CN217093250U - Mixing device with pressure flow compensation - Google Patents
Mixing device with pressure flow compensation Download PDFInfo
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- CN217093250U CN217093250U CN202123131874.5U CN202123131874U CN217093250U CN 217093250 U CN217093250 U CN 217093250U CN 202123131874 U CN202123131874 U CN 202123131874U CN 217093250 U CN217093250 U CN 217093250U
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Abstract
The utility model provides a mixing arrangement with pressure flow compensation relates to the supporting device of fracturing unit, the novel nipple rectifier comprises a cylindrical shel, be equipped with agitating unit in the barrel, the barrel includes outer barrel and interior barrel, be equipped with the feed liquor cavity between the lateral wall of outer barrel and interior barrel, outer barrel is equipped with the feed liquor pipe, feed liquor pipe and feed liquor cavity intercommunication, the inner wall of barrel is equipped with a plurality of efflux pipes including, efflux pipe and feed liquor cavity intercommunication are equipped with the drain pipe in the bottom of barrel, the drain pipe communicates with the bottom of interior barrel, still be equipped with at least one pressure flow compensation valve, the import and the feed liquor cavity intercommunication of pressure flow compensation valve, the export of pressure flow compensation valve is located the inner tube internally. Through adopting stirring and fluidic mode, ensure solid-liquid misce bene, including the barrel set up pressure flow compensation valve, when low flow, pressure flow compensation valve closed to ensure that the efflux flow is enough, avoid leading to mixing inhomogeneous or pressure to make the drain pipe sand setting because of the flow of efflux pipe is not enough.
Description
Technical Field
The utility model relates to a supporting equipment field of underground fracturing unit, especially a mixing arrangement with pressure flow compensation.
Background
In the fracturing construction process of oil and gas wells, the main function of the sand mixing equipment is to realize the mixing and conveying of the propping agent and the fracturing fluid, and 6-20m has been formed after years of development 3 A/min series product. The performance of the sand mixing equipment is not only affected by the centrifugal pump, but also depends on the performance of the mixing device, mainly including the mixing uniformity of the mixing device and the outlet fluidity, wherein the outlet fluidity directly affects the discharge performance of the centrifugal pump.
Chinese patent document CN 207446086U describes an injection type mixing tank suitable for sand mixing equipment, which adopts a structure of stirring mixing and jet mixing, can reduce the mixing and stirring power, solve the problems of sand settling at the liquid outlet and incapability of emptying the liquid outlet, and improve the overall service performance of the mixing tank. The problems that the output mixing uniformity of the whole machine is different, the pressure fluctuation of equipment discharge is larger under the working condition of variable flow, the output flow of the whole machine is obviously reduced, the output pressure is lower under the working condition of large flow of the whole machine and the like exist.
SUMMERY OF THE UTILITY MODEL
The utility model aims to solve the technical problem that a mixing arrangement with pressure flow compensation is provided, can adapt to the operating mode under the different flows, make under the variable flow operating mode, also can ensure that discharge pressure is enough. Preferably, the solid-liquid mixing is ensured to be uniform.
In order to solve the technical problem, the utility model discloses the technical scheme who adopts is: the utility model provides a mixing arrangement with pressure flow compensation, the novel nipple rectifier comprises a cylindrical shel, be equipped with agitating unit in the barrel, the barrel includes outer barrel and interior barrel, be equipped with the feed liquor cavity between the lateral wall of outer barrel and interior barrel, outer barrel is equipped with the feed liquor pipe, feed liquor pipe and feed liquor cavity intercommunication, the inner wall of barrel is equipped with a plurality of efflux pipes including, efflux pipe and feed liquor cavity intercommunication, be equipped with the drain pipe in the bottom of barrel, the bottom intercommunication of drain pipe and interior barrel, still be equipped with at least one pressure flow compensation valve, the import and the feed liquor cavity intercommunication of pressure flow compensation valve, the export of pressure flow compensation valve is located the inner tube internally.
In a preferred embodiment, as shown in fig. 6, in the pressure-flow compensation valve, a valve core is connected to a spring, preferably, in this embodiment, the valve core is connected to a valve rod, and the valve rod is provided with a spring, so that the valve core can be opened only when liquid from the liquid inlet cavity has sufficient pressure;
in the preferred scheme, the liquid inlet pipe is communicated with a variable frequency pump, the variable frequency pump is provided with a low-flow working condition and a high-flow working condition, and the liquid inlet pressure of the high-flow working condition is greater than that of the low-flow working condition;
the pressure flow compensation valve is set to be closed under the working condition of low flow and opened under the working condition of high flow. With this structure, the output pressure is stabilized by the pressure-flow compensation valve.
In the preferred scheme, be equipped with the roof at the top of barrel, be equipped with into sand mouth on the roof, the inner wall of the interior barrel of advancing sand mouth below is equipped with the dispersion efflux pipe, the dispersion efflux pipe be equipped with a plurality of openings along the circumference, the horizontal projection position of the directional sand mouth of a plurality of openings.
In the preferred scheme, the jet pipes are divided into two rows from top to bottom, the upper row of jet pipes jet at the bottom of the inner cylinder downwards, and the lower row of jet pipes jet horizontally.
In the preferred scheme, the bottom of the inner cylinder body is arc-shaped, the top wall of the liquid outlet pipe is communicated with the inner cylinder body, and the liquid outlet pipe is led out from one side of the inner cylinder body;
the liquid inlet cavity is also communicated with one end of the liquid outlet auxiliary discharge jet pipe, and the other end of the liquid outlet auxiliary discharge jet pipe is communicated with the end head of the liquid outlet pipe and is used for flushing accumulated sand in the liquid outlet pipe;
the bottom of the inner cylinder body is also provided with a plurality of liquid outlet branch pipes which are communicated with the liquid outlet pipe.
In the preferred scheme, the axis of the liquid outlet pipe inclines upwards from the connecting end to the free end, and an included angle is formed between the axis of the liquid outlet pipe and the horizontal plane;
the included angle is 1-7 degrees.
In a preferable scheme, the stirring device is provided with a vertical shaft, the top end of the shaft is connected with the rotary driving device, and a plurality of groups of stirring blades are arranged on the part of the shaft, which is positioned in the inner cylinder body;
the inner wall of the inner cylinder body is also provided with a turbulent baffle;
the shaft is also provided with a sand guide plate which is of an inverted cone structure and is used for enabling sand to be far away from the shaft.
In the preferred scheme, the shaft is a hollow shaft tube, the end of the hollow shaft tube is connected with the movable connector, a shaft jet flow port is arranged at the position, located in the inner cylinder, of the hollow shaft tube, and the shaft jet flow port is communicated with the hollow shaft tube.
In the preferred scheme, a liquid level meter is arranged in the inner cylinder body;
the liquid outlet pipe is connected with a connecting pipe, the connecting pipe is horizontally arranged, and a plurality of pipeline jet pipes are arranged on the connecting pipe.
The utility model provides a mixing arrangement with pressure flow compensation through adopting stirring and fluidic mode, ensures solid-liquid misce bene, including the barrel set up pressure flow compensation valve, when the low discharge, pressure flow compensation valve closes to it is enough to ensure the efflux flow, avoids leading to mixing inhomogeneously or pressure messenger drain pipe sand setting because of the flow of efflux pipe is not enough. In the preferred scheme, a plurality of open-ended dispersion jet pipes are arranged below the sand inlet, so that the sand and the water are mixed more uniformly. The liquid outlet auxiliary discharge jet flow pipe and the liquid outlet branch pipe can improve the effects of auxiliary discharge, sand mixing and accumulated sand scouring in the liquid outlet pipe. In the matched scheme, the liquid outlet pipe is inclined upwards, so that liquid in the liquid outlet pipe has buffering effect, the mixing effect in the liquid outlet pipe is improved, the uniformity of solid and liquid is further ensured, and the solid is prevented from being directly discharged from the liquid outlet pipe. The structure of leading sand board, turbulent baffle and axle jet flow mouth that sets up can further improve the solid-liquid mixing effect, makes solid sand mix in agitating unit's high-efficient mixing area. The level gauge that sets up can improve mixing efficiency through liquid level control, also can avoid the overflow jar accident.
Drawings
The invention will be further explained with reference to the following figures and examples:
fig. 1 is a front view of the present invention.
Fig. 2 is a top view of the present invention.
Fig. 3 is a sectional view a-a of fig. 2.
Fig. 4 is a perspective view of the present invention.
Fig. 5 is a cross-sectional view of a preferred structure of the present invention.
Fig. 6 is a schematic structural diagram of the pressure-flow compensation valve of the present invention.
In the figure: the device comprises a rotary driving device 1, a liquid inlet pipe 2, a sand guide plate 3, a bottom plate 4, a liquid outlet pipe 5, a liquid outlet guide plate 6, a liquid discharge pipe 7, a liquid discharge valve 8, a dispersion jet pipe 9, an upper jet pipe 10, an outer cylinder 11, an inner cylinder 12, a top plate 13, a liquid level meter 14, a stirrer 15, a liquid discharge auxiliary jet pipe 16, a liquid outlet branch pipe 17, a turbulence baffle 18, a pressure flow compensation valve 19, a spring 191, a valve rod 192, a valve core 193, a lower jet pipe 20, a movable connector 21, a hollow shaft pipe 22, a transmission gear 23, a shaft jet port 24, a connecting pipe 25, a pipeline jet pipe 26, a liquid inlet cavity 27 and a sand inlet 28.
Detailed Description
Example 1:
as shown in fig. 1-4 and 6, a mixing device with pressure flow compensation comprises a barrel, wherein a stirring device is arranged in the barrel, the barrel comprises an outer barrel 11 and an inner barrel 12, and a liquid inlet cavity 27 is arranged between the side walls of the outer barrel 11 and the inner barrel 12. Preferably, the inlet chamber 27 is of a closed structure. The outer cylinder 11 is provided with a liquid inlet pipe 2, the liquid inlet pipe 2 is communicated with a liquid inlet cavity 27, and the inner cylinder 12The inner wall is equipped with a plurality of efflux pipes, and efflux pipe and feed liquor cavity 27 intercommunication are equipped with drain pipe 5 in the bottom of barrel, and drain pipe 5 and the bottom of interior barrel 12 intercommunication still are equipped with at least one pressure flow compensation valve 19, and the import and the feed liquor cavity 27 intercommunication of pressure flow compensation valve 19, the export of pressure flow compensation valve 19 are located interior barrel 12. With the structure, when the liquid inlet pipe is connected with a liquid pump, such as a centrifugal pump, the centrifugal pump is driven by a variable frequency motor, and the flow range is 10-20m 3 And/min. When frequency conversion control is adopted, the rotating speed of the centrifugal pump is reduced by 10 m 3 The output flow and pressure of liquid are reduced under the/min working condition, if the section of the passage is kept unchanged, the jet pressure of the jet pipe is reduced, so that the jet pressure is insufficient, the mixing effect is difficult to achieve, and the discharge pressure is also insufficient. When 20m is used 3 Under the/min working condition, the output pressure is increased, so that the working pressure fluctuation of the system is large, and the stability of the conveying pressure of a downstream pump is not facilitated. The pressure flow compensation valve is closed under the low-flow working condition, so that the cross section of the passage is reduced, and the jet pressure of the jet pipe is correspondingly increased. The pressure flow compensation valve is opened under the high flow working condition, the cross section of the passage is compensated, and the jet pressure of the jet pipe is kept unchanged, so that the stability of the output pressure is ensured.
In the preferred embodiment, in the pressure-flow rate compensation valve 19, the valve core 193 is connected to the spring 191, so that the liquid from the liquid inlet cavity 27 has sufficient pressure to open the valve core 193;
the pressure-flow compensated valve 19 is arranged to close during low flow conditions and to open during high flow conditions.
In a preferred scheme, the liquid inlet pipe 2 is communicated with a variable frequency pump, the variable frequency pump is not shown in the figure, the variable frequency pump is provided with a low-flow working condition and a high-flow working condition, and the liquid inlet pressure of the high-flow working condition is greater than that of the low-flow working condition;
the pressure-flow compensation valve 19 is arranged to close during low flow conditions and to open during high flow conditions.
In a preferred scheme, as shown in fig. 5, a top plate 13 is arranged at the top of the barrel, a sand inlet 28 is arranged on the top plate 13, a dispersion jet pipe 9 is arranged on the inner wall of the inner barrel 12 below the sand inlet 28, a plurality of openings are arranged along the circumference of the dispersion jet pipe 9, and the plurality of openings point to the horizontal projection position of the sand inlet 28. With this structure, when the sand falls from the sand inlet 28 and passes through the dispersion jet pipe 9, it is dispersed by the jet flow to improve the mixing effect.
The preferable scheme is as shown in fig. 5, the jet pipes are divided into two rows from top to bottom, the upper row of jet pipes 10 jet towards the bottom of the lower inner cylinder 12, and the lower row of jet pipes 20 jet horizontally. From this structure, form many places turbulent flow, improve the mixing effect, especially the horizontal jet flow of discharging jet pipe 20 plays certain effect of blockking to the sand of part whereabouts down, avoids the conglobate sand directly to fall into drain pipe 5 in, influences the mixing effect.
In a preferable scheme, as shown in fig. 1 and 3, the bottom of the inner cylinder body 12 is arc-shaped, the top wall of the liquid outlet pipe 5 is communicated with the inner cylinder body 12, and the liquid outlet pipe 5 is led out from one side of the inner cylinder body 12;
the liquid inlet cavity 27 is also communicated with one end of the liquid outlet auxiliary discharge jet pipe 16, and the other end of the liquid outlet auxiliary discharge jet pipe 16 is communicated with the end head of the liquid outlet pipe 5 and is used for flushing accumulated sand in the liquid outlet pipe 5; with the structure, the sand accumulation at the bottom of the liquid outlet pipe 5 is avoided.
The bottom of the inner cylinder 12 is also provided with a plurality of liquid outlet branch pipes 17, and the liquid outlet branch pipes 17 are communicated with the liquid outlet pipe 5. With this structure, the liquid discharge effect is further improved.
In a preferred scheme, as shown in fig. 3, the axis of the liquid outlet pipe 25 is inclined upwards from the connecting end to the free end, and the axis of the liquid outlet pipe 25 forms an included angle a with the horizontal plane;
the included angle a is 1-7 degrees. With this structure, a buffer is formed at the position of the liquid outlet pipe 25 to improve the mixing effect, and with this structure, the volume of the cylinder can be increased as much as possible in a narrow space.
Preferably, as shown in fig. 3, the stirring device is provided with a vertical shaft, the top end of the shaft is connected with the rotary driving device 1, and the part of the shaft located in the inner cylinder 12 is provided with a plurality of groups of stirring blades;
the inner wall of the inner cylinder body 12 is also provided with a turbulent baffle 18; the structure is used for forming turbulence in the barrel by matching with the stirring blades, and the solid-liquid mixing effect is improved.
Still be equipped with on the axle and lead sand plate 3, lead sand plate 3 and be the back taper structure, lead sand plate 3 and be used for making the position of sand distance axle. By the structure, the sand is prevented from being gathered at the position close to the shaft, and the turbulent flow is formed at the position close to the stirring blade, so that the solid-liquid mixing effect is further improved.
In a preferred embodiment, as shown in fig. 5, the shaft is a hollow shaft tube 22, an end of the hollow shaft tube 22 is connected to the movable connector 21, a shaft jet port 24 is disposed at a position of the hollow shaft tube 22 in the inner cylinder 12, and the shaft jet port 24 is communicated with the hollow shaft tube 22. Preferably, the axial jet port 24 corresponds to the lower jet pipe 20 in position, and the two are slightly staggered in height, so that the sand is further away from the axial position, and the solid-liquid mixing effect is further improved. By the combination of the structure, the sand is uniformly mixed with the liquid in the falling process, a better mixing effect is realized in a smaller cylinder volume, and the discharge pressure is stable.
In a preferred scheme, as shown in fig. 4, a liquid level meter 14 is arranged in the inner cylinder body 12; by the structure, the liquid height in the inner barrel body 12 is controlled, the liquid inlet flow of the liquid inlet pipe 2 is further controlled, the solid-liquid mixing efficiency is ensured, and the tank overflowing accident is avoided.
The free end of the liquid outlet pipe 5 is connected with a connecting pipe 25, the connecting pipe 25 is horizontally arranged, and a plurality of pipeline jet pipes 26 are arranged on the connecting pipe 25. With this structure, the sand is prevented from settling in the pipe after the liquid outlet pipe 5.
A liquid discharge pipe 7 is further arranged at the bottom of the inner cylinder body 12, the liquid discharge pipe 7 is communicated with the liquid outlet pipe 5 and a liquid outlet auxiliary discharge jet pipe 16, a liquid discharge valve 8 is arranged on the liquid discharge pipe 7, and the connecting position of the liquid outlet auxiliary discharge jet pipe 16 is positioned between the liquid discharge valve 8 and the end head of the liquid outlet pipe 5. The diameter of the discharge tube 7 and discharge assist jet 16 is smaller than the diameter of the discharge tube 5. preferably, the diameter of the discharge tube 7 and discharge assist jet 16 is smaller than 1/4 of the diameter of the discharge tube 5. With the structure, a high-speed jet flow is formed in the liquid outlet auxiliary discharge jet flow pipe 16, so that sand accumulation at the position of the liquid outlet pipe 5 is avoided, and the liquid discharge valve 8 is difficult to open.
When in use, liquid enters the inner cylinder body 12 from the liquid inlet pipe 2 through the liquid inlet cavity 27, and the liquid also enters the hollow shaft pipe 22 from the movable connector 21, and forms jet flows at the positions of the dispersion jet pipe 9, the upper jet pipe 10, the lower jet pipe 20, the liquid outlet auxiliary discharge jet pipe 16 and the shaft jet port 24 respectively; the agitator 15 drives the hollow shaft tube 22 to rotate through the transmission gear 23 in the rotation driving device 1. The rotation driving device 1 includes a motor and a speed reducer, and for example, a worm gear speed reducer is used to drive the hollow shaft tube 22 to rotate. The blades on the hollow shaft tube 22 rotate to create turbulence downwardly and outwardly and create more turbulent structures at the location of the turbulence baffle 18, which in combination with the turbulence created by the jet tube creates more, and more complex, turbulent structures. The solid material enters the inner cylinder body 12 from the sand inlet 28, contacts with the jet flow of the dispersion jet pipe 9 and is dispersed in the falling process, then contacts with the jet flow of the upper discharge pipe 10 and the stirring blade of the first layer to be mixed, part of sand flushed by the jet flow and close to the hollow shaft pipe 22 is separated from the hollow shaft pipe 22 by the sand guide plate 3 and the shaft jet port 24, the sand is mixed in a high-efficiency mixing area, the stirring blade of the first layer sends fully mixed solid-liquid mixed liquid into the liquid outlet pipe 5, and the fully mixed solid-liquid mixed liquid is further mixed under the impact of the liquid outlet auxiliary discharge jet pipe 16. The liquid outlet guide plate 6 is arranged at the top of the upper inclined end of the liquid outlet pipe 5 and is tangent to the inner cylinder 12 to guide the liquid into the connecting pipe 25 and avoid deposition at the position of the connecting joint. When the flow rate is low, the liquid pressure is not enough to overcome the elasticity of the spring 191, and the valve core 193 cannot be opened; in a high-flow working condition, the liquid pressure overcomes the elasticity of the spring 191, the valve core 193 is opened, and the pressure flow compensation valve 19 also generates jet flow.
The above embodiments are merely preferred technical solutions of the present invention, and should not be considered as limitations of the present invention, and the features in the embodiments and the examples in the present application may be arbitrarily combined with each other without conflict. The protection scope of the present invention shall be defined by the claims and the equivalents of the technical features in the claims. Namely, equivalent alterations and modifications within the scope of the invention are also within the scope of the invention.
Claims (10)
1. The utility model provides a mixing arrangement with pressure flow compensation, the novel nipple rectifier comprises a cylindrical shel, be equipped with agitating unit in the barrel, the barrel includes outer barrel (11) and interior barrel (12), outer barrel (11) top is equipped with roof (13), be equipped with sand inlet (28) on roof (13), be equipped with feed liquor cavity (27) between the lateral wall of outer barrel (11) and interior barrel (12), outer barrel (11) are equipped with feed liquor pipe (2), feed liquor pipe (2) are used for being connected with the pump, feed liquor pipe (2) and feed liquor cavity (27) intercommunication, the inner wall of barrel (12) is equipped with a plurality of efflux pipes including, efflux pipe and feed liquor cavity (27) intercommunication, be equipped with drain pipe (5) in the bottom of barrel, the bottom intercommunication of drain pipe (5) and interior barrel (12), characterized by: the device is also provided with at least one pressure flow compensation valve (19), the inlet of the pressure flow compensation valve (19) is communicated with the liquid inlet cavity (27), and the outlet of the pressure flow compensation valve (19) is positioned in the inner cylinder body (12).
2. A mixing apparatus with pressure flow compensation as claimed in claim 1, wherein: in the pressure flow compensation valve (19), a valve core (193) is connected with a spring (191) so that the valve core (193) can be opened only when liquid from the liquid inlet cavity (27) has enough pressure;
the pressure-flow compensation valve (19) is arranged to close during low flow conditions and to open during high flow conditions.
3. A mixing apparatus with pressure flow compensation as claimed in claim 1, wherein: the liquid inlet pipe (2) is communicated with a variable frequency pump, the variable frequency pump is provided with a low flow working condition and a high flow working condition, and the liquid inlet pressure of the high flow working condition is greater than that of the low flow working condition;
the pressure flow compensation valve (19) is arranged to be closed under low flow conditions and to be opened under high flow conditions.
4. A mixing apparatus with pressure flow compensation as claimed in claim 1, wherein: the inner wall of the inner cylinder body (12) below the sand inlet (28) is provided with a dispersion jet pipe (9), the dispersion jet pipe (9) is provided with a plurality of openings, and the plurality of openings point to the horizontal projection position of the sand inlet (28).
5. A mixing apparatus with pressure flow compensation as claimed in claim 1, wherein: the jet pipes are divided into two rows from top to bottom, the upper row of jet pipes (10) jet at the bottom of the inner cylinder (12) downwards, and the lower row of jet pipes (20) jet horizontally.
6. A mixing apparatus with pressure flow compensation as claimed in claim 1, wherein: the bottom of the inner cylinder body (12) is arc-shaped, the top wall of the liquid outlet pipe (5) is communicated with the inner cylinder body (12), and the liquid outlet pipe (5) is led out from one side of the inner cylinder body (12);
the liquid inlet cavity (27) is also communicated with one end of the liquid outlet auxiliary discharge jet pipe (16), and the other end of the liquid outlet auxiliary discharge jet pipe (16) is communicated with the end head of the liquid outlet pipe (5) and is used for flushing accumulated sand in the liquid outlet pipe (5);
the bottom of the inner cylinder body (12) is also provided with a plurality of liquid outlet branch pipes (17), and the liquid outlet branch pipes (17) are communicated with the liquid outlet pipe (5).
7. A mixing apparatus with pressure flow compensation as claimed in claim 1, wherein: the axis of the liquid outlet pipe (5) inclines upwards from the connecting end to the free end, and an included angle (a) is formed between the axis of the liquid outlet pipe (5) and the horizontal plane;
the included angle (a) is 1-7 degrees.
8. A mixing apparatus with pressure flow compensation as claimed in claim 1, wherein: the stirring device is provided with a vertical shaft, the top end of the shaft is connected with the rotary driving device (1), and a plurality of groups of stirring blades are arranged on the part of the shaft, which is positioned in the inner cylinder body (12);
the inner wall of the inner cylinder body (12) is also provided with a turbulent baffle (18);
still be equipped with on the axle and lead sand board (3), lead sand board (3) and be the back taper structure, lead sand board (3) and be used for making the position of sand off-axle.
9. A mixing apparatus with pressure flow compensation as claimed in claim 8, wherein: the shaft be hollow central siphon (22), the end and the swing joint head (21) of hollow central siphon (22) are connected, be equipped with axle jet flow mouth (24) in the position that hollow central siphon (22) are located interior barrel (12), axle jet flow mouth (24) and hollow central siphon (22) intercommunication.
10. A mixing apparatus with pressure flow compensation as claimed in claim 1, wherein: a liquid level meter (14) is arranged in the inner cylinder body (12);
the liquid outlet pipe (5) is connected with a connecting pipe (25), the connecting pipe (25) is horizontally arranged, and a plurality of pipeline jet pipes (26) are arranged on the connecting pipe (25).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202123131874.5U CN217093250U (en) | 2021-12-14 | 2021-12-14 | Mixing device with pressure flow compensation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202123131874.5U CN217093250U (en) | 2021-12-14 | 2021-12-14 | Mixing device with pressure flow compensation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN217093250U true CN217093250U (en) | 2022-08-02 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202123131874.5U Active CN217093250U (en) | 2021-12-14 | 2021-12-14 | Mixing device with pressure flow compensation |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN217093250U (en) |
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2021
- 2021-12-14 CN CN202123131874.5U patent/CN217093250U/en active Active
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