CN212348373U - Turbulent flow type liquid mixing structure - Google Patents
Turbulent flow type liquid mixing structure Download PDFInfo
- Publication number
- CN212348373U CN212348373U CN202020835335.6U CN202020835335U CN212348373U CN 212348373 U CN212348373 U CN 212348373U CN 202020835335 U CN202020835335 U CN 202020835335U CN 212348373 U CN212348373 U CN 212348373U
- Authority
- CN
- China
- Prior art keywords
- liquid
- mixing
- turbulent flow
- vortex
- tube
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Images
Abstract
The utility model discloses a vortex formula liquid mixed structure. This scheme includes the hybrid tube, the hybrid tube is provided with inlet and liquid outlet, the hybrid tube is the column, and both ends seal, inlet, liquid outlet set up respectively the both ends of hybrid tube, still be provided with vortex liquid mixing spare in the lumen of hybrid tube, vortex liquid mixing spare sets up a plurality ofly, and is a plurality of there is the through-flow clearance between the vortex liquid mixing spare. Through set up a plurality of vortex in the lumen in the hybrid tube and mix liquid spare, mix liquid spare through the vortex and form the hindrance to the flow of liquid, can only follow the vortex and mix the through-flow clearance of liquid spare and flow to take place the effect of choked flow, vortex, and then reach the effect of mixing liquid, thereby obtain the misce bene's mixed liquid from the liquid outlet, this kind of mixed structure has simple structure, advantage that occupation space is little.
Description
Technical Field
The utility model relates to a chemical industry field, concretely relates to vortex formula liquid mixed structure.
Background
In the chemical field, there are often cases where it is necessary to mix and stir the composition.
At present, in laboratories and production processes, such as hypochlorous acid production, mixing of liquid and liquid or liquid and solid components is still accomplished in a manner of a tank body with large occupied volume and a stirring device.
In the prior patent application of the applicant, the application number 201810770481.2 of the chinese utility model discloses a system for producing stable sterilization and disinfection solution, which comprises a first storage tank for storing weak acid liquid, a second storage tank for storing weak alkali liquid, a third storage tank for storing a solution a for providing hypochlorous acid ions, and a mixing reaction container for preparing sterilization and disinfection solution, wherein the reaction container is provided with a raw water input port, a weak acid liquid input port, a weak alkali liquid input port and a solution input port which are respectively used for connecting a raw water conveying pipeline, the first storage tank, the second storage tank and the third storage tank; the raw water input port is connected with a raw water conveying pipeline, a stop valve and a raw water PH measuring meter are arranged between the input port and the raw water conveying pipeline, a filter, a metering pump and a stop valve are arranged on pipelines between the first storage tank and the reaction container, between the second storage tank and the reaction container, and between the third storage tank and the reaction container, and a PH/hypochlorous acid sensor is arranged in the mixed reaction container and is used for measuring the PH value and the effective hypochlorous acid molecular concentration of the sterilization and disinfection solution; the mixing reaction container is also provided with an output port for connecting an outlet pipeline, and the outlet pipeline is provided with a shutoff valve and a filter;
the patent application also discloses that the mixing reaction container is a stirring reaction container, and in the actual production and application processes, the stirring reaction container has larger volume, large occupied space and is not easy to move, so that equipment for producing sterilized water is produced at a certain fixed position under the general condition, and the aim of incapability of flexibly changing the position due to heavy equipment is achieved if a factory building is moved or the position needs to be changed; in addition, the volume of the stirring reaction container is large, so that the stirring reaction container cannot meet the requirements of relevant occasions with limited production space or outdoor emergency medical assistance or outdoors.
Therefore, a liquid mixing structure with small occupied volume and good mixing effect is needed to meet the requirement of reducing the volume of mixing equipment on the whole, and the liquid mixing structure is suitable for the purposes of being portable outdoors and saving production space.
SUMMERY OF THE UTILITY MODEL
In order to solve the technical problem, an object of the utility model is to provide a vortex formula liquid mixed structure, it includes the hybrid tube, sets up a plurality of vortex in the lumen of hybrid tube and mixes liquid spare, mixes liquid spare through the vortex and cuts apart, crosses the liquid stream to reach mixed liquid's effect, this vortex formula liquid mixed structure has simple structure, advantage that occupation space is little.
In order to realize the purpose of the utility model, the utility model adopts the following technical scheme:
the utility model provides a vortex formula liquid mixed structure, includes the hybrid tube, the hybrid tube is provided with inlet and liquid outlet, the hybrid tube is the column, and both ends are sealed, inlet, liquid outlet set up respectively the both ends of hybrid tube, still be provided with vortex liquid mixing spare in the lumen of hybrid tube, vortex liquid mixing spare sets up a plurality ofly, and is a plurality of there is the through-flow clearance between the vortex liquid mixing spare.
Through setting up like this, mix the liquid in-process, add the liquid of treating mixing or stirring to the lumen of hybrid tube through the inlet, make liquid flow to the direction of liquid outlet by the inlet, if the liquid of adding can not independently flow, can pressurize liquid, liquid flows the in-process in the lumen, because the vortex mixes liquid spare and hinders the mobile formation of liquid, the through-flow clearance that can only follow the vortex and mix liquid spare flows, thereby take place the choked flow, the effect of vortex, and then reach the effect of mixing liquid, thereby obtain the misce bene's mixed liquid from the liquid outlet, this kind of mixed structure has simple structure, the little advantage of occupation space.
Preferably, the particle size D of the turbulent flow liquid mixing part is larger than that of the liquid inlet and the liquid outlet.
Through setting up like this, reducible vortex mixes liquid spare and gets into inlet, liquid outlet, avoids appearing the condition of blockking up inlet, liquid outlet.
Preferably, the particle diameters D of the turbulent mixing parts are the same or different.
Through setting up like this, the liquid spare size is mixed to the vortex can set up to the nonconformity to make the vortex mix the distribution in the through-flow clearance that the liquid spare formed and have certain randomness, make the liquid stream direction that the intracavity local flow is more various, make the liquid stream cut apart, the number of times of crossing increase more, improve mixed effect.
Preferably, the mixing pipe is internally provided with filter screens at the liquid inlet and the liquid outlet, and the aperture of each filter screen is smaller than the particle size D of the turbulent flow liquid mixing part.
Through setting up like this, avoid mixing the liquid spare and getting into and cause the jam phenomenon in inlet or the liquid outlet by the vortex in the mixing tube intracavity, stable, reliable in making the vortex formula liquid mixed structure use.
Preferably, a plurality of the turbulent flow liquid mixing pieces are fixedly connected to form a turbulent flow structure.
Through setting up like this, accessible connecting piece reciprocal anchorage between a plurality of vortex liquid mixing spare, perhaps a plurality of vortex liquid mixing spare an organic whole is formed to form a holistic vortex structure, reduce appear because of single vortex liquid mixing spare causes the unstable problem of liquid mixing effect because of the activity, and be convenient for produce.
Preferably, the turbulent liquid mixing part is one or a combination of a plurality of spheres, cylinders, prisms, cones, pyramids and ellipsoids.
Through setting up like this, the shape of vortex liquid mixing spare can select various, selects for use the combination in a flexible way according to the needs of mixing.
Preferably, the filter screen is a polyethylene screen.
Through the arrangement, the polyethylene net has better corrosion resistance, and is particularly suitable for being applied to production occasions of chlorine-containing disinfectant fluid by the turbulent flow type liquid mixing structure.
Preferably, the turbulent liquid mixing part is one or a combination of glass beads, ceramic beads and polyethylene beads.
Through the arrangement, the turbulent flow liquid mixing part is selected from one or a combination of a plurality of glass beads, ceramic beads and polyethylene beads, and the turbulent flow liquid mixing structure is particularly suitable for being applied to production occasions of chlorine-containing disinfectant fluid.
Preferably, the liquid inlet and the liquid outlet are provided with switches, two ends of the mixing pipe are respectively provided with a connecting port, the connecting ports are provided with sealing covers, and the two turbulent flow type liquid mixing structures connect the connecting ports on the two different mixing pipes through a connecting sleeve.
Through setting up like this, conveniently carry out vertical concatenation with a plurality of vortex formula liquid mixed structure, increase the length of liquid mixing, prolong liquid mixing time.
Preferably, on the same mixing tube, an insertion part extends from the connecting port at one end, the insertion part is matched with the connecting port at the other end, and the insertion part can be inserted into or screwed in the connecting port at the other end.
Through setting up like this, mosaic structure is simple and convenient, and structural wholeness is good.
Compared with the prior art, the utility model discloses profitable technological effect has been obtained:
1. through set up a plurality of vortex in the lumen in the hybrid tube and mix liquid spare, mix liquid spare through the vortex and form the hindrance to the flow of liquid, can only follow the vortex and mix the through-flow clearance of liquid spare and flow to take place the effect of choked flow, vortex, and then reach the effect of mixing liquid, thereby obtain the misce bene's mixed liquid from the liquid outlet, this kind of mixed structure has simple structure, advantage that occupation space is little.
2. The particle diameter D of the turbulent flow mixing part is larger than that of the liquid inlet and the liquid outlet or is provided with a filter screen, so that the turbulent flow type liquid mixing structure is stable and reliable in the use process.
3. It is a plurality of the liquid spare fixed connection is mixed in the vortex forms a vortex structure, reduces to appear because of single vortex mixes the liquid spare and causes the unstable problem of liquid effect because of the activity to be convenient for produce.
4. The turbulent flow liquid mixing structure also facilitates splicing.
Drawings
Fig. 1 is a schematic structural diagram of a first embodiment of the present invention;
fig. 2 is a schematic structural view in a top view direction according to an embodiment of the present invention;
FIG. 3 is a schematic diagram illustrating the splicing of two turbulent fluid mixing structures according to a first embodiment of the present invention;
fig. 4 is a schematic view of another splicing manner adopted by two turbulent flow type liquid mixing structures in the first embodiment of the present invention;
fig. 5 is a schematic structural diagram of a third embodiment of the present invention;
fig. 6 is a schematic diagram of the splicing use of two turbulent flow type liquid mixing structures in the third embodiment of the present invention;
fig. 7 is a schematic structural diagram of a fourth embodiment of the present invention;
fig. 8 is a schematic diagram of the splicing of two turbulent flow type liquid mixing structures in the fourth embodiment of the present invention.
Wherein, the technical characteristics that each reference numeral refers to are as follows:
1. a mixing tube; 101. a liquid inlet; 102. a liquid outlet; 103. a connection port; 1031. a plug-in part; 2. a turbulent flow liquid mixing part; 3. filtering with a screen; 301. a bottom; 302. a side portion; 4. a sleeve; 5. a switch; 6. a sealing cover; 7. a connecting sleeve.
Detailed Description
In order to make the objects, technical solutions and advantages of the present invention more apparent, the present invention is further described in detail with reference to the following embodiments, but the scope of the present invention is not limited to the following specific embodiments.
Example one
Referring to fig. 1, fig. 2 and fig. 3, the present embodiment discloses a turbulent flow type liquid mixing structure, including a mixing tube 1, where the mixing tube 1 is provided with a liquid inlet 101 and a liquid outlet 102, the mixing tube 1 is cylindrical, and two ends of the mixing tube 1 are closed, the mixing tube 1 is cylindrical or prismatic, and the mixing tube 1 is made into a straight tube or a bent tube according to actual use requirements, and in this embodiment, the mixing tube 1 is a cylindrical straight tube;
the mixing tube can be a plastic tube, a metal tube, a ceramic tube or a glass tube;
the liquid inlet 101 and the liquid outlet 102 are respectively arranged at two ends of the mixing tube 1, and the liquid inlet 101 and the liquid outlet 102 can be arranged at the end or the side wall of the mixing tube 1, in this embodiment, the liquid inlet 101 and the liquid outlet 102 are arranged on the side wall of the mixing tube 1, the liquid inlet 101 and the liquid outlet 102 are positioned in the same longitudinal section and are respectively positioned at two sides of the mixing tube 1, and the liquid inlet directions are parallel to each other and have the same direction;
referring to fig. 1, a turbulent flow liquid mixing part 2 is further arranged in the tube cavity of the mixing tube 1, the turbulent flow liquid mixing part 2 is arranged in a plurality of numbers, and through-flow gaps are formed among the turbulent flow liquid mixing parts 2.
The arrangement of the turbulent mixing parts 2 can be regular or irregular, and the through-flow gaps can be the same or different.
Referring to fig. 1, the particle diameter D of the turbulent fluid mixing member 2 is larger than both the fluid inlet 101 and the fluid outlet 102, and when the turbulent fluid mixing member 2 has an irregular shape, the particle diameter D of the turbulent fluid mixing member 2 is the minimum width dimension thereof.
The particle diameters D of the turbulent flow liquid mixing pieces 2 are the same or different, in the embodiment, the particle diameters D of the turbulent flow liquid mixing pieces 2 are the same, and the turbulent flow liquid mixing pieces 2 are regularly arranged layer by layer from bottom to top.
Referring to fig. 1 and 2, the mixing tube 1 is provided with a filter screen 3 at the liquid inlet 101 and the liquid outlet 102, and the aperture of the filter screen 3 is smaller than the particle diameter D of the turbulent flow mixing element 2, in this embodiment, the filter screen 3 includes a bottom portion 301 and a side portion 302 fixed to the bottom portion 301, the bottom portion 301 and the side portion 302 are provided with a filter screen 3 aperture, and the side portion 302 is circular and the side portion 302 is fixed to the inner diameter of the mixing tube 1.
The turbulent flow liquid mixing piece 2 is one or a combination of a plurality of spheres, cylinders, prisms, cones, pyramids and ellipsoids.
In this embodiment, vortex liquid mixing part 2 is the spheroid, and the spheroidal surface is smooth, and in other embodiments, the spheroidal surface can set up to be coarse, perhaps sets up arch, pit on spheroidal surface to increase choked flow, vortex effect, and then increase the effect of mixing liquid.
In order to be suitable for the production of chlorine-containing disinfectant fluid, the filter net 3 is a polyethylene net in this embodiment.
The turbulent flow liquid mixing part 2 is one or a combination of glass beads, ceramic beads and polyethylene beads.
Referring to fig. 3, two turbulent liquid mixing structures can be used in combination to connect the inlet 101 and outlet 102 on two different mixing tubes 1 by a sleeve 4.
Referring to fig. 3, when the two turbulent flow type liquid mixing structures are connected, the two turbulent flow type liquid mixing structures may be arranged to be parallel to each other, or one of the turbulent flow type liquid mixing structures may be arranged upright (i.e. the liquid inlet is located below and the liquid outlet is located above), and the other turbulent flow type liquid mixing structure is arranged upside down (refer to fig. 4).
The utility model discloses use of embodiment:
when mixing liquid, two or more than two kinds of liquid to be mixed are added into the tube cavity of the mixing tube 1 through the liquid inlet 101, so that the liquid flows from the liquid inlet 101 to the liquid outlet 102, and if the added liquid can not flow independently, the liquid can be pressurized.
In the process of flowing liquid in the tube cavity, the turbulent flow liquid mixing part 2 blocks the flowing of the liquid and can only flow from the through-flow gap of the turbulent flow liquid mixing part 2, so that liquid flows are separated and intersected to generate the effects of flow resistance and turbulent flow, the effect of liquid mixing is further achieved, and the uniformly mixed liquid is obtained from the liquid outlet 102.
Example two
The present embodiment discloses another turbulent flow type liquid mixing structure, and based on the first embodiment, the present embodiment is different from the first embodiment in that:
a plurality of vortex mixes liquid spare fixed connection, forms a vortex structure, and a plurality of vortex mixes liquid spare and can also fix through setting up recess, bellied cooperation structure like bolt, screw bolt through the connecting piece, can also make a plurality of vortex mix liquid spare integrated into one piece.
EXAMPLE III
Referring to fig. 5 and fig. 6, the present embodiment discloses another turbulent flow type liquid mixing structure, and based on the above embodiment, the present embodiment is different from the above embodiment in that:
the liquid inlet 101 and the liquid outlet 102 are both provided with a switch 5, two end portions of the mixing tube 1 are respectively provided with a connection port 103, and the connection port 103 is provided with a sealing cover 6.
When in use, the liquid inlet 101 and the liquid outlet 102 are selected as appropriate according to the requirement for liquid inlet and liquid outlet.
Example four
Referring to fig. 7, the present embodiment discloses another turbulent flow type liquid mixing structure, and based on the above embodiment, the present embodiment is different from the above embodiment in that:
referring to fig. 7 and 8, on the same mixing tube 1, a plug part 1031 extends from the connection port 103 at one end, the plug part 1031 is matched with the connection port 103 at the other end, and the plug part 1031 can be plugged or screwed into the connection port 103 at the other end;
when the connection is carried out in a screw connection mode, external threads can be arranged outside the insertion part, internal threads are arranged in the connecting end part, and the connection is carried out in a matched mode through the external threads and the internal threads.
When the two turbulent flow type liquid mixing structures are spliced, the splicing part 1031 of one mixing tube 1 is spliced in the connecting port 103 of the other mixing tube 1, so that the splicing is realized.
Variations and modifications to the above-described embodiments may occur to those skilled in the art, in light of the above teachings and teachings. Therefore, the present invention is not limited to the specific embodiments disclosed and described above, and some modifications and changes to the present invention should fall within the protection scope of the claims of the present invention. In addition, although specific terms are used in the specification, the terms are used for convenience of description and do not limit the utility model in any way.
Claims (10)
1. The utility model provides a vortex formula liquid mixed structure, includes hybrid tube (1), hybrid tube (1) is provided with inlet (101) and liquid outlet (102), its characterized in that, hybrid tube (1) is the column, and both ends are sealed, inlet (101), liquid outlet (102) set up respectively the both ends of hybrid tube (1), still be provided with vortex and mix liquid spare (2) in the lumen of hybrid tube (1), vortex mixes liquid spare (2) and sets up a plurality ofly, and is a plurality of there is the through-flow clearance between vortex mixes liquid spare (2).
2. The turbulent flow liquid mixing structure of claim 1, wherein the turbulent flow liquid mixing member (2) has a larger particle size D than both the liquid inlet (101) and the liquid outlet (102).
3. The turbulent flow liquid mixing structure according to claim 1 or 2, wherein the particle diameters D of the respective turbulent flow liquid mixing members (2) are the same or different in size.
4. The turbulent flow type liquid mixing structure of claim 1 or 2, wherein a filter screen (3) is arranged at each of the liquid inlet (101) and the liquid outlet (102) in the mixing tube (1), and the aperture of the mesh of the filter screen (3) is smaller than the particle diameter D of the turbulent flow type liquid mixing part (2).
5. The turbulent flow type liquid mixing structure according to claim 1 or 2, wherein a plurality of turbulent flow type liquid mixing members (2) are fixedly connected to form a turbulent flow structure.
6. The turbulent fluid mixing structure according to claim 1 or 2, wherein the turbulent fluid mixing member (2) is one or more of a sphere, a cylinder, a prism, a cone, a pyramid, and an ellipsoid.
7. Turbulent flow liquid mixing structure according to claim 4, characterized in that the sieve (3) is a polyethylene mesh.
8. The turbulent fluid mixing structure as claimed in claim 6, wherein the turbulent fluid mixing member (2) is a combination of one or more of glass beads, ceramic beads and polyethylene beads.
9. The turbulent flow type liquid mixing structure of claim 1, 7 or 8, wherein the liquid inlet (101) and the liquid outlet (102) are provided with switches (5), the two ends of the mixing tube (1) are respectively provided with a connection port (103), the connection port (103) is provided with a sealing cover (6), and the two turbulent flow type liquid mixing structures connect the connection ports (103) on two different mixing tubes (1) through a connection sleeve (7).
10. The turbulent flow type liquid mixing structure of claim 9, wherein a plug part (1031) extends from the connection port (103) at one end of the mixing tube (1), the plug part (1031) is matched with the connection port (103) at the other end, and the plug part (1031) is inserted or screwed into the connection port (103) at the other end.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020835335.6U CN212348373U (en) | 2020-05-18 | 2020-05-18 | Turbulent flow type liquid mixing structure |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020835335.6U CN212348373U (en) | 2020-05-18 | 2020-05-18 | Turbulent flow type liquid mixing structure |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN212348373U true CN212348373U (en) | 2021-01-15 |
Family
ID=74150796
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202020835335.6U Active CN212348373U (en) | 2020-05-18 | 2020-05-18 | Turbulent flow type liquid mixing structure |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN212348373U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113670974A (en) * | 2021-09-18 | 2021-11-19 | 天津大学合肥创新发展研究院 | Supercritical CO2Mixed working medium heat exchange experimental system |
-
2020
- 2020-05-18 CN CN202020835335.6U patent/CN212348373U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113670974A (en) * | 2021-09-18 | 2021-11-19 | 天津大学合肥创新发展研究院 | Supercritical CO2Mixed working medium heat exchange experimental system |
| CN113670974B (en) * | 2021-09-18 | 2023-10-31 | 天津大学合肥创新发展研究院 | Supercritical CO 2 Mixed working medium heat exchange experiment system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CA2167823A1 (en) | An Apparatus and a Method for Mixing or Dissolving a Particulate Solid in a Liquid | |
| KR100916709B1 (en) | Powerless Mixing Apparatus Within Pipe | |
| CN212348373U (en) | Turbulent flow type liquid mixing structure | |
| CN208054995U (en) | A kind of dosing on-line dilution device | |
| CN101648117B (en) | Microscopic bubble or drop generating device | |
| CN208320516U (en) | A kind of pipe-line mixer | |
| CN209406089U (en) | A kind of water-gas mixer that tracheae extends | |
| CN201844155U (en) | Pipeline dosing device | |
| CN205084643U (en) | Static mixer | |
| CN212559588U (en) | Slow-release medicament proportional dosing box | |
| CN203342661U (en) | Slurry medicine rotational flow mixing device for sewage treatment | |
| US20130032519A1 (en) | Biological sewage treatment device | |
| CN212549075U (en) | Small-size chlorine-containing disinfectant production facility | |
| CN208213071U (en) | Pipe-line mixer | |
| CN207749582U (en) | Anti pollution water tank | |
| CN207222158U (en) | Turbulent flow chemicals dosing plant on preparation equipment | |
| CN206445951U (en) | A kind of uniform humidifying agitator | |
| CN102172485B (en) | Spraying-type fluid mixing device | |
| CN111467990A (en) | Small-size chlorine-containing disinfectant production facility | |
| CN212549074U (en) | Sleeve type liquid mixing structure | |
| CN207095622U (en) | Plunger type resistance orifice plate | |
| CN216103932U (en) | Material circulation basin | |
| CN205995289U (en) | A kind of venturi mixer of two-way injection | |
| CN209352580U (en) | A kind of pneumatic stirring chemicals dosing plant | |
| CN211963772U (en) | High-pressure static mixer |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |