CN214513854U - Static mixer - Google Patents

Abstract

The utility model discloses a static mixer, it includes the casing, sets up the mixing unit in the casing, the mixing unit includes the water conservancy diversion post, sets gradually at least a slice single helix twisted piece and at least two sets of double helix twisted pieces on the water conservancy diversion post along fluid flow direction, double helix twisted pieces comprises two syntropy helix twisted pieces. The utility model provides a static mixer, it accomplishes the homogeneous mixing through the continuous fluid flow mode that changes for the fluid mixing is more even.

Description

Static mixer

Technical Field

The utility model belongs to the technical field of the fluid mixes, specifically speaking relates to a static mixer.

Background

The static mixer is a high-efficiency mixing device without moving parts, and the basic working mechanism of the static mixer is to change the flowing state of fluid in a pipe by using a mixing unit body fixed in the pipe so as to achieve the purposes of good dispersion and full mixing of different fluids.

The working principle of the static mixer is that fluid flows in a pipeline to impact various plate elements, the velocity gradient of laminar motion of the fluid is increased or turbulent flow is formed, the laminar flow is divided, moved and recombined, and in the turbulent flow, the fluid can generate violent vortex in the cross section direction besides the three conditions, and strong shearing force acts on the fluid to further divide and mix the fluid, and finally the fluid is mixed to form the required emulsion. So called "static" mixers, means that there are no moving parts in the pipe, only static elements.

The common type of static mixer is an SX type static mixer, and the unit of the static mixer is composed of a plurality of X type units by crossed horizontal bars according to a certain rule, and the technical characteristics are as follows: the degree of uneven mixing is s X-5%, which is suitable for the medium and high viscosity liquid-liquid reaction, mixing and absorption process with viscosity not more than 104 centipoises or the mixing and reaction process for producing high polymer fluid, and the using effect is better when the processing amount is larger. However, the static mixer completes uniform mixing by changing the way of fluid laminar flow, and the mixing capability is general, so that the fluid mixing requirements of gas-liquid mixing and high uniformity cannot be met.

Accordingly, further developments and improvements are still needed in the art.

SUMMERY OF THE UTILITY MODEL

In order to solve the above problems, a static mixer is proposed, which is particularly suitable for mixing gas and liquid by continuously changing the fluid flow mode to achieve uniform mixing.

In order to achieve the above object, the utility model provides a following technical scheme:

the utility model provides a static mixer, its includes the casing, sets up the mixing unit in the casing, mixing unit includes the guide post, sets gradually at least a slice single helix twisted piece and at least two sets of two helix twisted pieces on the guide post along the fluid flow direction, two helix twisted pieces comprise two syntropy helix twisted pieces.

Furthermore, the single spiral twisting piece is provided with one piece, the double spiral twisting pieces are provided with even groups, and the spiral directions of the adjacent groups of double spiral twisting pieces are opposite.

Preferably, four groups of double helical twisting sheets are arranged.

Furthermore, the fluid inlet end of the single helical twisting piece extends outwards along the helical direction relative to the fluid outlet end, and the single helical twisting piece and the helical twisting piece rotating in the opposite direction in the adjacent double helical twisting pieces are arranged in a staggered manner along the respective helical direction, the fluid inlet end of the helical twisting piece in the double helical twisting pieces extends outwards along the helical direction relative to the fluid outlet end, and the helical twisting pieces rotating in the opposite direction in the adjacent double helical twisting pieces are arranged in a staggered manner along the respective helical direction.

Furthermore, a first connection site used for fixedly connecting the single helical blade with the guide column is arranged between the single helical blade and the guide column, the first connection site enables a first gap to be formed between the single helical blade and the guide column, a second connection site used for fixedly connecting the double helical blade with the guide column is arranged between the double helical blade and the guide column, and the second connection site enables a second gap to be formed between the double helical blade and the guide column.

Furthermore, the first connection sites are provided with at least two first connection sites which are respectively located at the top and bottom ends of the single spiral twisted piece, and the second connection sites are provided with at least two second connection sites which are respectively located at the top and bottom ends of the spiral twisted piece corresponding to the spiral twisted pieces in the double spiral twisted pieces.

Furthermore, a first diversion trench used for changing the direction of fluid to flush the first connection site is arranged on the single-spiral twisted piece corresponding to the first connection site, and a second diversion trench used for changing the direction of fluid to flush the second connection site is arranged on the double-spiral twisted piece corresponding to the second connection site.

Furthermore, a connecting line between the first guide groove and the second guide groove is parallel to the axial direction of the guide column.

Preferably, the first diversion trench and the second diversion trench are arc-shaped notches.

Further, the casing includes the barrel, is fixed in the import flange of barrel one end, is fixed in the export flange of the barrel other end, form the cavity that holds that is used for holding mixing unit between import flange and barrel, the export flange, hold the cavity and be the cylindricality cavity, the both ends of water conservancy diversion post correspond import flange and export flange and are provided with the fixed part that is used for injecing mixing unit and hold the cavity respectively.

Advantageous effects

The utility model provides a static mixer compares with prior art and has following beneficial effect:

(1) when the fluid passes through the static mixer, the fluid flow modes (laminar flow and turbulent flow) are continuously changed to complete uniform mixing, so that the fluid is more uniformly mixed, and meanwhile, the pressure loss of the static mixer is not higher than 0.5Bar due to the accurate spiral twisted piece design;

(2) the single spiral twisting piece and the multiple groups of double spiral twisting pieces with opposite rotation directions are sequentially arranged, so that the fluid is better in dividing and converging effect, and higher in mixing efficiency and uniformity;

(3) the fluid impact force entering the static mixer is relieved through the single spiral twisting piece, the fluid sequentially enters the double spiral twisting pieces with opposite rotation directions and then continuously changes the flow direction of the fluid, the fluid positioned at the center can be pushed to the periphery, and the fluid at the periphery is pushed to the center, so that a good radial mixing effect is obtained.

(4) The single spiral twisted piece and the guide groove arranged on the spiral twisted piece effectively remove the sanitary dead angle of the contact position between the single spiral twisted piece and the guide column and the contact position between the double spiral twisted piece and the guide column, and avoid the fluid from remaining at the sanitary dead angle.

(5) The inlet flange, the outlet flange and the corresponding fixed tooth sheets on the flow guide column are mutually matched, so that the mixing unit is limited in the accommodating cavity, and the mixing unit is prevented from rotating along with the entering of fluid in the accommodating cavity.

Drawings

FIG. 1 is a schematic structural view of a static mixer according to embodiment 1 of the present invention;

FIG. 2 is a front view of a static mixer according to embodiment 1 of the present invention;

FIG. 3 is a cross-sectional view of the static mixer at A-A in FIG. 2;

fig. 4 is an isometric view of a mixing unit in embodiment 1 of the invention;

FIG. 5 is a partial enlarged view of FIG. 4 at B;

fig. 6 is a front view of a mixing unit in embodiment 1 of the present invention;

fig. 7 is a plan view of the mixing unit in embodiment 1 of the present invention.

In the drawings: 100. a housing; 110. a barrel; 120. an inlet flange; 130. an outlet flange; 200. a mixing unit; 210. a flow guide column; 220. a single helical twisting sheet; 221. a first diversion trench; 230. double helical twisting sheets; 232. a second guiding gutter; 241. a second gap; 250. and fixing the toothed sheet.

Detailed Description

In order to make those skilled in the art better understand the technical solution of the present invention, the following embodiments of the present invention are combined to make clear and complete description of the technical solution of the present invention, and based on the embodiments in the present application, other similar embodiments obtained by those skilled in the art without creative efforts shall all belong to the scope of protection of the present application. In addition, directional terms such as "upper", "lower", "left", "right", etc. in the following embodiments are directions with reference to the drawings only, and thus, the directional terms are used for illustration and not for limitation of the present invention.

Detailed description of the preferred embodiment 1

A static mixer, as shown in fig. 1-7, comprises a housing 100, and a mixing unit 200 disposed in the housing 100, wherein the mixing unit 200 comprises a flow guiding column 210, and at least one single helical twisting blade 220 and at least two sets of double helical twisting blades 230 sequentially disposed on the flow guiding column 210 along a fluid flowing direction. The static mixer of the present embodiment can reduce the impact force of the entering fluid by the design of the single helical twisting blade 220, so that the entering fluid can smoothly and stably enter the double helical twisting blade 230 for mixing. The double-helix twisted piece 230 increases the effect of fluid turbulence and improves the mixing speed and mixing uniformity of the fluid.

Specifically, the double-helical twisted piece 230 is composed of two equidirectional helical twisted pieces, the initial positions of the two helical twisted pieces are different, the initial positions of the two helical twisted pieces are symmetrical with respect to the axis of the guide column 210, and the pitches of the two helical twisted pieces are equal.

Specifically, the single helical blade 220 is provided with one blade, the double helical blades 230 are provided with even groups, and since there is pressure loss when fluid enters the single helical blade 220 and the double helical blades 230, in order to control the pressure loss value of the fluid flowing through the static mixer, in the embodiment, the single helical blade 220 is provided with one blade, and the double helical blades 230 are provided with four groups, which have the function of ensuring that the fluid and the gas are uniformly mixed and simultaneously keeping the pressure loss of the fluid flowing through the static mixer within 0.5Bar, so that the fluid flowing through the static mixer meets the specified pressure loss requirement.

Further, the spiral directions of the adjacent double helical twisting plates 230 are opposite, and the arrangement mode enables the fluid to continuously change the flow direction after passing through the adjacent double helical twisting plates 230, so that the fluid at the center can be pushed to the periphery, and the fluid at the periphery is pushed to the center, thereby obtaining good radial mixing effect.

In this embodiment, the spiral direction of the single spiral twisted piece 220 is right-handed, the spiral direction of the spiral twisted piece in the adjacent double spiral twisted piece 230 is right-handed, and the spiral direction of the spiral twisted piece in the adjacent double spiral twisted piece 230 is left-handed, right-handed, and left-handed in sequence.

Further, the distance between the bottom end of the single helical twisting piece 220 and the top end of the adjacent double helical twisting piece 230 is larger than the distance between the bottom end of the double helical twisting piece 230 and the top end of the adjacent double helical twisting piece 230, and the distance is used for completely dispersing fluid and gas into the adjacent double helical twisting piece 230 through the single helical twisting piece 220 as far as possible and uniformly mixing the fluid and the gas through the double helical twisting pieces 230 in sequence. In each set of double helical blades 230, the spacing between adjacent double helical blades 230 is equal.

Preferably, the distance between the bottom end of a single helical twisting blade 220 and the top end of an adjacent double helical twisting blade 230 is twice the distance between the bottom end of a double helical twisting blade 230 and the top end of an adjacent double helical twisting blade 230.

Further, the fluid inlet end of the single helical twisting blade 220 extends outwards along the helical direction relative to the fluid outlet end, so that the distance between the fluid inlet end and the fluid outlet end of the single helical twisting blade 220 is greater than one thread pitch, and meanwhile, the single helical twisting blade 220 and the helical twisting blades rotating in opposite directions in the adjacent double helical twisting blades 230 are arranged in a staggered manner along the respective helical directions; the fluid inlet end of double helical flighting 230 extends outwardly in a helical direction relative to the fluid outlet end. Specifically, the fluid entry end of two reverse spiral twisted pieces that set up in two spiral twisted pieces 230 all outwards extends for fluid outlet end, the fluid entry end of spiral twisted piece is greater than a pitch with fluid outlet end's distance, the crisscross setting of spiral twisted piece 220 along respective helical direction of mutual opposite rotation in adjacent two spiral twisted pieces 230 simultaneously, the effect of above-mentioned setting lies in rushing out two spiral twisted pieces 230 when avoiding fluid whereabouts, guarantees that fluid falls in proper order along two spiral twisted pieces, and then guarantees the homogeneous mixing on two spiral twisted pieces between the fluid.

Further, a first connection site for fixedly connecting the single helical blade 220 with the guide column 210 is arranged between the single helical blade 220 and the guide column 210, the first connection site enables a first gap to be formed between the single helical blade 220 and the guide column 210, a second connection site for fixedly connecting the double helical blade 230 with the guide column 210 is arranged between the double helical blade 230 and the guide column 210, the second connection site enables a second gap 241 to be formed between the double helical blade 230 and the guide column 210, the first gap and the second gap 241 indicate that the single helical blade 220 and the guide column 210 and the double helical blade 230 and the guide column 210 are not fixedly attached to each other, and the first gap and the second gap serve to reduce the dead angle area of connection between the single helical blade 220 and the guide column 210 and between the double helical blade 230 and the guide column 210 and reduce the residual amount of fluid at the contact position between the single helical blade 220 and the guide column 210 and between the double helical blade 230 and the guide column 210, the dead angle cleaning workload of the subsequent process is reduced.

Further, the first connection sites are provided with at least two first connection sites which are respectively located at the top and bottom ends of the single spiral twisted piece 220, and the second connection sites are provided with at least two second connection sites which are respectively located at the top and bottom ends of the spiral twisted piece corresponding to the spiral twisted piece in the double spiral twisted piece 230.

A first diversion trench 221 for changing the direction of the fluid to flush the first connection site is arranged on the single helical blade 220 corresponding to the first connection site, a second diversion trench 232 for changing the direction of the fluid to flush the second connection site is arranged on the double helical blade 230 corresponding to the second connection site, and the first diversion trench 221 and the second diversion trench 232 play a role in guiding the fluid.

Further, a connecting line between the first guiding groove 221 and the second guiding groove 232 is parallel to the axial direction of the guiding column 210, so that the impact force of the fluid entering the first guiding groove 221 and the second guiding groove 232 from top to bottom is ensured to be large, and the flushing effect on the corresponding first connecting position or the second connecting position is ensured to be large.

Preferably, the first guiding gutter 221 and the second guiding gutter 232 are arc-shaped notches, the opening angles of the arc-shaped notches face the first connecting point and the second connecting point respectively, when the fluid falls, the direction of the fluid is changed under the action of the arc-shaped notches, so that the fluid is flushed towards the corresponding first connecting point or the corresponding second connecting point, the sanitary dead angle of the contact position between the single helical twisted piece 220 and the guiding column 210 and the contact position between the double helical twisted piece 230 and the guiding column 210 is effectively cleared, and the fluid is prevented from remaining at the sanitary dead angle.

In this embodiment, the number of the first connection sites is three, the three first connection sites are respectively located at the top and bottom two ends and the center of the single helical twisting piece 220, on the basis of reducing the contact area between the single helical twisting piece 220 and the guide post 210 as much as possible, the connection stability between the single helical twisting piece 220 and the guide post 210 is improved, it is ensured that the connection between the single helical twisting piece 220 and the guide post 210 is not broken under the impact of fluid, the effect of high-pressure water impact resistance of the mixing unit 200 is realized, and further, the stability of the whole structure of the mixing unit 200 and the service life of the static mixer are improved. The first flow guide grooves 221 are respectively arranged corresponding to the first connection sites at the three positions, wherein one first flow guide groove 221 is arranged corresponding to the first connection sites at the top and the bottom of the single-spiral twisted piece 220, two first flow guide grooves 221 are arranged corresponding to the first connection sites at the center of the single-spiral twisted piece 220, the two first flow guide grooves 221 are respectively located at two sides of the first connection sites at the center of the single-spiral twisted piece 220, the flushing of dead corners at two sides of the first connection sites at the center of the single-spiral twisted piece 220 is realized, and the single-spiral twisted piece 220 is effectively prevented from being corroded by residual fluid. On the same way, the second connection site corresponds spiral twisted piece 230 in the spiral twisted piece and is provided with threely, three second connection site is located spiral twisted piece's top both ends and center department respectively, on the basis that reduces area of contact between spiral twisted piece and the guide post 210 as far as possible, improve the stability of being connected between spiral twisted piece and the guide post 210, guarantee that the junction between spiral twisted piece and the guide post 210 can not take place the fracture under fluidic impact, realize the effect of the resistant high-pressure water impact of hybrid cell 200, and then improve hybrid cell 200 overall structure's stability and static mixer's life. The second guiding gutter 232 corresponds the second hookup location setting of three position respectively, wherein, the second hookup location that second guiding gutter 232 corresponds spiral twister top bottom both ends sets up two respectively, the second hookup location that second guiding gutter 232 corresponds spiral twister center department is provided with two, two second guiding gutters 232 are located the both sides of spiral twister center department second hookup location respectively, realize washing of spiral twister center department second hookup location both sides dead angle, effectively prevent remaining fluid corrosion spiral twister.

Further, the housing 100 includes a cylinder 110, an inlet flange 120 fixed to one end of the cylinder 110, and an outlet flange 130 fixed to the other end of the cylinder 110, wherein a receiving cavity for receiving the mixing unit 200 is formed between the inlet flange 120 and the cylinder 110 and between the inlet flange 130 and the outlet flange 110, and the receiving cavity is a cylindrical cavity.

Further, the two ends of the flow guiding column 210 are respectively provided with a fixing portion for fixing the flow guiding column 210 to prevent the flow guiding column 210 from shaking in the accommodating cavity corresponding to the inlet flange 120 and the outlet flange 130.

Specifically, the fixing portion is a plurality of fixing teeth 250 uniformly arranged around the top and bottom ends of the flow guiding column 210. In this embodiment, three pieces of the fixed blade 250 are provided. The inlet flange 120 and the outlet flange 130 cooperate with the corresponding fixing teeth 250 of the guide column 210 to limit the mixing unit 200 in the receiving cavity, and prevent the guide column 210 from shaking in the receiving cavity due to the fluid entering the receiving cavity.

Specifically, the distance between the fixed tooth plate 250 and the inner wall of the cylinder 110 is 0.5-1mm, so that a large impact force is generated when fluid enters through the inlet flange 120, and the distance between the fixed tooth plate 250 and the inner wall of the cylinder 110 can eliminate a part of the impact force generated when the fluid enters into the cylinder 110, thereby avoiding the occurrence of the damage of the mixing unit 200 caused by the large impact force.

The sizes of the guide columns 210, the single helical twisting pieces 220 and the double helical twisting pieces 230 can be flexibly adjusted according to the size of the corresponding cylinder 110.

When the fluid laminar flow separation device is used, fluid enters the accommodating cavity through the top of the cylinder body 110, when the fluid enters the single spiral twisting piece 220, the impact force of the fluid is relieved by the streamline structure of the single spiral twisting piece 220, the fluid enters the double spiral twisting piece 230 along the single spiral twisting piece 220, the flow resistance in the whole process is small, no blockage occurs, meanwhile, the double spiral twisting piece 230 increases the speed gradient of the laminar flow movement of the fluid or forms turbulent flow, 'splitting-position moving-remixing' during laminar flow, and when the fluid is turbulent flow, the fluid can generate violent vortex flow in the cross section direction besides the three conditions, so that strong shearing force acts on the fluid, the fluid is further split and mixed, and particularly, the fluid-liquid mixing device has a good effect. The fluid is continuously cut, sheared, rotated and remixed by the single helical twisting sheet 220 and the double helical twisting sheet 230 in the static mixer, and finally the required mixed fluid is formed, so that the continuous, efficient and quick mixing process is realized.

The utility model discloses a mode (laminar flow and torrent) that constantly changes fluidic flow accomplishes even mixing process, and wherein the pressure loss of accurate single spiral twisted piece 220 and two spiral twisted pieces 230 makes static mixer is not higher than 0.5 Bar.

The above description is only a preferred embodiment of the present invention, and should not be taken as limiting the scope of the invention, i.e. the present invention is intended to cover all equivalent variations and modifications within the scope of the present invention.

Claims (10)

1. The static mixer is characterized by comprising a shell and a mixing unit arranged in the shell, wherein the mixing unit comprises a flow guide column, at least one single helical twisting piece and at least two groups of double helical twisting pieces, the single helical twisting pieces and the at least two groups of double helical twisting pieces are sequentially arranged on the flow guide column along the flowing direction of a fluid, and the double helical twisting pieces are composed of two equidirectional helical twisting pieces.

2. The static mixer of claim 1, wherein said single helical flighting is provided in one piece and said double helical flighting is provided in an even number of sets, adjacent sets of double helical flighting having opposite helical directions.

3. The static mixer of claim 2, wherein said double helical flighting is provided in four sets.

4. The static mixer of claim 2, wherein the fluid inlet end of the single helical flighting extends outwardly in a helical direction relative to the fluid outlet end and the single helical flighting is interleaved with the counter-rotating helical flighting of an adjacent pair of helical flighting in the respective helical direction, the fluid inlet end of a helical flighting of the pair of helical flighting extends outwardly in a helical direction relative to the fluid outlet end and the counter-rotating helical flighting of an adjacent pair of helical flighting is interleaved in the respective helical direction.

5. The static mixer of claim 1, wherein a first connection point for fixedly connecting the single helical blade with the guide post is arranged between the single helical blade and the guide post, the first connection point enables a first gap to be formed between the single helical blade and the guide post, a second connection point for fixedly connecting the double helical blade with the guide post is arranged between the double helical blade and the guide post, and the second connection point enables a second gap to be formed between the double helical blade and the guide post.

6. The static mixer of claim 5, wherein the first connection points are provided with at least two and two first connection points respectively located at the top and bottom ends of the single helical twisting sheet, and the second connection points are provided with at least two and two second connection points respectively located at the top and bottom ends of the helical twisting sheet corresponding to the helical twisting sheet in the double helical twisting sheet.

7. The static mixer of claim 5, wherein a first flow guide groove for changing the direction of the fluid to wash the first connection site is provided on the single-helix reamer corresponding to the first connection site, and a second flow guide groove for changing the direction of the fluid to wash the second connection site is provided on the double-helix reamer corresponding to the second connection site.

8. The static mixer of claim 7, wherein a line between the first and second channels is parallel to an axial direction of the guide post.

9. The static mixer of claim 7, wherein the first and second channels are arcuate notches.

10. The static mixer of claim 1, wherein the housing comprises a cylinder, an inlet flange fixed at one end of the cylinder, and an outlet flange fixed at the other end of the cylinder, wherein a receiving cavity for receiving the mixing unit is formed between the inlet flange and the cylinder, and the outlet flange, and the two ends of the flow guiding column are respectively provided with a fixing portion for fixing the flow guiding column to prevent the flow guiding column from shaking in the receiving cavity corresponding to the inlet flange and the outlet flange.

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