WO2011138162A1 - Mixing process and mixing arrangement - Google Patents
Mixing process and mixing arrangement Download PDFInfo
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- WO2011138162A1 WO2011138162A1 PCT/EP2011/056123 EP2011056123W WO2011138162A1 WO 2011138162 A1 WO2011138162 A1 WO 2011138162A1 EP 2011056123 W EP2011056123 W EP 2011056123W WO 2011138162 A1 WO2011138162 A1 WO 2011138162A1
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- fluid
- main stream
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- channel wall
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/30—Injector mixers
- B01F25/31—Injector mixers in conduits or tubes through which the main component flows
- B01F25/314—Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit
- B01F25/3142—Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit the conduit having a plurality of openings in the axial direction or in the circumferential direction
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/30—Injector mixers
- B01F25/31—Injector mixers in conduits or tubes through which the main component flows
- B01F25/314—Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/30—Injector mixers
- B01F25/31—Injector mixers in conduits or tubes through which the main component flows
- B01F25/314—Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit
- B01F25/3142—Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit the conduit having a plurality of openings in the axial direction or in the circumferential direction
- B01F25/31422—Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit the conduit having a plurality of openings in the axial direction or in the circumferential direction with a plurality of perforations in the axial direction only
Definitions
- the invention relates to a method for mixing a plurality of fluids, of which at least one fluid is at least partially formed by a chemical, into a main flow delimited by a duct wall.
- the invention also relates to a mixing arrangement for mixing at least a first and a second fluid via a respective nozzle with a
- Nozzle opening of which at least the second fluid is at least partially formed by a chemical in a bounded by a channel wall main flow, in particular for carrying out the method.
- the object of the invention is therefore to ensure the widest possible interference of a chemical in a main stream while avoiding deposits.
- the object with regard to the method has been achieved in that a first fluid is at least partially injected in the flow direction of the main flow before a second fluid in the main stream and the point of entry of the second fluid in the main flow is further away from the channel wall than the inlet point of the first fluid in the mainstream.
- the second fluid which is preferably at least partially formed by a chemical, is injected into the main stream at a distance from the channel wall, deposition in the region of this injection and at the channel wall is already counteracted. In addition, this also supports the mixing, as it is shifted away from the edge of the main stream away.
- the mixed flow resulting from the injection of the first fluid into the main flow is deflected in the direction of flow of the main flow and thus flows around at least the nozzle, if possible also the nozzle opening of the second fluid, which likewise impedes deposition.
- the invention offers particular advantages with regard to thorough mixing in a main stream formed by a pulp suspension for producing a paper, board, tissue or other fibrous web.
- the application is also advantageous for main streams, etc. of process, fresh water. be formed.
- the admixed fluids can be formed by chemicals, a pulp suspension or water, and depending on the nature and effect of a chemical, these may also be added in advance to the pulp suspension or the water. If, in addition to the second, further fluids are to be injected and mixed into the main stream, which are at least partially formed by a chemical, it is advantageous if the first fluid is at least partially in
- Flow direction of the main stream is injected before the other fluid in the main stream and the entry point of the other fluid in the main flow is further away from the channel wall than the inlet point of the first fluid in the
- Flow direction of the main flow are arranged side by side. Depending on the degree of mixing desired and Verwirblung the entry points of these fluids in the main flow can be the same or different distances from the channel wall.
- the distance of the nozzle opening of the second and further fluid to the channel wall should be between 5 mm and 10% of the maximum cross-sectional dimension of the main flow.
- the inlet point of the second fluid encloses the inlet point of the further fluid or the nozzle for the further fluid.
- the entry points of the fluid are juxtaposed, and in the other case, the point of entry of the further fluid extends further into the main flow than the entry point of the second fluid.
- the fluids or the nozzle jet emanating from the nozzle should be injected at an angle of between 10 and 170 °, preferably between 70 and 110 ° to the flow direction of the main flow.
- Main current extends.
- the first fluid with the main flow forms a mixed flow, which the nozzle and possibly also the nozzle opening of the second fluid with a directional component in the direction of the injection and in
- This mixed flow prevents deposits on the channel wall and the injection, which could emanate from the second fluid and also protects the chemical during the injection into the main flow.
- the mixing of the second fluid in the main stream is promoted by this mixed stream.
- the nozzle opening of the first fluid should be as close as possible to the channel wall, if possible with this form a plane.
- the nozzles for the second and the further fluid can be guided with advantage through different nozzle openings for different or the same fluid in the main stream.
- the distance between the nozzle openings of the second and further fluid to the channel wall may be the same or different.
- Nozzle openings for the second and the further fluid in the flow direction of the main flow with equal or different distance to the channel wall
- the nozzle for the further fluid extends through the nozzle opening for the second fluid in the main stream, wherein the nozzle openings have the same or a different distance from the channel wall.
- the nozzle openings may have a round or square cross-section. The nozzles can pierce the respective nozzle openings centrally or eccentrically.
- the range of the jets depends in addition to the parameters of the main flow substantially from the fluid pressure at the nozzle opening, the jet area and their change over the length of the jet.
- Nozzle jets inclined to the flow direction of the main stream preferably inclined against this flow direction or perpendicular to the
- the main flow delimited by the channel wall has a round, in particular a circular cross-section.
- angular, in particular rectangular cross sections are appropriate. This is especially true when the
- Main flow leading channel wall is open at the top.
- Figures 1 to 4 show schematic cross sections through various mixing arrangements.
- the mixing arrangements shown here serve for admixing a plurality of fluids 1, 2, 3, 4 to a main fluid flow 6 from a pulp suspension, which is guided in a tubular channel to a headbox of a machine for producing a fibrous web, in particular a paper web, and a consistency between 0.05 and 7.0%, in particular between 0.2 and 2.5%.
- Some fluids 2,3 are hereby at least partially of chemicals, in particular retention agents, such as polyacrylamide, polyvinylamine, polyethylene oxide, fixatives or even of microparticles, such. Bentonite or silicate formed.
- retention agents such as polyacrylamide, polyvinylamine, polyethylene oxide, fixatives or even of microparticles, such. Bentonite or silicate formed.
- the fluids 1, 2, 3, 4 can also be formed, at least in part, by pulp suspension or water (process or fresh water). If the fluids 1, 4 consist entirely of pulp suspension or water, they serve in
- Pulp suspension or water before spraying into the main stream 6 to mix a chemical Pulp suspension or water before spraying into the main stream 6 to mix a chemical. This premixing is sometimes possible if there is no substantial pre-reaction of the chemical or deposits through it
- the main stream 6 passes through one guided by a channel wall 5 channel with circular cross-section.
- a plurality of mixing arrangements for admixing the fluids 1, 2, 3, 4 into the main flow 6 are preferably possible distributed over the circumference of the channel.
- the mixing arrangement shown in Figure 1 is very simple and is essentially formed by two nozzles 1 1, 12 which inject a first fluid 1 and a second fluid 2 transversely to the flow direction 7 of the main stream 6 in this. At least the second fluid 2 consists partly of a chemical.
- the nozzle opening 8 of the nozzle 1 1 for the first fluid 1 is in the plane of the channel wall 5, which should prevent deposits in this inlet region of the fluid 1.
- the nozzle 12 for the second fluid 2 is guided centrally through the nozzle opening 8 of the nozzle 1 1 of the first fluid 1 in the main stream 6.
- the nozzle opening 9 of the nozzle 12 for the second fluid 2 is not only relatively deep in the main stream 6 but also relatively far away from the channel wall 5. This is advantageous because because of the chemicals of the second fluid 2 reinforced with deposits in the
- Entry area is to be expected in the main stream 6, however, by the
- the first fluid 1 when injected into the main flow 6, the first fluid 1 forms a mixed flow with a component in and transverse to the flow direction 7 of the
- Main flow 6 so that the nozzle 12 and the outgoing from her nozzle jet is flowed around with the second fluid 2 of this mixed flow. This also prevents deposits, protects the second fluid 2 when it exits into the main flow 6 and ensures intensive but gentle mixing of the two fluids 1, 2 with the main flow 6.
- Figure 2 shows a mixing arrangement in which the second 2 and another 3 fluid at least partially formed by a chemical and is also injected perpendicular to the flow direction 7 of the main stream 6 in this.
- the nozzles are 12,13 accordingly the principle described for Figure 1 by a respective nozzle opening 8,15 out, which lies in the plane of the channel wall 5.
- the first fluid 1 flows around the second fluid 2 and the fourth fluid 4 flows around the third fluid 3 during the injection.
- the nozzle openings 9, 16 of the two nozzles 12, 13 are located equidistant from the channel wall 5.
- the nozzles 12, 13 for the second 2 and the further fluid 3 with at least one chemical are common
- both nozzles 12,13 and their jets with the two fluids 2,3 are flowed around by the, formed at the entrance of the first fluid 1 in the main stream 6 mixed flow.
- a nozzle 13 extends further into the main stream 6 than the other nozzle 12, which provide additional turbulence and the
- the mixing arrangement according to FIG. 4 mixes three fluids 1, 2, 3 perpendicular to
- the fluids 1, 2, 3, 4 should be injected at a pressure in the latter which is between 1, 5 and 10 bar above the pressure in the main stream 6.
- the invention enables efficient mixing and mixing of multiple chemicals even with a large chemical-to-mainstream ratio.
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- Chemical Kinetics & Catalysis (AREA)
- Accessories For Mixers (AREA)
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Abstract
Description
MISCHVERFAHREN UND MISCHANORDNUNG MIXING METHOD AND MIXING ARRANGEMENT
Die Erfindung betrifft ein Verfahren zur Einmischung von mehreren Fluiden, von denen zumindest ein Fluid wenigstens teilweise von einer Chemikalie gebildet wird, in einen von einer Kanalwand begrenzten Hauptstrom. The invention relates to a method for mixing a plurality of fluids, of which at least one fluid is at least partially formed by a chemical, into a main flow delimited by a duct wall.
Die Erfindung betrifft auch eine Mischanordnung zur Einmischung von wenigstens einem ersten und einem zweiten Fluid über jeweils eine Düse mit einer The invention also relates to a mixing arrangement for mixing at least a first and a second fluid via a respective nozzle with a
Düsenöffnung, von denen zumindest das zweite Fluid wenigstens teilweise von einer Chemikalie gebildet wird, in einen von einer Kanalwand begrenzten Hauptstrom, insbesondere zur Durchführung des Verfahrens. Nozzle opening, of which at least the second fluid is at least partially formed by a chemical in a bounded by a channel wall main flow, in particular for carrying out the method.
Bei der Herstellung der Faserstoffsuspension kommen zunehmend Chemikalien zum Einsatz, die den Herstellungsprozess und/oder die Qualität der Faserstoffbahn positiv beeinflussen sollen. Dabei handelt es sich meist um Fixier- oder Retentionsmittel. Beim Zuführen eines Fluids in einen Hauptstrom, insbesondere jedoch in eine strömende Faserstoffsuspension stellt sich grundsätzlich das Problem einer möglichst guten Durchmischung. Dabei ist der Grad der Durchmischung auch mit dem In the manufacture of the pulp suspension increasingly chemicals are used, which should positively influence the manufacturing process and / or the quality of the fibrous web. These are usually fixing or retention agents. When feeding a fluid into a main stream, but in particular into a flowing pulp suspension, there is basically the problem of the best possible thorough mixing. Here is the degree of mixing with the
Chemikalienbedarf verbunden. Associated with chemicals.
Um den Chemikalienbedarf zu minimieren gibt es bereits seit längerer Zeit To minimize the need for chemicals has been around for some time
Bestrebungen die Durchmischung zu verbessern, was jedoch bisher noch nicht ausreichend befriedigen kann. Efforts to improve the mixing, but so far can not satisfy enough.
Problematisch sind dabei insbesondere auch Ablagerungen im Bereich der In particular, deposits in the area of the are problematic
Eindüsung. Injection.
Die Aufgabe der Erfindung ist es daher eine möglichst umfassende Einmischung einer Chemikalie in einen Hauptstrom unter Vermeidung von Ablagerungen zu gewährleisten. Erfindungsgemäß wurde die Aufgabe hinsichtlich des Verfahrens dadurch gelöst, dass ein erstes Fluid zumindest teilweise in Strömungsrichtung des Hauptstromes vor einem zweiten Fluid in den Hauptstrom eingedüst wird und die Eintrittsstelle des zweiten Fluids in den Hauptstrom weiter von der Kanalwand entfernt ist als die Eintrittstelle des ersten Fluids in den Hauptstrom. The object of the invention is therefore to ensure the widest possible interference of a chemical in a main stream while avoiding deposits. According to the invention, the object with regard to the method has been achieved in that a first fluid is at least partially injected in the flow direction of the main flow before a second fluid in the main stream and the point of entry of the second fluid in the main flow is further away from the channel wall than the inlet point of the first fluid in the mainstream.
Da das zweite Fluid, welches vorzugsweise zumindest teilweise von einer Chemikalie gebildet wird, mit Abstand zur Kanalwand in den Hauptstrom eingedüst wird, wird bereits einer Ablagerung im Bereich dieser Eindüsung und an der Kanalwand entgegengewirkt. Außerdem unterstützt dies auch die Vermischung, da diese vom Rand des Hauptstroms weg verlagert wird. Since the second fluid, which is preferably at least partially formed by a chemical, is injected into the main stream at a distance from the channel wall, deposition in the region of this injection and at the channel wall is already counteracted. In addition, this also supports the mixing, as it is shifted away from the edge of the main stream away.
Hinzukommt, dass sich der nach der Eindüsung des ersten Fluids in den Hauptstrom ergebende Mischstrom in Strömungsrichtung des Hauptstroms abgelenkt wird und so zumindest die Düse, möglichst jedoch auch die Düsenöffnung des zweiten Fluids umströmt, was ebenfalls eine Ablagerung behindert. Außerdem schont eine In addition, the mixed flow resulting from the injection of the first fluid into the main flow is deflected in the direction of flow of the main flow and thus flows around at least the nozzle, if possible also the nozzle opening of the second fluid, which likewise impedes deposition. In addition, a spares one
Umströmung der Düsenöffnung für das zweite Fluid die Chemikalie vor der starken Beanspruchung beim Austritt in den Hauptstrom. Flow around the nozzle opening for the second fluid, the chemical from the heavy stress on exit into the main stream.
Im Ergebnis kommt es zu einer intensiven Vermischung beider Fluide mit dem As a result, there is an intensive mixing of the two fluids with the
Hauptstrom. Main power.
Besondere Vorteile biete die Erfindung hinsichtlich Durchmischung bei einem von einer Faserstoffsuspension zur Herstellung einer Papier-, Karton-, Tissue- oder einer anderen Faserstoffbahn gebildeten Hauptstrom. Vorteilhaft ist die Anwendung jedoch auch bei Hauptströmen, die von Prozess-, Frischwasser o.ä. gebildet werden. The invention offers particular advantages with regard to thorough mixing in a main stream formed by a pulp suspension for producing a paper, board, tissue or other fibrous web. However, the application is also advantageous for main streams, etc. of process, fresh water. be formed.
Dabei können die beigemischten Fluide von Chemikalien, einer Faserstoffsuspension oder Wasser gebildet werden, wobei In Abhängigkeit von der Art und Wirkung einer Chemikalie diese auch bereits vorab der Faserstoffsuspension oder dem Wasser beigemischt sein kann. Sofern neben dem zweiten noch weitere Fluide in den Hauptstrom eingedüst und gemischt werden sollen, die zumindest teilweise von einer Chemikalie gebildet werden, so ist es vorteilhaft, wenn das erste Fluid zumindest teilweise in In this case, the admixed fluids can be formed by chemicals, a pulp suspension or water, and depending on the nature and effect of a chemical, these may also be added in advance to the pulp suspension or the water. If, in addition to the second, further fluids are to be injected and mixed into the main stream, which are at least partially formed by a chemical, it is advantageous if the first fluid is at least partially in
Strömungsrichtung des Hauptstromes vor dem weiteren Fluid in den Hauptstrom eingedüst wird und die Eintrittsstelle des weiteren Fluids in den Hauptstrom weiter von der Kanalwand entfernt ist als die Eintrittstelle des ersten Fluids in den Flow direction of the main stream is injected before the other fluid in the main stream and the entry point of the other fluid in the main flow is further away from the channel wall than the inlet point of the first fluid in the
Hauptstrom. Main power.
Dies führt zu einer wesentlichen Vereinfachung, da hier das erste Fluid gleichzeitig die Einmischung des zweiten und weiterer Fluide unterstützt. This leads to a substantial simplification, since here the first fluid simultaneously assists in the mixing of the second and further fluids.
Entsprechend der Art und Wirkung der Chemikalien der Fluide kann es vorteilhaft sein, wenn die Düsenöffnungen des zweiten und weiteren Fluids in Depending on the nature and effect of the chemicals of the fluids, it may be advantageous if the nozzle openings of the second and further fluid in
Strömungsrichtung des Hauptstroms nebeneinander angeordnet sind. Je nach Grad der gewünschten Vermischung und Verwirblung können die Eintrittsstellen dieser Fluide in den Hauptstrom gleich oder unterschiedlich weit von der Kanalwand entfernt liegen. Flow direction of the main flow are arranged side by side. Depending on the degree of mixing desired and Verwirblung the entry points of these fluids in the main flow can be the same or different distances from the channel wall.
Der Abstand der Düsenöffung des zweiten und weiteren Fluids zur Kanalwand sollte zwischen 5 mm und 10% der maximalen Querschnittsausdehnung des Hauptstroms liegen. The distance of the nozzle opening of the second and further fluid to the channel wall should be between 5 mm and 10% of the maximum cross-sectional dimension of the main flow.
Es kann allerdings ebenso von Vorteil sein, wenn die Eintrittstelle des zweiten Fluids die Eintrittstelle des weiteren Fluids oder die Düse für das weitere Fluid umschließt. Im ersten Fall befinden sich die Eintrittstellen der Fluid nebeneinander und im anderen Fall reicht die Eintrittsstelle des weiteren Fluids weiter in den Hauptstrom hinein als die Eintrittstelle des zweiten Fluids. However, it may also be advantageous if the inlet point of the second fluid encloses the inlet point of the further fluid or the nozzle for the further fluid. In the first case, the entry points of the fluid are juxtaposed, and in the other case, the point of entry of the further fluid extends further into the main flow than the entry point of the second fluid.
Um die Vermischung der Fluide mit dem Hauptstrom durch eine starke Verwirblung zu unterstützen sollten die Fluide bzw. der von den Düsen ausgehende Düsenstrahl mit einem Winkel zwischen 10 und 170°, vorzugsweise zwischen 70 und 1 10° zur Strömungsrichtung des Hauptstromes in diesen eingedüst werden. Hinsichtlich der Mischanordnung ist wesentlich, dass die Düse für das zweite Fluid durch die Düsenöffnung für das erste Fluid über die Kanalwand hinaus in den In order to assist the mixing of the fluids with the main flow by a strong turbulence, the fluids or the nozzle jet emanating from the nozzle should be injected at an angle of between 10 and 170 °, preferably between 70 and 110 ° to the flow direction of the main flow. With regard to the mixing arrangement, it is essential that the nozzle for the second fluid through the nozzle opening for the first fluid beyond the channel wall in the
Hauptstrom hineinreicht. Im Ergebnis bildet das erste Fluid mit dem Hauptstrom einen Mischstrom, welcher die Düse und möglichst auch deren Düsenöffnung des zweiten Fluids mit einer Richtungskomponente in Richtung der Eindüsung und in Main current extends. As a result, the first fluid with the main flow forms a mixed flow, which the nozzle and possibly also the nozzle opening of the second fluid with a directional component in the direction of the injection and in
Strömungsrichtung des Hauptstroms umströmt. Flow direction of the main flow flows around.
Dieser Mischstrom verhindert Ablagerungen an der Kanalwand sowie der Eindüsung, welche vom zweiten Fluid ausgehen könnten und schont außerdem die Chemikalie bei der Eindüsung in den Hauptstrom. Auch die Einmischung des zweiten Fluids in den Hauptstrom wird von diesem Mischstrom gefördert. This mixed flow prevents deposits on the channel wall and the injection, which could emanate from the second fluid and also protects the chemical during the injection into the main flow. The mixing of the second fluid in the main stream is promoted by this mixed stream.
Zur Vereinfachung der Konstruktion aber auch um Ablagerungen an der Düse des ersten Fluids zu verhindern, sollte die Düsenöffnung des ersten Fluids möglichst nah an der Kanalwand liegen, möglichst mit dieser eine Ebene bilden. To simplify the construction but also to prevent deposits on the nozzle of the first fluid, the nozzle opening of the first fluid should be as close as possible to the channel wall, if possible with this form a plane.
Wie bereits erwähnt, können auch weitere Fluide, welche zumindest teilweise von einer Chemikalie gebildet werden, in den Hauptstrom eingedüst werden. As already mentioned, other fluids, which are at least partially formed by a chemical, can also be injected into the main stream.
Dabei können die Düsen für das zweite und das weitere Fluid mit Vorteil durch verschiedene Düsenöffnungen für unterschiedliche oder das gleiche Fluid in den Hauptstrom geführt werden. Der Abstand der Düsenöffnungen des zweiten und des weiteren Fluids zur Kanalwand kann dabei gleich oder unterschiedlich sein. In this case, the nozzles for the second and the further fluid can be guided with advantage through different nozzle openings for different or the same fluid in the main stream. The distance between the nozzle openings of the second and further fluid to the channel wall may be the same or different.
Eine vorteilhafte Ausführung ergibt sich ebenso, wenn die Düsen für das zweite und das weitere Fluid gemeinsam durch die Düsenöffnung für das erste Fluid über die Kanalwand hinaus in den Hauptstrom hineinreichen. Dabei können die An advantageous embodiment also results if the nozzles for the second and the further fluid jointly extend through the nozzle opening for the first fluid beyond the channel wall into the main flow. The can
Düsenöffnungen für das zweite und das weitere Fluid in Strömungsrichtung des Hauptstroms mit gleichem oder unterschiedlichem Abstand zur Kanalwand Nozzle openings for the second and the further fluid in the flow direction of the main flow with equal or different distance to the channel wall
nebeneinander liegen. Es kann jedoch ebenso vorteilhaft sein, wenn die Düse für das weitere Fluid durch die Düsenöffnung für das zweite Fluid in den Hauptstrom hineinreicht, wobei die Düsenöffnungen den gleichen oder einen unterschiedlichen Abstand zur Kanalwand haben. Entsprechend den Anforderungen an die Durchmischung, die Art der Fluide sowie die Gestaltung der Kanalwand und des Kanalquerschnitts können die Düsenöffnungen einen runden oder eckigen Querschnitt haben. Auch können die Düsen die jeweiligen Düsenöffnungen mittig oder aber außermittig durchstoßen. lie next to each other. However, it may also be advantageous if the nozzle for the further fluid extends through the nozzle opening for the second fluid in the main stream, wherein the nozzle openings have the same or a different distance from the channel wall. Depending on the requirements of the mixing, the type of fluids and the design of the channel wall and the channel cross section, the nozzle openings may have a round or square cross-section. The nozzles can pierce the respective nozzle openings centrally or eccentrically.
Die Reichweite der Düsenstrahlen hängt neben den Parametern des Hauptstromes im Wesentlichen vom Fluiddruck an der Düsenöffnung, der Strahlfläche sowie deren Veränderung über die Länge des Düsenstrahls ab. The range of the jets depends in addition to the parameters of the main flow substantially from the fluid pressure at the nozzle opening, the jet area and their change over the length of the jet.
Ein geringerer Fluiddruck führt genauso wie eine starke Verbreiterung des A lower fluid pressure leads as well as a strong broadening of the
Düsenstrahls zu einer Verminderung der Reichweite des Düsenstrahls im Jet to a reduction in the range of the jet in the
Hauptstrom. Main power.
Dies bietet die Möglichkeit die Reichweite der Düsenstrahlen in der gewünschten Form zu beeinflussen. This offers the possibility to influence the range of the nozzle jets in the desired shape.
Insbesondere in Abhängigkeit von der Stärke des Hauptstromes können die In particular, depending on the strength of the main stream, the
Düsenstrahlen zur Strömungsrichtung des Hauptstromes geneigt, vorzugsweise entgegen dieser Strömungsrichtung geneigt oder aber senkrecht zur Nozzle jets inclined to the flow direction of the main stream, preferably inclined against this flow direction or perpendicular to the
Strömungsrichtung des Hauptstromes ausgerichtet sein. Be aligned flow direction of the main flow.
Zur Minimierung des Herstellungsaufwandes aber auch zur Schaffung ausgeglichener Strömungsverhältnisse ist es von Vorteil, wenn der von der Kanalwand begrenzte Hauptstrom einen runden, insbesondere einen kreisförmigen Querschnitt aufweist. Allerdings sind bei bestimmten Anwendungen eckige, insbesondere rechteckige Querschnitte angebracht. Dies gilt insbesondere auch dann, wenn die den In order to minimize the production costs but also to create balanced flow conditions, it is advantageous if the main flow delimited by the channel wall has a round, in particular a circular cross-section. However, in certain applications angular, in particular rectangular cross sections are appropriate. This is especially true when the
Hauptstrom führende Kanalwand nach oben offen ist. Main flow leading channel wall is open at the top.
Nachfolgend soll die Erfindung an mehreren Ausführungsbeispielen näher erläutert werden. In der beigefügten Zeichnung zeigen die Figuren 1 bis 4 schematische Querschnitte durch verschiedene Mischanordnungen. Die hier dargestellten Mischanordnungen dienen zur Beimischung von mehreren Fluiden 1 ,2,3,4 zu einem fluiden Hauptstrom 6 aus einer Faserstoffsuspension, welcher in einem rohrförmigen Kanal zu einem Stoffauflauf einer Maschine zur Herstellung einer Faserstoffbahn , insbesondere einer Papierbahn geführt wird und eine Stoffdichte zwischen 0,05 und 7,0 %, insbesondere zwischen 0,2 und 2,5 % aufweist. The invention will be explained in more detail below with reference to several exemplary embodiments. In the accompanying drawing, Figures 1 to 4 show schematic cross sections through various mixing arrangements. The mixing arrangements shown here serve for admixing a plurality of fluids 1, 2, 3, 4 to a main fluid flow 6 from a pulp suspension, which is guided in a tubular channel to a headbox of a machine for producing a fibrous web, in particular a paper web, and a consistency between 0.05 and 7.0%, in particular between 0.2 and 2.5%.
Einige Fluide 2,3 werden hierbei zumindest teilweise von Chemikalien, insbesondere Retentionsmitteln, wie beispielsweise Polyacrylamid, Polyvinylamin, Polyethylenoxid, Fixiermitteln oder aber auch von Mikropartikeln, wie z.B. Bentonit oder Silikat gebildet. Some fluids 2,3 are hereby at least partially of chemicals, in particular retention agents, such as polyacrylamide, polyvinylamine, polyethylene oxide, fixatives or even of microparticles, such. Bentonite or silicate formed.
Um einen thermischen Schock dieser Chemikalien bei ihrer Eindüsung zu vermeiden, ist es meist von Vorteil, deren Temperatur an die Temperatur des Hauptstroms 6 anzugleichen, d.h. in der Regel zu erwärmen. In order to avoid a thermal shock of these chemicals during their injection, it is usually advantageous to adjust their temperature to the temperature of the main stream 6, i. usually to warm.
Dabei setzt eine umfassende Wirkung dieser Chemikalien auch eine intensive A comprehensive effect of these chemicals also sets an intensive one
Vermischung der Fluide 2,3 in dem Hauptstrom 6 voraus. Mixing of the fluids 2,3 in the main stream 6 ahead.
Die Fluide 1 ,2,3,4 können aber zumindest teilweise auch von Faserstoffsuspension oder Wasser (Prozess- oder Frischwasser) gebildet werden. Falls die Fluide 1 ,4 gänzlich aus Faserstoffsuspension oder Wasser bestehen, so dienen sie im However, the fluids 1, 2, 3, 4 can also be formed, at least in part, by pulp suspension or water (process or fresh water). If the fluids 1, 4 consist entirely of pulp suspension or water, they serve in
Wesentlichen der Turbulenzbildung im Hauptstrom 6 und bei Wasser einer Essentially the turbulence in the main stream 6 and a water
Verdünnung des Hauptstroms 6. Es besteht allerdings auch die Möglichkeit einem Fluid 1 ,2,3,4 aus einer Dilution of the main stream 6. However, there is also the possibility of a fluid 1, 2,3,4 from a
Faserstoffsuspension oder Wasser vor der Eindüsung in den Hauptstrom 6 eine Chemikalie beizumischen. Diese Vormischung ist mitunter möglich, falls keine wesentliche Vorreaktion der Chemikalie oder Ablagerungen durch diese zu Pulp suspension or water before spraying into the main stream 6 to mix a chemical. This premixing is sometimes possible if there is no substantial pre-reaction of the chemical or deposits through it
befürchten sind. Im Ergebnis verbessert sich auch der Vermischungsgrad der entsprechenden Chemikalie im Hauptstrom 6. are afraid. As a result, the degree of mixing of the corresponding chemical in the main stream 6 also improves.
Bei den in den Figuren gezeigten Mischanordnungen wird der Hauptstrom 6 durch einen, von einer Kanalwand 5 begrenzten Kanal mit kreisförmigen Querschnitt geführt. Dabei ist eine Mehrzahl von Mischanordnungen zur Beimischung der Fluide 1 ,2,3,4 in den Hauptstrom 6 vorzugsweise regelmäßig über den Umfang des Kanals verteilt möglich. In the mixing arrangements shown in the figures, the main stream 6 passes through one guided by a channel wall 5 channel with circular cross-section. In this case, a plurality of mixing arrangements for admixing the fluids 1, 2, 3, 4 into the main flow 6 are preferably possible distributed over the circumference of the channel.
Die in Figur 1 dargestellte Mischanordnung ist sehr einfach aufgebaut und wird im wesentlichen von zwei Düsen 1 1 ,12 gebildet, die ein erstes Fluid 1 und ein zweites Fluid 2 quer zur Strömungsrichtung 7 des Hauptstromes 6 in diesen eindüsen. Dabei besteht zumindest das zweite Fluid 2 teilweise aus einer Chemikalie. The mixing arrangement shown in Figure 1 is very simple and is essentially formed by two nozzles 1 1, 12 which inject a first fluid 1 and a second fluid 2 transversely to the flow direction 7 of the main stream 6 in this. At least the second fluid 2 consists partly of a chemical.
Wesentlich ist hierbei, dass die Düsenöffnung 8 der Düse 1 1 für das erste Fluid 1 in der Ebene der Kanalwand 5 liegt, was Ablagerungen in diesem Eintrittsbereich des Fluids 1 verhindern soll. It is essential here that the nozzle opening 8 of the nozzle 1 1 for the first fluid 1 is in the plane of the channel wall 5, which should prevent deposits in this inlet region of the fluid 1.
Dagegen ist die Düse 12 für das zweite Fluid 2 mittig durch die Düsenöffnung 8 der Düse 1 1 des ersten Fluids 1 in den Hauptstrom 6 hineingeführt. Damit liegt die Düsenöffnung 9 der Düse 12 für das zweite Fluid 2 nicht nur relativ tief im Hauptstrom 6 sonder auch relativ weit entfernt von der Kanalwand 5. Dies ist von Vorteil, weil wegen der Chemikalien des zweiten Fluids 2 verstärkt mit Ablagerungen im In contrast, the nozzle 12 for the second fluid 2 is guided centrally through the nozzle opening 8 of the nozzle 1 1 of the first fluid 1 in the main stream 6. Thus, the nozzle opening 9 of the nozzle 12 for the second fluid 2 is not only relatively deep in the main stream 6 but also relatively far away from the channel wall 5. This is advantageous because because of the chemicals of the second fluid 2 reinforced with deposits in the
Eintrittsbereich in den Hauptstrom 6 zu rechnen ist, was jedoch durch das Entry area is to be expected in the main stream 6, however, by the
Hineinragen in den Hauptstrom 6 behindert wird. Hereininragen is hampered in the main stream 6.
Des weiteren bildet das erste Fluid 1 beim Eindüsen in den Hauptstrom 6 einen Mischstrom mit einer Komponente in und quer zur Strömungsrichtung 7 des Furthermore, when injected into the main flow 6, the first fluid 1 forms a mixed flow with a component in and transverse to the flow direction 7 of the
Hauptstroms 6, so dass die Düse 12 sowie der von ihr ausgehende Düsenstrahl mit dem zweiten Fluid 2 von dieser Mischströmung umströmt wird. Auch dies verhindert Ablagerungen, schont das zweite Fluid 2 beim Austritt in den Hauptstrom 6 und sorgt für eine intensive aber schonende Vermischung der beiden Fluide 1 ,2 mit dem Hauptstrom 6. Main flow 6, so that the nozzle 12 and the outgoing from her nozzle jet is flowed around with the second fluid 2 of this mixed flow. This also prevents deposits, protects the second fluid 2 when it exits into the main flow 6 and ensures intensive but gentle mixing of the two fluids 1, 2 with the main flow 6.
Im Gegensatz dazu zeigt Figur 2 eine Mischanordnung bei der das zweite 2 und ein weiteres 3 Fluid zumindest teilweise von einer Chemikalie gebildet und ebenfalls senkrecht zur Strömungsrichtung 7 des Hauptstroms 6 in diesen eingedüst wird. Das Eindüsen dieser beiden Fluide 2,3 erfolgt über Düsen 12,13, die über die Kanalwand 5 hinaus in den Hauptstrom 6 hineinragen. Dabei sind die Düsen 12,13 entsprechend dem zu Figur 1 beschriebenen Prinzip durch jeweils eine Düsenöffnung 8,15 geführt, welche in der Ebene der Kanalwand 5 liegt. In contrast, Figure 2 shows a mixing arrangement in which the second 2 and another 3 fluid at least partially formed by a chemical and is also injected perpendicular to the flow direction 7 of the main stream 6 in this. The injection of these two fluids 2,3 via nozzles 12,13, which protrude beyond the channel wall 5 also in the main stream 6. The nozzles are 12,13 accordingly the principle described for Figure 1 by a respective nozzle opening 8,15 out, which lies in the plane of the channel wall 5.
Während über die Düse 1 1 mit der Düsenöffnung 8 das erste Fluid 1 in den While on the nozzle 1 1 with the nozzle opening 8, the first fluid 1 in the
Hauptstrom 6 gelangt, wird über die Düse 14 mit der Düsenöffnung 15 ein weiteres Fluid 4 in den Hauptstrom 6 eingedüst. Main flow 6 passes, is injected via the nozzle 14 with the nozzle opening 15, a further fluid 4 in the main stream 6.
Im Ergebnis umströmt das erste Fuid 1 das zweite Fluid 2 und das vierte Fluid 4 das dritte Fluid 3 bei der Eindüsung. As a result, the first fluid 1 flows around the second fluid 2 and the fourth fluid 4 flows around the third fluid 3 during the injection.
Beispielhaft sind hierbei die Düsenöffnungen 9,16 der beiden Düsen 12,13 gleichweit von der Kanalwand 5 entfernt. Ergänzend befindet sich noch eine in den Hauptstrom 6 hineinragende Trennwand 10 zwischen den Düsenöffnungen 8,15 der Düsen 1 1 ,14, was eine sofortige Vermischung beider Fluide 1 ,4 dieser Düsen 1 1 ,14 verhindern soll. By way of example, the nozzle openings 9, 16 of the two nozzles 12, 13 are located equidistant from the channel wall 5. In addition, there is still a projecting into the main flow 6 partition 10 between the nozzle openings 8,15 of the nozzles 1 1, 14, which should prevent immediate mixing of the two fluids 1, 4 of these nozzles 1 1, 14.
Bei der in Figur 3 dargestellten Ausführung sind die Düsen 12,13 für das zweite 2 und das weitere Fluid 3 mit wenigstens einer Chemikalie durch eine gemeinsame In the embodiment shown in FIG. 3, the nozzles 12, 13 for the second 2 and the further fluid 3 with at least one chemical are common
Düsenöffnung 8 der Düse 1 1 für das erste Fluid 1 geführt. Nozzle opening 8 of the nozzle 1 1 for the first fluid 1 out.
Dementsprechend werden beide Düsen 12,13 sowie deren Düsenstrahlen mit den beiden Fluiden 2,3 von dem, beim Eintritt des ersten Fluids 1 in den Hauptstrom 6 gebildeten Mischstrom umströmt. Dabei reicht eine Düse 13 weiter in den Hauptstrom 6 als die andere Düse 12, was für zusätzliche Verwirbelungen sorgen und die Accordingly, both nozzles 12,13 and their jets with the two fluids 2,3 are flowed around by the, formed at the entrance of the first fluid 1 in the main stream 6 mixed flow. In this case, a nozzle 13 extends further into the main stream 6 than the other nozzle 12, which provide additional turbulence and the
Vermischung fördern kann. Can promote mixing.
Die Mischanordnung gemäß Figur 4 mischt drei Fluide 1 ,2,3 senkrecht zur The mixing arrangement according to FIG. 4 mixes three fluids 1, 2, 3 perpendicular to
Strömungsrichtung 7 in den Hauptstrom 6. Kennzeichnend ist hierbei, dass die Düse 12 für das zweite Fluid 2 durch die Düsenöffnung 8 der Düse 1 1 für das erste Fluid 1 und die Düse 13 für das dritte Fluid 3 durch die Düsenöffnung 9 der Düse 12 für das zweite Fluid 2 in den Hauptstrom 6 hineingeführt ist. Dabei ist die Düsenöffnung 16 der Düse 3 für das dritte Fluid 3 weiter von der Kanalwand 5 entfernt als die Flow direction 7 in the main flow 6. It is characteristic that the nozzle 12 for the second fluid 2 through the nozzle opening 8 of the nozzle 1 1 for the first fluid 1 and the nozzle 13 for the third fluid 3 through the nozzle opening 9 of the nozzle 12 for the second fluid 2 is led into the main flow 6. In this case, the nozzle opening 16 of the nozzle 3 for the third fluid 3 is further away from the channel wall 5 than the
Düsenöffnung 9 der Düse 12 für das zweite Fluid 2. Nozzle opening 9 of the nozzle 12 for the second fluid second
Daraus ergibt sich eine Umströmung des zweiten Fluids 2 bei der Eindüsung durch den Mischstrom vom ersten Fluid 1 und eine Umströmung des dritten Fluids 3 bei der Eindüsung durch einen Mischstrom des zweiten Fluids 2. Diese Umströmung schont insbesondere sehr langkettige Chemikalien, da diese bei der Eindüsung in den Hauptstrom 6 einer starken Belastung ausgesetzt sind, welche ihre Zusammensetzung und Funktion beeinträchtigen kann. This results in a flow around the second fluid 2 during the injection through the mixed flow from the first fluid 1 and a flow around the third fluid 3 during the injection through a mixed flow of the second fluid 2. This flow protects in particular very long-chain chemicals, as they are exposed to the injection into the main stream 6 of a heavy load, which may affect their composition and function.
Durch die hiermit erreichbare, intensive und schonende Vermischung kann der Chemikalienbedarf wesentlich minimiert werden. By this achievable, intensive and gentle mixing of the demand for chemicals can be significantly minimized.
Zur Ausbildung eines ausreichenden Düsenstrahls im Hauptstrom 6 sollten die Fluide 1 ,2,3,4 mit einem Druck in diesen eingedüst werden, der zwischen 1 ,5 und 10 bar über dem Druck im Hauptstrom 6 liegt. To form a sufficient jet in the main stream 6, the fluids 1, 2, 3, 4 should be injected at a pressure in the latter which is between 1, 5 and 10 bar above the pressure in the main stream 6.
Die Erfindung ermöglicht eine effiziente Einmischung und Vermischung von mehreren Chemikalien auch bei einem großen Mengenverhältnis zwischen Chemikalie und Hauptstrom. The invention enables efficient mixing and mixing of multiple chemicals even with a large chemical-to-mainstream ratio.
Claims
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201180033346.6A CN102971066B (en) | 2010-05-05 | 2011-04-18 | Mixed method and mixing apparatus |
| EP11717982.0A EP2566611B1 (en) | 2010-05-05 | 2011-04-18 | Mixing process and mixing arrangement |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE102010028573.0 | 2010-05-05 | ||
| DE102010028573A DE102010028573A1 (en) | 2010-05-05 | 2010-05-05 | mixing process |
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| Publication Number | Publication Date |
|---|---|
| WO2011138162A1 true WO2011138162A1 (en) | 2011-11-10 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/EP2011/056123 Ceased WO2011138162A1 (en) | 2010-05-05 | 2011-04-18 | Mixing process and mixing arrangement |
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| Country | Link |
|---|---|
| EP (1) | EP2566611B1 (en) |
| CN (1) | CN102971066B (en) |
| DE (1) | DE102010028573A1 (en) |
| WO (1) | WO2011138162A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20170197189A1 (en) * | 2010-09-28 | 2017-07-13 | Dow Global Technologies Llc | Reactive flow static mixer with cross-flow obstructions |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FI20125338A7 (en) | 2012-03-26 | 2013-09-27 | Wetend Tech Oy | A method of and an apparatus for mixing chemicals having opposite electric charges into a process liquid flow |
| CN103212320B (en) * | 2013-03-19 | 2015-04-29 | 重庆科技学院 | Vertical three-nozzle liquid static mixer |
| WO2016015991A1 (en) | 2014-07-29 | 2016-02-04 | Voith Patent Gmbh | Method and device for dosing and mixing at least one fluidic medium into a process stream |
| DE102014015036A1 (en) * | 2014-10-09 | 2016-04-28 | Steinmüller Babcock Environment Gmbh | Oxidation tank and method for treating effluent water of a seawater scrubber |
| CN112127191A (en) * | 2020-09-28 | 2020-12-25 | 新晃县自强纸业有限责任公司 | Conveying pipeline for producing corrugated medium paper by using waste paper box |
| CN112211019A (en) * | 2020-09-28 | 2021-01-12 | 新晃县自强纸业有限责任公司 | Method for producing corrugated medium paper by using waste paper box |
| CN116377165A (en) * | 2023-03-22 | 2023-07-04 | 江苏青云机械有限公司 | Strong Antibacterial Stainless Steel Casting Process |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0683266A1 (en) * | 1994-05-13 | 1995-11-22 | Voith Sulzer Papiermaschinen GmbH | Headbox for papermaking machine with local fluid admixture |
| WO2006005795A1 (en) * | 2004-07-15 | 2006-01-19 | Wetend Technologies Oy | Method and apparatus for feeding chemical into a liquid flow |
-
2010
- 2010-05-05 DE DE102010028573A patent/DE102010028573A1/en not_active Withdrawn
-
2011
- 2011-04-18 WO PCT/EP2011/056123 patent/WO2011138162A1/en not_active Ceased
- 2011-04-18 CN CN201180033346.6A patent/CN102971066B/en not_active Expired - Fee Related
- 2011-04-18 EP EP11717982.0A patent/EP2566611B1/en not_active Not-in-force
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0683266A1 (en) * | 1994-05-13 | 1995-11-22 | Voith Sulzer Papiermaschinen GmbH | Headbox for papermaking machine with local fluid admixture |
| WO2006005795A1 (en) * | 2004-07-15 | 2006-01-19 | Wetend Technologies Oy | Method and apparatus for feeding chemical into a liquid flow |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20170197189A1 (en) * | 2010-09-28 | 2017-07-13 | Dow Global Technologies Llc | Reactive flow static mixer with cross-flow obstructions |
| US9975094B2 (en) * | 2010-09-28 | 2018-05-22 | Dow Global Technologies Llc | Reactive flow static mixer with cross-flow obstructions |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102971066A (en) | 2013-03-13 |
| DE102010028573A1 (en) | 2011-11-10 |
| CN102971066B (en) | 2016-08-03 |
| EP2566611B1 (en) | 2014-06-11 |
| EP2566611A1 (en) | 2013-03-13 |
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