, one flowing in the passageway 44 and the other flowing in the passageway 45.
  • That portion of the fluid flowing in channels 42 and 44 is recombined at the opening 37, while the fluid flowing in channels 43 and 45 is recombined at the opening 38.
  • the fluid stream entering the housing 20 is therefore first divided into halves, each half flowing through an opening such as that at 37 and 38 on to the second segment.
  • the flow up to this point has been essentially longitudinal but upon passing through the openings 37 and 38 is simultaneously divided by the partition 40 and is directed transversely of the housing 20.
  • Each half stream is accordingly divided into quarter streams, each quarter stream following one of the passageways 42, 43, 44 and 45.
  • the quarter streams travel their respective passageways and reach an opening 37 or 38, the quarter streams are recombined into half streams; however, each quarter stream is combined with a quarter stream of a different half stream.
  • the-newly formed half streams again flow longitudinally of the housing 20 to the next segment 30.
  • the superficially mixed fluid entering the mixing apparatus 15 from the conduit 14 is first divided into two half streams; each half stream is divided into quarter streams while simultaneously with such division the direction of the quarter streams is changed from longitudinal to transverse.
  • Each quarter stream travels a transverse path to be recombined with a different quarter stream while the direction is simultaneously changed from transverse to longitudinal.
  • the change in direction of the fluid as it passes through the respective segments forces the fluid against the transverse walls of the segments as the fluids changes direction from longitudinal to transverse.
  • This direction change not only enhances the mixing of the fluids but in those instances where the apparatus is used in a heat transferring environment, the direction change and large fluid surface contact area effectively reduces boundary layer insulation to greatly enhance the heat transfer capacity of the apparatus. Further, flow direction can be reversed with equal effectiveness.
  • a transverse wall 60 forces fluid streams impinging thereagainst to change from a longitudinal to a transverse direction of flow.
  • Passageways 61, 62, 63, and 64 receive fluid streams from the preceding segment and direct the streams, after being divided by partition 66, to openings 67 and 69.
  • the openings 67 and 69 register with the beginnings of the passageways of the next succeeding segment in a manner described in the preceding embodiment.
  • the successive segments of the embodiment shown in FIGS. 5 and 6 are also rotated 90 with respect to each other through the utilizatof the segment shown in FIG. 3 and that only the spe ciflc shape has been changed.
  • a schematic mixer is shown connected to receive three fluid streams A, B, and C, said streams having been superficially mixed by combination with the input conduit 81.
  • the fluid stream containing the three separate fluids may be mixed to any desired degree by simply adding additional segments to the mixing apparatus. If only one segment is used, the stream is divided into two streams which may then be recombined; however, if two. segments are used, the two streams exiting from the first segment are again divided, thus effectively producing four streams. Similarly, successive segments each effectively double the number of streams that are produced during the mixing of the fluids as it passes through the mixing apparatus.
  • the degree of mixing desired may be determined in accordance with numerous factors, but the apparatus of the present invention will divide and recombine for every segment that is added to the stack of segments. Thus, the precise number of segments required to provide the desired degree of mixing may be determined, thereby permitting unneeded segments to be removed to minimize the fluid pressure required to force the fluid through the mixing apparatus.
  • Mixing apparatus for transmitting and mixing fluids comprising:
  • an elongated segmented tubular member having a longitudinal axis, for connection to a source of fluids to be mixed, said fluids entering and exiting said tubular member parallel to said longitudinal axis;
  • each segment of said tubular member including:

Abstract

A method and apparatus is disclosed wherein a material or fluid stream is directed along a longitudinal axis of an elongated segmented tubular member. The stream is divided into halves, and each half is directed against a transverse wall of one of the segments wherein the half streams are again divided into quarter streams while simultaneously directed transversely of the tubular member. The quarter streams are directed through passageways in the segment and are subsequently recombined with each quarter stream being combined with a quarter stream from a different half stream. Simultaneous with the recombination, the newly formed half streams are again directed longitudinally of the tubular member.

Description

United States Patent [191 Shano [4 1 Jan. 1,1974
[ APPARATUS AND METHOD FOR MIXING MATERIALS [75] Inventor: Charles L. Shano, Phoenix, Ariz.
[73] Assignee: Western Controls Inc., Pheonix,
Ariz.
22 Filed: Sept. 18, 1972 [21] Appl. No.: 289,821
3,701,619 10/1972 Appeldoorn 259/4 Primary ExaminerRobert W. Jenkins Att0rneyWilliam C. Cahill et a1.
[5 7] ABSTRACT A method and apparatus is disclosed wherein a material or fluid stream is directed along a longitudinal axis of an elongated segmented tubular member. The stream is divided into halves, and each half is directed against a transverse wall of one of the segments wherein the half streams are again divided into quarter streams while simultaneously directed transversely of the tubular member. The quarter streams are directed through passageways in the segment and are subsequently recombined with each quarter stream being combined with a quarter stream from a different half stream. Simultaneous with the recombination, the newly formed half streams are again directed longitudinally of the tubular member.
6 Claims, 8 Drawing Figures PATENTEU JAN 1 7 SHEUINZ APPARATUS AND METHOD FOR MIXING I MATERIALS The present invention relates to mixing apparatus and methods, and particularly to a method and apparatus for receiving fluid streams, each of a different material, and recombining the streams into a single homogeneous stream.
It is frequently important to insure the homogeneity of a fluid and to mix different fluids to form the homogeneous fluid immediately prior to its utilization. The mixing of such fluids has previously required the use of relatively complex apparatus if complete homogeneity is to be insured; further, the complexity of such apparatus indicates a relatively high cost. Typically, fluids to be recombined are transmitted to a mixing device and, after mixing, are transported to the point of utilization through a cylindrical conduit. The mixing apparatus therefore usually may conveniently take the form of a cylindrical member connected in series with the exit conduit. The material being mixed or the fluids passing through the mixer may require the addition of heat or the mixing process may be exothermic, requiring the removal of heat in the mixer. The surface area of contact between the fluid passing through the mixer is an important function of the ability of the apparatus to conduct heat either from or to the fluid passing therethrough.
It is therefore an object of the present invention to provide a mixing apparatus for receiving a plurality of fluids to be mixed and for mixing the fluids to provide a single homogeneous fluid.
It is another object of the present invention to provide a mixing apparatus that is inexpensive to manufacture while providing an efficient structure to insure thorough mixing of the fluids.
It is still another object of the present invention to provide a mixing apparatus that can readily be disassembled for cleaning and replacing worn parts.
It is still another object of the present invention to provide apparatus for conducting fluids therethrough incorporating a large surface area in contact with the fluid to promote efficient heat transfer.
It is also an object of the present invention to provide a method for mixing fluid streams to provide a single homogeneous fluid stream.
It is a further object of the present invention to provide a method for mixing fluid streams wherein the fluid is divided into smaller streams while the direction of fluid flow is changed from longitudinal to transverse.
These and other objects of the present invention will become apparent to those skilled in the art as the description thereof proceeds.
The present invention may be described by reference to the accompanying drawings, in which:
FIG. 1 is a perspective view of apparatus constructed in accordance with the teachings of the present invention for mixing two fluids.
FIG. 2 is a cross-sectional view of a portion of FIG. 1, taken along line 22.
FIG. 3 is a cross-sectional view of FIG. 2, taken along line 3-3.
FIG. 4 is a cross-sectional view of a portion of FIG. 3, taken along line 44.
FIG. 5 is a plan view of a modified segment for use in the method and apparatus of the present invention.
FIG. 6 is a cross-sectional view of FIG. 5, taken along line 6-6.
FIG. 7 is.a schematic view of the apparatus of the present invention, showing the application of the invention to the mixing of three fluids.
FIG. 8 is a schematic diagram useful for describing the mixing operation of the apparatus of the present invention.
Referring now to FIGS. 1-4, conduits l0 and 11 are each connected to a different source (not shown) of fluid, said fluids to be mixed. The conduits 10 and 11 are connected in any conventional means, such as a Y coupling 12, thus superficially combining the two fluids in conduit 14. Conduit 14 is connected to the apparatus of the present invention 15 which is shown in cross section in FIG. 2. The fluids, superficially mixed in the conduit 14, enter the mixing apparatus 15 longitudinally thereof. The mixing apparatus incorporates a cylindrical housing 20 which is internally threaded at either end to receive end fittings 22 and 24 which, in turn, are connected to an input conduit 14 and an output conduit 26 respectively. The housing 20, in the embodiment chosen for illustration, is cylindrical but it will be obvious to those skilled in the art that a rectangular or other cross section may be used, although with somewhat less efficiency. The housing supports a plurality of segments 30, each segment being identical with the others. The segments are interfitted with each succeeding segment so as to form a fluid-tight segmented cylinder through which the fluids pass, as will be described more fully hereinafter. The interfitted segments 30 may be spaced from the ends of the housing 20 by suitable spacers 31 and 32.
Each of the segments may conveniently be molded of plastic, or, in the event the apparatus is used in a heat exchanging environment, may be of an appropriately formed metal or other high heat conductivity metal.
Referring specifically to FIG. 3, the segment 30 shown therein may be seen to include a transverse wall 35 which, if not provided with openings therethrough, would interrupt the flow of fluid through the segment. However, the transverse wall 35 is provided with two openings 37 and 38 positioned diametric with respect to each other. A dividing partition 40 extends upwardly from the transverse wall 35; the dividing partition 40 forms passageways 42, 43, 44, and 45, each of said passageways extending transversely to the longitudinal axis of the housing 20. Each segment 30 is provided with a detent 47 and an extension 48 (see FIG. 4) wherein each segment, while identical to all other segments, is rotated with respect to the succeeding segment since the extension 48 is positioned 90 about the axis of the housing 20 from the detent in that segment. Therefore, as the segments are stacked, the extensions 48 prevent the segments from nesting unless they are rotated 90 with respect to each other. The segments are formed so as to stack and snap together to fonn a self-sealing structure that may be used without the housing 20, although the housing 20 adds structural strength to the assembly.
With the 90 orientation of the succeeding segments, it may be seen that the openings 37 and 38 in the transverse wall 35 are oriented with the passageways 50, 51, 52, and 53 of the next succeeding segment. Similarly, the next preceding segment would have its openings oriented with the passageways 42, 43, 44, and 45. In this manner, fluid exiting from the preceding segment into the segment shown in FIG. 3 would be in the form of two streams flowing longitudinally of the housing 20, the first of which would flow directly into the segment 30 and be divided by the partition 40 into two streams, one flowing in the passageway 42 and the other flowing in the passageway 43; the second of the streams entering the segment 30 would be divided by the partition 40 into two streams, one flowing in the passageway 44 and the other flowing in the passageway 45. That portion of the fluid flowing in channels 42 and 44 is recombined at the opening 37, while the fluid flowing in channels 43 and 45 is recombined at the opening 38. The fluid stream entering the housing 20 is therefore first divided into halves, each half flowing through an opening such as that at 37 and 38 on to the second segment. The flow up to this point has been essentially longitudinal but upon passing through the openings 37 and 38 is simultaneously divided by the partition 40 and is directed transversely of the housing 20. Each half stream is accordingly divided into quarter streams, each quarter stream following one of the passageways 42, 43, 44 and 45. When the quarter streams travel their respective passageways and reach an opening 37 or 38, the quarter streams are recombined into half streams; however, each quarter stream is combined with a quarter stream of a different half stream. Simultaneously with the recombination of the quarter streams, the-newly formed half streams again flow longitudinally of the housing 20 to the next segment 30. In this manner, the superficially mixed fluid entering the mixing apparatus 15 from the conduit 14 is first divided into two half streams; each half stream is divided into quarter streams while simultaneously with such division the direction of the quarter streams is changed from longitudinal to transverse. Each quarter stream travels a transverse path to be recombined with a different quarter stream while the direction is simultaneously changed from transverse to longitudinal. The change in direction of the fluid as it passes through the respective segments forces the fluid against the transverse walls of the segments as the fluids changes direction from longitudinal to transverse. This direction change not only enhances the mixing of the fluids but in those instances where the apparatus is used in a heat transferring environment, the direction change and large fluid surface contact area effectively reduces boundary layer insulation to greatly enhance the heat transfer capacity of the apparatus. Further, flow direction can be reversed with equal effectiveness.
Referring now to FIGS. 5 and 6, a modified segment form is shown. A transverse wall 60 forces fluid streams impinging thereagainst to change from a longitudinal to a transverse direction of flow. Passageways 61, 62, 63, and 64 receive fluid streams from the preceding segment and direct the streams, after being divided by partition 66, to openings 67 and 69. The openings 67 and 69 register with the beginnings of the passageways of the next succeeding segment in a manner described in the preceding embodiment. The successive segments of the embodiment shown in FIGS. 5 and 6 are also rotated 90 with respect to each other through the utilizaof the segment shown in FIG. 3 and that only the spe ciflc shape has been changed.
Referring now to FIGS. 7 and 8, a schematic mixer is shown connected to receive three fluid streams A, B, and C, said streams having been superficially mixed by combination with the input conduit 81. Referring to FIG. 8, it may be seen that the fluid stream containing the three separate fluids (A B C) may be mixed to any desired degree by simply adding additional segments to the mixing apparatus. If only one segment is used, the stream is divided into two streams which may then be recombined; however, if two. segments are used, the two streams exiting from the first segment are again divided, thus effectively producing four streams. Similarly, successive segments each effectively double the number of streams that are produced during the mixing of the fluids as it passes through the mixing apparatus. The degree of mixing desired may be determined in accordance with numerous factors, but the apparatus of the present invention will divide and recombine for every segment that is added to the stack of segments. Thus, the precise number of segments required to provide the desired degree of mixing may be determined, thereby permitting unneeded segments to be removed to minimize the fluid pressure required to force the fluid through the mixing apparatus.
I claim:
1. Mixing apparatus for transmitting and mixing fluids comprising:
a. an elongated segmented tubular member, having a longitudinal axis, for connection to a source of fluids to be mixed, said fluids entering and exiting said tubular member parallel to said longitudinal axis;
b. means within said tubular member for dividing a fluid stream entering said tubular member into a plurality of minor streams;
c. each segment of said tubular member including:
1. a transverse wall for intercepting each of said minor streams and directing said minor streams transversely of said tubular member,
2. a dividing partition extending from said transverse wall for dividing each of said minor streams into portions thereof,
3. a plurality of segment exits,
4. a plurality of transversely extending passageways for directing the portions of each minor stream to a different one of said segment exits to be combined at said exits with the portions of a dif ferent one of said minor streams;
d. said fluids directed longitudinally from the exits of each segment to the succeeding segment.
2. The combination set forth in claim 1, wherein said elongated segmented tubular member is cylindrical.
3. The combination set forth in claim 1, wherein said means for dividing a fluid stream into a plurality of minor streams comprises the first segment of said tubular member to be encountered by said fluid stream entering said tubular member. I
4. The combination set forth in claim 1, wherein said segments are identical and are nested with respect to each other and are rotated with respect to the preceding and succeeding segments.
5. The combination set forth in claim 1, wherein said segments are interfitted with each preceding segment a. combining said different fluid streams to form a d. combining each quarter stream of one half stream gl fluid f f flowing along a gi axis; with a quarter stream of another half stream while b. dividing said single fluid stream into two half Simultaneously changing the direction of flow to streams flowing longitudinally along said axis;
0. dividing each of said half streams into quarter 5 streams while simultaneously changing the direction of said quarter streams to transverse of said Streamaxis;
parallel to said axis to form new half streams; and e. combining said new half streams to form a single

Claims (9)

1. Mixing apparatus for transmitting and mixing fluids comprising: a. an elongated segmented tubular member, having a longitudinal axis, for connection to a source of fluids to be mixed, said fluids entering and exiting said tubular member parallel to said longitudinal axis; b. means within said tubular member for dividing a fluid stream entering said tubular member into a plurality of minor streams; c. each segment of said tubular member including: 1. a transverse wall for intercepting each of said minor streams and directing said minor streams transversely of said tubular member, 2. a dividing partition extending from said transverse wall for dividing each of said minor streams into portions thereof, 3. a plurality of segment exits, 4. a plurality of transversely extending passageways for directing the portions of each minor stream to a different one of said segment exits to be combined at said exits with the portions of a different one of said minor streams; d. said fluids directed longitudinally from the exits of each segment to the succeeding segment.
2. The combination set forth in claim 1, wherein said elongated segmented tubular member is cylindrical.
2. a dividing partition extending from said transverse wall for dividing each of said minor streams into portions thereof,
3. a plurality of segment exits,
3. The combination set forth in claim 1, wherein said means for dividing a fluid stream into a plurality of minor streams comprises the first segment of said tubular member to be encountered by said fluid stream entering said tubular member.
4. The combination set forth in claim 1, wherein said segments are identical and are nested with respect to each other and are rotated 90* with respect to the preceding and succeeding segments.
4. a plurality of transversely extending passageways for directing the portions of each minor stream to a different one of said segment exits to be combined at said exits with the portions of a different one of said minor streams; d. said fluids directed longitudinally from the exits of each segment to the succeeding segment.
5. The combination set forth in claim 1, wherein said segments are interfitted with each preceding segment to provide a seal therebetween and to form said tubular member.
6. A method for mixing different fluid streams to form a single homogeneous fluid stream, comprising the steps of: a. combining said different fluid streams to form a single fluid stream flowing along a given axis; b. dividing said single fluid stream into two half streams flowing longitudinally along said axis; c. dividing each of said half streams into quarter streams while simultaneously changing the direction of said quarter streams to transverse of said axis; d. combining each quarter stream of one half stream with a quarter stream of another half stream while simultaneously changing the direction of flow to parallel to said axis to form new half streams; and e. combining said new half streams to form a single stream.
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US3856270A (en) * 1973-10-09 1974-12-24 Fmc Corp Static fluid mixing apparatus
FR2485391A1 (en) * 1980-06-27 1981-12-31 Fiat Ricerche STATIC MIXER FOR LIQUID AND SEMI-LIQUID MATERIALS
US4352572A (en) * 1980-01-09 1982-10-05 Hwang-Chuan Chen Continuous and automatic oil-water mixing method and its installation
US4522504A (en) * 1983-12-08 1985-06-11 Pyles Division Linear in-line mixing system
US5255974A (en) * 1990-09-19 1993-10-26 Sulzer Brothers Limited Static mixer
US5327941A (en) * 1992-06-16 1994-07-12 The United States Of America As Represented By The Secretary Of The Navy Cascade orificial resistive device
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US20040135017A1 (en) * 2001-05-07 2004-07-15 Sukeyoshi Sekine Mixing, crushing, and pulverizing device, and method of pulverizing substances using the device
US20050215954A1 (en) * 2004-03-29 2005-09-29 Mallinckrodt Inc. Apparatus and method for maintaining suspendible agents in suspension
US20060165488A1 (en) * 2005-01-27 2006-07-27 Keith Morris Hand held tamping device
US20070140042A1 (en) * 2004-06-04 2007-06-21 Gerhard Schanz Multicomponent packaging with static micromixer
US20080031081A1 (en) * 2006-07-28 2008-02-07 Rigo S.R.L. Mixing device for delivering a resin or other products mixed with a foaming gas
US20080106968A1 (en) * 2003-07-25 2008-05-08 Wella Ag Components for Static Micromixers, Micromixers Constructed from such Components and Use of such Micromixers for Mixing or Dispersing or for Carrying Out Chemical Reactions
US20080277009A1 (en) * 2007-05-10 2008-11-13 Fluid-Quip, Inc. Multiple helical vortex baffle
US20180266578A1 (en) * 2017-03-14 2018-09-20 Jesse Baxter Tank overhead line liquid backflow restriction device

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Cited By (23)

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US3856270A (en) * 1973-10-09 1974-12-24 Fmc Corp Static fluid mixing apparatus
US4352572A (en) * 1980-01-09 1982-10-05 Hwang-Chuan Chen Continuous and automatic oil-water mixing method and its installation
FR2485391A1 (en) * 1980-06-27 1981-12-31 Fiat Ricerche STATIC MIXER FOR LIQUID AND SEMI-LIQUID MATERIALS
US4522504A (en) * 1983-12-08 1985-06-11 Pyles Division Linear in-line mixing system
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US5255974A (en) * 1990-09-19 1993-10-26 Sulzer Brothers Limited Static mixer
US5327941A (en) * 1992-06-16 1994-07-12 The United States Of America As Represented By The Secretary Of The Navy Cascade orificial resistive device
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US20040135017A1 (en) * 2001-05-07 2004-07-15 Sukeyoshi Sekine Mixing, crushing, and pulverizing device, and method of pulverizing substances using the device
US20080067271A1 (en) * 2001-05-07 2008-03-20 Sukeyoshi Sekine Apparatus for mixing and/or crushing substances into fine particles and method of crushing substances into fine particles using such apparatus
US20080106968A1 (en) * 2003-07-25 2008-05-08 Wella Ag Components for Static Micromixers, Micromixers Constructed from such Components and Use of such Micromixers for Mixing or Dispersing or for Carrying Out Chemical Reactions
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US20070140042A1 (en) * 2004-06-04 2007-06-21 Gerhard Schanz Multicomponent packaging with static micromixer
US20060165488A1 (en) * 2005-01-27 2006-07-27 Keith Morris Hand held tamping device
US20080031081A1 (en) * 2006-07-28 2008-02-07 Rigo S.R.L. Mixing device for delivering a resin or other products mixed with a foaming gas
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US8696192B2 (en) * 2007-05-10 2014-04-15 Fluid-Quip, Inc. Multiple helical vortex baffle
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