CN114229955A - Unpowered cyclone type liquid mixing method and unpowered cyclone type liquid mixer - Google Patents
Unpowered cyclone type liquid mixing method and unpowered cyclone type liquid mixer Download PDFInfo
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- CN114229955A CN114229955A CN202111520515.0A CN202111520515A CN114229955A CN 114229955 A CN114229955 A CN 114229955A CN 202111520515 A CN202111520515 A CN 202111520515A CN 114229955 A CN114229955 A CN 114229955A
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- 239000007788 liquid Substances 0.000 title claims abstract description 100
- 238000000034 method Methods 0.000 title claims abstract description 25
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 208
- 238000005265 energy consumption Methods 0.000 abstract description 2
- 238000003756 stirring Methods 0.000 description 10
- 230000000694 effects Effects 0.000 description 9
- 230000015572 biosynthetic process Effects 0.000 description 3
- 239000003814 drug Substances 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000003116 impacting effect Effects 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000001112 coagulating effect Effects 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5281—Installations for water purification using chemical agents
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/38—Treatment of water, waste water, or sewage by centrifugal separation
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/02—Fluid flow conditions
- C02F2301/024—Turbulent
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/02—Fluid flow conditions
- C02F2301/026—Spiral, helicoidal, radial
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- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
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Abstract
The invention aims to solve the technical problems of more energy consumption and insufficient mixing in liquid mixing in the prior art, and provides an unpowered rotational flow type liquid mixing method and an unpowered rotational flow type liquid mixer, wherein the unpowered rotational flow type liquid mixing method changes the flowing direction of liquid in a flowing plane and enables the liquid to form a fall head so as to accelerate the flow speed of the liquid and form rotational flow with a turbulent flow state, so that the liquid is fully mixed; the unpowered rotational flow liquid mixer comprises a water inlet pipe, a rotational flow generating container and a water outlet pipe, wherein the rotational flow generating container is provided with a water inlet and a water outlet, the water inlet of the rotational flow generating container is hermetically communicated with the water inlet pipe, the water outlet of the rotational flow generating container is hermetically communicated with the water outlet pipe, the water outlet pipe is vertically arranged, and the water outlet pipe is rotatably connected with an impeller; by adopting the method and the structure of the invention, the water flow can be mixed without an additional power source, and the energy required by the mixed liquid during water treatment can be greatly reduced.
Description
Technical Field
The invention relates to the field of water treatment, in particular to an unpowered cyclone type liquid mixing method and an unpowered cyclone liquid mixer.
Background
In water treatment, it is sometimes necessary to mix different water bodies or water bodies with chemicals, for example, in sewage treatment, it is necessary to mix sewage and coagulation chemicals. In order to fully mix liquid and medicament in order to reach better effect of coagulating, generally adopt special mixing stirring device to stir, current mixing stirring device utilizes motor drive stirring vane stirring liquid to mix generally, and water treatment all needs to go on constantly, need to use the motor to drive stirring vane continuously and rotate, therefore the energy of consumption is more. Because of adopting single mixed mode, in impeller stirring process, because the direction of impeller is always as one, stirring time is not enough, and the liquid and the medicament can not be fully mixed.
Disclosure of Invention
The invention aims to provide an unpowered cyclone type liquid mixing method and an unpowered cyclone liquid mixer, aiming at the technical problems of more energy consumption and insufficient mixing in the liquid mixing process in the prior art.
The technical purpose of the invention is realized by the following technical scheme:
the unpowered spiral-flow type liquid mixing method changes the flow direction of liquid in the flow plane and makes the liquid form head difference to speed the flow speed of the liquid and form spiral flow with turbulent flow state, so that the liquid is fully mixed.
Preferably, the liquid to be mixed flows into the container, the flowing direction is changed under the action of the inner wall of the container, the liquid enters a water outlet arranged at the bottom of the container and flows out along a water outlet pipe vertically arranged to generate a fall, and a rotational flow with a turbulent flow state is formed at the water outlet.
Preferably, the water flow enters the water outlet to form a rotational flow, the rotational flow pushes an impeller arranged in the water outlet or the water outlet pipe, the rotational flow pushes the impeller to rotate, the spiral degree of the rotational flow is improved to be changed into a spiral flow, and the mixed liquid is mixed again.
Preferably, the liquid to be mixed enters the container along the tangential direction, a rotational flow is formed in the container, a water outlet at the bottom of the container is opposite to the center of the rotational flow, the impeller at the water outlet is pushed to rotate when the rotational flow flows out of the water outlet, and the water flow speed of the liquid to be mixed is 1.7-2.5 m/s.
The utility model provides an unpowered whirl liquid mixer, includes inlet tube, whirl generating container and outlet pipe, whirl generating container is equipped with water inlet and delivery port, and whirl generating container's delivery port sets up on its diapire, and whirl generating container's water inlet sets up on its lateral wall, and whirl generating container's water inlet and the sealed intercommunication of inlet tube, whirl generating container's delivery port and the sealed intercommunication of outlet pipe, the vertical setting of outlet pipe, outlet pipe department rotate and are connected with the impeller, the axis of impeller with the axis coincidence of outlet pipe, the impeller setting is in the outlet pipe, or the impeller part is located the outlet, partly is higher than the delivery port, or the impeller is higher than the delivery port setting and the impeller is relative with the water inlet.
Preferably, the central line of the water outlet is perpendicular to but not intersected with the central line of the water inlet, the central line of the water outlet and the central line of the water inlet are arranged in a staggered manner, and the central line of the water inlet is higher than the central line of the water outlet.
Preferably, the water outlet is positioned at the central position of the bottom wall of the rotational flow generating container.
Preferably, the swirl generating vessel is a cylindrical vessel.
Preferably, the inner side wall of the swirl generating container is arranged along a spiral line.
Preferably, the water inlet of the swirl generating container is arranged tangentially to the side wall thereof.
The invention has the following beneficial effects:
in the method, the flow direction and the fall of the liquid to be mixed are changed, so that the flow speed of the liquid is accelerated, the molecules in the liquid are changed into a turbulent flow state from a downstream state, the flow direction of the liquid is diversified, a plurality of water flows in different directions are formed, mutual collision is generated among the water flows, the liquid medicine molecules to be mixed are fully fused in the water, the mixing of the mixed liquid can be realized under the condition of no power, meanwhile, the flow direction of the mixed liquid is changed in a flow plane, the fall is generated, the water flow can be changed into the rotational flow, the water flow is changed into the rotational flow with the turbulent flow state, the direction of the water flow is further changed, the collision is generated among the water molecules again, and the second obvious stirring is formed, so that the mixing is more uniform. The impeller is installed in the container and rotates under the pushing of the rotational flow, the helical degree of the rotational flow is enhanced, the helical flow is formed in the container, the mixed liquid is mixed again, the bottom of the container is provided with a water outlet, and the mixed flow flows out from the water outlet.
Therefore, the method of the invention utilizes the liquid to be mixed to enter the container and flow out from the bottom of the container, the water flow changes the direction under the action of the container and then flows out from the water outlet at the bottom of the container, thereby increasing the flow velocity to generate the water flow drop, forming the rotational flow with turbulent flow state under the action of the flow velocity increase and the water flow drop, and increasing the flow velocity of the water flow and forming the rotational flow by the flow velocity of the water flow and the furling action of the container without arranging an additional power device, thereby saving the power and reducing the loss of energy.
Meanwhile, the liquid fall is utilized to push one or more rotatably arranged impellers to rotate, the impellers are pushed to rotate through naturally generated rotational flow, the helicity of the rotational flow is enhanced to form a helical flow to mix liquid, the relative positions of all molecules in the liquid are further changed, high mixing between the liquid and solid, and the liquid is realized, in the process that the liquid impacts the impellers to rotate, the impellers break up the water flow impacting the blades of the impellers, a part of the dispersed water flow can impact the water flow flowing to the impellers, and a part of the water flow can impact a container, so that the change amplitude and the change speed of the relative positions of all molecules in the liquid are improved, and a good liquid mixing effect can be realized Or the energy required for liquids and solids.
The unpowered rotational flow liquid mixer comprises a water inlet pipe, a rotational flow generating container and a water outlet pipe, wherein a water outlet of the rotational flow generating container is arranged on the bottom wall of the rotational flow generating container, a water inlet of the rotational flow generating container is arranged on the side wall of the rotational flow generating container, and the center line of the water outlet is perpendicular to the center line of the water inlet, so that inlet water can horizontally enter the rotational flow generating container and vertically and downwards flow out, rotational flow can be formed at the water outlet of the rotational flow generating container by water flow, an impeller is rotationally connected in the water outlet pipe or the rotational flow generating container, the impeller is pushed to rotate by the rotational flow to form helical flow, the liquid is mixed by purely utilizing the flowing kinetic energy of the water flow, no additional power source is needed, and the energy needed by the mixed liquid during water treatment can be greatly reduced.
Drawings
FIG. 1 is a schematic structural view of embodiment 1 of the present invention;
FIG. 2 is a schematic structural view of example 1 of the present invention with the water inlet pipe and the top cover of the unpowered vortex generation vessel removed;
FIG. 3 is a schematic structural view of embodiment 2 of the present invention with the water inlet pipe and the top wall of the unpowered vortex generation vessel removed;
FIG. 4 is a schematic structural view of embodiment 3 of the invention with the water inlet pipe and the top wall of the unpowered vortex generation vessel removed;
fig. 5 is a schematic structural diagram of an embodiment of the unpowered vortex generator when one side of the impeller is opposite to the water inlet.
Reference number legend, 10, water inlet pipe; 20. a water outlet pipe; 30. a swirl flow generating vessel; 31. a water inlet; 32. a water outlet; 40. an impeller; 50. and (4) a bracket.
Detailed Description
The present invention will be described in further detail with reference to the accompanying drawings. In which like parts are designated by like reference numerals.
A non-power rotational flow type liquid mixing method changes the flowing direction of liquid and forms a fall head to change the liquid from a downstream state to a turbulent state to realize the primary mixing of mixed liquid, changes the flowing direction of the liquid and forms the fall head by the following method, a turning structure, such as a corner or an open arc diversion structure, is arranged on a closed or open pipeline to guide the flowing direction of the liquid to change to form the turbulent flow, a water outlet is arranged at the bottom of the pipeline to ensure that water flows out from the water outlet to form the fall head, and the water flows naturally form rotational flow when entering the water outlet. The liquid to be mixed flows into the container quickly, the flow direction of the liquid is blocked by the container, the liquid flows out from a water outlet at the bottom of the container to form turbulence and fall, and the liquid forms rotational flow when entering the water outlet. The better method is that on the basis of the method, the liquid is directly pushed or the rotational flow formed by the liquid is used for pushing the impeller 40 which is rotationally arranged at the water outlet of the container or in the water outlet pipe to rotate, the helicity of the rotational flow is enhanced to enable the rotational flow to be spiral flow, the spiral flow further mixes the liquid, the relative position of each molecule in the liquid in the spiral flow can be changed, thereby the liquid is fully mixed, in the process that the liquid pushes the impeller 40 to rotate, the impeller 40 breaks up the water flow impacting the blade of the impeller, a part of the dispersed water flow and the subsequent water flow flowing to the impeller 40 mutually impact, a part of the water flow collides with the container, the change amplitude and the change speed of the relative position of each molecule in the liquid are improved, and the better liquid mixing effect can be realized, the method of the invention only utilizes the kinetic energy of the flowing of the water flow to mix the liquid, no extra power source is needed, and the energy required by the mixed liquid during water treatment can be greatly reduced.
The unpowered cyclone type liquid mixing method can be realized by adopting the unpowered cyclone liquid mixer with the following structure. As shown in fig. 1-4, the unpowered swirling liquid mixer includes a water inlet pipe 10, a swirling generating container 30, a water outlet pipe 20, and an impeller 40. The water inlet pipe 10 is horizontally arranged, the water outlet pipe 20 is vertically arranged, the central line of the water outlet 32 is perpendicular to the central line of the water inlet 31 but not intersected with the central line of the water inlet 31, the central lines of the water inlet and the water outlet can be positioned in the same plane, or the central line of the water inlet is higher than the central line of the water outlet, and the central line of the water inlet is higher than the central line of the water outlet, so that the turbulent flow of the rotational flow can be increased. The water inlet 31 of the rotational flow generating container 30 is communicated with the water inlet pipe 10 in a sealing way, and the water outlet 32 of the unpowered rotational flow generating container is communicated with the water outlet pipe 20 in a sealing way. Water flows in from the side direction of the rotational flow generating container 30, the direction of the water flow is changed under the action of the rotational flow generator, water flows out from the water outlet downwards under the action of gravity, the flow speed of the water flow is high, the general flow speed is 1.7-2.5 m/s, the water flow can form turbulent flow in the rotational flow generating container 30, drop is formed in the water outlet pipe, and rotational flow is formed at the water outlet. As shown in fig. 3, the swirling flow generating container 30 is preferably a cylindrical container or the inner side wall of the container shown in fig. 1 is disposed along a spiral line, and the water outlet 32 is preferably disposed at the center of the bottom wall of the swirling flow generating container 30, so that water can flow out from the water outlet 32 more smoothly, and swirling flow formation at the water outlet 32 is facilitated, and when the swirling flow generating container 30 forms swirling flow, water flow can occupy the space in the swirling flow generating container 30 more sufficiently, thereby reducing dead angle of water flow and facilitating swirling flow formation. Of course, the swirling flow generating container 30 may be formed in other shapes such as a square shape and a triangular shape, as long as the flow direction of the water is changed after the water enters the container. As shown in fig. 2, the center line of the water outlet 32 does not intersect the center line of the water inlet 31, preventing the inflow water from directly flowing out of the water outlet 32, and contributing to the formation of a swirling flow in the swirling flow generating container 30. Preferably, the water inlet 31 of the rotational flow generating container 30 is arranged along the tangential direction of the side wall of the rotational flow generating container 30, and the water outlet is positioned at the center of the bottom wall of the rotational flow generator, so that the center of the rotational flow coincides with the center of the water outlet, and water flows out from the water outlet more smoothly, thereby being more beneficial to forming rotational flow at the water outlet. As shown in fig. 1-5, the impeller 40 is disposed at the water outlet, and may be located in the water outlet, or a part of the impeller may be located in the water outlet, and another part of the impeller may be located outside the water outlet, so as to improve the water mixing effect, or may be disposed completely higher than the water outlet, as shown in fig. 5, and one side of the impeller is opposite to the water inlet, so that the water flowing from the water inlet may directly impact the impeller. When water flows into the rotational flow generation container 30 from the water inlet pipe, under the blocking effect of the inner wall of the rotational flow generation container 30, the water flow changes the direction to revolve, when the water flows out from the water outlet 32, the rotational flow is formed at the water outlet 32, the rotational flow pushes the impeller 40 to rotate, the rotation of the impeller further increases the revolving speed of the rotational flow and further increases the helicity of the rotational flow to form the helical flow, the liquid molecules in the rotational flow and the helical flow are relatively displaced to realize the stirring and mixing of the liquid, the water stirred by the impeller can be distributed in the whole rotational flow generation container 30 to be collided with the water flow or generate multiple times of collision with the inner wall of the rotational flow generation container 30 under the centrifugal force effect of the helical flow, therefore, the activity of the water molecules is enhanced, the liquid mixing effect is better, and the liquid mixing is more sufficient.
The rotating surface of the impeller 40 and the bottom surface of the rotational flow generation container 30 can be arranged in parallel, and can also be inclined at a certain angle, the impeller 40 is just opposite to the water outlet or the edge part of the impeller positioned at the water outlet, as long as the rotational flow formed by the rotational flow generation container 30 can push the impeller 40 to rotate, the impeller rotates under the pushing action of the rotational flow, water molecules meet with the water flow outside the center of the rotational flow in the remote distribution under the action of centrifugal force, the activity of the water molecules is increased, and the mixing effect is better. As shown in fig. 1-4, the rotation axis of the impeller 40 is preferably vertically arranged, and since the axis of the rotational flow is vertical, the rotational flow needs less energy to push the vertically arranged impeller 40 to rotate, and the rotation direction of the impeller 40 is consistent with the pushing direction of the water flow, so that the kinetic energy loss of the water flow is small. In addition, since the axis of the rotational flow formed in the rotational flow generating container 30 is coaxial with the rotational flow generating container, the impeller 40 is preferably coaxial with the water outlet pipe 20, so that kinetic energy generated by the rotational flow is converted into kinetic energy of the rotation of the impeller 40 with a high conversion rate, and the utilization rate of water energy is highest.
Specifically, the method comprises the following steps: example 1, as shown in fig. 1 and 2, the swirl generating vessel 30 is a cylindrical vessel having a sidewall arranged along a spiral line, and the water inlet pipe 10 is arranged in a tangential direction of the sidewall of the swirl generating vessel 30. The outlet 32 of the swirl generating container 30 is located on the bottom wall thereof and the centre line of the outlet is coaxial with the side wall of the swirl generating container. The impeller 40 is arranged in the water outlet pipe 20, two supports 50 are fixedly arranged in the water outlet pipe 20, the supports 50 are respectively positioned at two ends of a rotating shaft of the impeller 40, and the rotating shaft of the impeller 40 is respectively connected with the two supports 50.
Example 2, as shown in fig. 3, differs from example 1 in that the swirl generation container 30 is cylindrical, the axis of the water inlet pipe 10 perpendicularly intersects with the axis of the swirl generation container 30, and the water outlet 32 of the swirl generation container 30 is located at the center of the bottom wall thereof and is coaxial with the swirl generation container 30.
Embodiment 3, as shown in fig. 4, differs from embodiment 1 in that the impeller 40 is disposed obliquely, and both ends of the impeller 40 are respectively connected to the pipe walls of the water outlet pipe 20.
The specific examples are merely illustrative of the invention and are not intended to be limiting.
Claims (10)
1. A unpowered spiral-flow type liquid mixing method is characterized in that: the flow direction of the liquid in the flow plane is changed, the liquid forms a fall head, so that the flow speed of the liquid is accelerated, and a rotational flow with a turbulent flow state is formed, so that the liquid is fully mixed.
2. The unpowered cyclonic liquid mixing method of claim 1, wherein: the liquid to be mixed flows into the container, the flowing direction is changed under the action of the inner wall of the container, the liquid enters a water outlet arranged at the bottom of the container and flows out along a water outlet pipe vertically arranged to generate a fall, and a rotational flow with a turbulent flow state is formed at the water outlet.
3. The unpowered cyclonic liquid mixing method of claim 1 or 2, wherein: the water flow enters the water outlet to form rotational flow, the rotational flow pushes the impeller arranged in the water outlet or the water outlet pipe, the rotational flow pushes the impeller to rotate, the spiral degree of the rotational flow is improved to be changed into spiral flow, and the mixed liquid is mixed again.
4. The unpowered cyclonic liquid mixing method of claim 1, wherein: the liquid to be mixed enters the container along the tangential direction, a rotational flow is formed in the container, a water outlet at the bottom of the container is opposite to the center of the rotational flow, the impeller at the water outlet is pushed to rotate when the rotational flow flows out of the water outlet, and the water flow speed of the liquid to be mixed is 1.7-2.5 m/s.
5. An unpowered whirl liquid mixer which characterized in that: comprises a water inlet pipe (10), a rotational flow generating container (30) and a water outlet pipe (20), the cyclone generating container (30) is provided with a water inlet (31) and a water outlet (32), the water outlet (32) of the cyclone generating container (30) is arranged on the bottom wall of the cyclone generating container, the water inlet (31) of the cyclone generating container (30) is arranged on the side wall of the cyclone generating container, the water inlet (31) of the cyclone generating container (30) is hermetically communicated with the water inlet pipe (10), the water outlet (32) of the cyclone generating container (30) is hermetically communicated with the water outlet pipe (20), the water outlet pipe (20) is vertically arranged, the water outlet pipe (20) is rotatably connected with an impeller (40), the axial line of the impeller (40) is superposed with the axial line of the water outlet pipe (20), the impeller is arranged in the water outlet, or the impeller is partially positioned in the water outlet and partially higher than the water outlet, or the impeller is arranged higher than the water outlet and is opposite to the water inlet.
6. The unpowered cyclonic liquid mixer of claim 5 wherein: the central line of the water outlet (32) is vertical to the central line of the water inlet (31) but does not intersect with the central line of the water outlet, the central line of the water outlet and the central line of the water inlet are staggered, and the central line of the water inlet is higher than the central line of the water outlet.
7. The unpowered cyclonic liquid mixer of claim 5 wherein: the water outlet (32) is positioned at the central position of the bottom wall of the rotational flow generating container (30).
8. The unpowered cyclonic liquid mixer of claim 5 wherein: the swirl flow generating container (30) is a cylindrical container.
9. The unpowered cyclonic liquid mixer of claim 5 wherein: the inner side wall of the rotational flow generating container (30) is arranged along a spiral line.
10. The unpowered cyclonic liquid mixer of claim 9 wherein: the water inlet (31) of the rotational flow generating container (30) is arranged along the tangential direction of the side wall.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202111520515.0A CN114229955A (en) | 2021-12-13 | 2021-12-13 | Unpowered cyclone type liquid mixing method and unpowered cyclone type liquid mixer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202111520515.0A CN114229955A (en) | 2021-12-13 | 2021-12-13 | Unpowered cyclone type liquid mixing method and unpowered cyclone type liquid mixer |
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| CN114229955A true CN114229955A (en) | 2022-03-25 |
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| CN202111520515.0A Pending CN114229955A (en) | 2021-12-13 | 2021-12-13 | Unpowered cyclone type liquid mixing method and unpowered cyclone type liquid mixer |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114939375A (en) * | 2022-06-07 | 2022-08-26 | 健帆生物科技集团股份有限公司 | Liquid preparation method and liquid preparation device |
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| KR20100039513A (en) * | 2008-10-08 | 2010-04-16 | 한국수자원공사 | Mixing apparatus using a rotary flux |
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| CN105347449A (en) * | 2015-11-30 | 2016-02-24 | 无锡工源机械有限公司 | Cyclone reactor |
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2021
- 2021-12-13 CN CN202111520515.0A patent/CN114229955A/en active Pending
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| Publication number | Priority date | Publication date | Assignee | Title |
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| KR20100039513A (en) * | 2008-10-08 | 2010-04-16 | 한국수자원공사 | Mixing apparatus using a rotary flux |
| CN101921014A (en) * | 2009-06-12 | 2010-12-22 | 帕洛阿尔托研究中心公司 | The mixing screw that is used for floc conditioning |
| KR101558822B1 (en) * | 2014-12-23 | 2015-10-08 | 장윤근 | Turbulence flow using chemical rapid blending device |
| CN105347449A (en) * | 2015-11-30 | 2016-02-24 | 无锡工源机械有限公司 | Cyclone reactor |
| CN211521706U (en) * | 2019-12-27 | 2020-09-18 | 吉林省拓达环保设备工程有限公司 | Different direction multi-swirl mixer |
| CN112843878A (en) * | 2021-03-05 | 2021-05-28 | 江苏威乐环保科技有限公司 | Archimedes spiral runner type cyclone separation well |
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| CN114939375A (en) * | 2022-06-07 | 2022-08-26 | 健帆生物科技集团股份有限公司 | Liquid preparation method and liquid preparation device |
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