CN214915026U - Stirring equipment - Google Patents

Stirring equipment Download PDF

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Publication number
CN214915026U
CN214915026U CN202023119195.1U CN202023119195U CN214915026U CN 214915026 U CN214915026 U CN 214915026U CN 202023119195 U CN202023119195 U CN 202023119195U CN 214915026 U CN214915026 U CN 214915026U
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CN
China
Prior art keywords
stirring
liquid
flow distribution
distribution pipe
gas
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Expired - Fee Related
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CN202023119195.1U
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Chinese (zh)
Inventor
王刚
严蒙泉
刘成波
邸江波
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Xichuan Coal Mine Branch Of Huaneng Tongchuan Zhaojin Coal Power Co Ltd
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Xichuan Coal Mine Branch Of Huaneng Tongchuan Zhaojin Coal Power Co Ltd
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Priority to CN202023119195.1U priority Critical patent/CN214915026U/en
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Publication of CN214915026U publication Critical patent/CN214915026U/en
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Abstract

The application provides a stirring equipment relates to machinery, solves present stirring mode and makes the material mix inadequately to lead to the unsatisfactory problem of stirring effect. The stirring equipment comprises a stirring container provided with a liquid inlet pipeline, a flow distribution pipe and a fluid power conveying device; wherein the flow distribution tube is disposed in the stirred vessel; the fluid power conveying device is arranged outside the stirring container and is connected with one end of the flow distribution pipe. The application provides a agitated vessel is used for stirring the material.

Description

Stirring equipment
Technical Field
The application relates to the field of machinery, especially, relate to a agitated vessel.
Background
The stirring equipment is equipment capable of mixing liquid, gas, liquid or solid, and can accelerate stirring speed and improve the uniformity of material mixing compared with manual stirring.
At present agitated vessel stirs the material by the mode of mechanical stirring more, usually sets up the pivot that has the paddle inside agitated vessel, the pivot is connected with the outside motor of agitated vessel, and the pivot rotates and drives the paddle rotation under the drive of motor to the realization is to the stirring of material. However, the mechanical stirring mode often has a better stirring effect on the area involved by the blade, and the stirring of the materials in the corner area inside the stirring equipment is not obvious, so that the materials in the stirring equipment are not sufficiently mixed, and the stirring effect is not ideal.
SUMMERY OF THE UTILITY MODEL
The utility model provides an agitated vessel can be used for solving present stirring mode and make the material mix inadequately to lead to the unsatisfactory technical problem of stirring effect.
The embodiment of the utility model provides a stirring device, which comprises a stirring container provided with a liquid inlet pipeline, a flow distribution pipe and a fluid power conveying device;
wherein the flow distribution tube is disposed in the stirred vessel;
the fluid power conveying device is arranged outside the stirring container and is connected with one end of the flow distribution pipe.
Optionally, in one embodiment, the wall of the flow distribution pipe is provided with gaps, and the gaps are arranged along the length direction of the pipe.
Optionally, in one embodiment, the gap is flared in cross-section.
Optionally, in one embodiment, a plate is rolled into the flow distribution pipe, a first end and a second end of the plate have a space therebetween, and the second end overlaps the first end by a preset length to form the trumpet-shaped gap.
Optionally, in one embodiment, the flow distribution tube is disposed at the bottom of the stirred vessel in an archimedean spiral.
Optionally, in one embodiment, the fluid power delivery device is a liquid delivery device, and the fluid power delivery device comprises an inlet valve, a delivery pump and an outlet valve;
wherein, the inlet valve with the outlet valve all sets up on the stirred vessel, the inlet valve passes through the delivery pump with the outlet valve links to each other, and the inlet valve with one end of flow distribution pipe links to each other.
Optionally, in one embodiment, the fluid power delivery device is a gas delivery device, and the fluid power delivery device comprises an inlet valve and an air supply device;
wherein the inlet valve is arranged on the stirring container and is connected with one end of the flow distribution pipe, and the inlet valve is connected with the air supply device.
Optionally, in an embodiment, the fluid power delivery device is a gas-liquid delivery device, and the fluid power delivery device includes an outlet valve, a delivery pump, a gas-liquid mixer, an inlet valve, and a gas supply device;
wherein the inlet valve and the outlet valve are both arranged on the stirring container, and the outlet valve is connected with the inlet valve through the delivery pump and the gas-liquid mixer in sequence;
the gas supply device is connected with the inlet valve through the gas-liquid mixer, and the inlet valve is connected with one end of the flow distribution pipe.
Optionally, in one embodiment, the stirring apparatus further comprises a gas exhaust device disposed at the top of the stirring vessel.
Optionally, in an embodiment, the stirring apparatus further includes a drainage baffle, and the drainage baffle is disposed inside the stirring container and above the inlet of the liquid inlet pipeline corresponding to the stirring container.
The utility model discloses the beneficial effect who brings as follows:
the stirring equipment provided by the embodiment of the application comprises a stirring container provided with a liquid inlet pipeline, a flow distribution pipe and a fluid power conveying device; wherein the flow distribution tube is disposed in the stirred vessel; the fluid power conveying device is arranged outside the stirring container and is connected with one end of the flow distribution pipe. When needs are to stirring, the material is followed inlet channel gets into stirred vessel, and fluid power conveyor carries fluid into the flow distribution pipe with certain pressure, during the fluid formed the efflux via the flow distribution pipe and squeezes into the material in the stirred vessel, right the material forms the disturbance, causes the flow of material in the stirred vessel, and is right in order to realize the stirring of material, it is more even to enable each composition mixture in the material, and then improves stirring effect.
Drawings
In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the drawings required to be used in the description of the embodiments are briefly introduced below, and it is obvious that the drawings in the following description are some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to these drawings without creative efforts. In the drawings:
fig. 1 is a schematic structural diagram of a stirring apparatus provided in an embodiment of the present application;
fig. 2 is a schematic structural diagram of a flow distribution pipe according to an embodiment of the present disclosure;
FIG. 3 is a schematic cross-sectional view of a conduit of a flow distribution tube according to an embodiment of the present application;
FIG. 4 is a schematic cross-sectional view of a conduit of another flow distribution tube provided in an embodiment of the present application;
FIG. 5 is a schematic structural diagram of another stirring apparatus provided in the embodiments of the present application;
FIG. 6 is a schematic structural diagram of another stirring apparatus provided in the embodiment of the present application;
FIG. 7 is a schematic structural diagram of another stirring apparatus provided in the embodiment of the present application;
FIG. 8 is a schematic structural diagram of another stirring apparatus provided in the embodiment of the present application;
FIG. 9 is a schematic structural diagram of another stirring apparatus provided in the embodiment of the present application; .
Reference numerals:
10-stirring equipment; 101-a stirred vessel; 102-a liquid inlet pipeline; 103-a flow distribution pipe; 1031-clearance; 1032 — first end; 1033 — a second end; 104-fluid power transmission device; 1041 — an inlet valve; 1042 — a transfer pump; 1043-an outlet valve; 1044-air supply devices; 1045 — gas-liquid mixer; 105-a drainage baffle; 106 — an exhaust; 205-exhaust pipe; 210-a blower; 211-liquid outlet pipe.
Detailed Description
In order to make the objects, technical solutions and advantages of the present application more apparent, the technical solutions of the present application will be described in detail and completely with reference to the following specific embodiments of the present application and the accompanying drawings. It should be apparent that the described embodiments are only some of the embodiments of the present application, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present application.
The features of the terms first and second in the description and in the claims of the present application may explicitly or implicitly include one or more of such features. In the description of the present application, "a plurality" means two or more unless otherwise specified. In addition, "and/or" in the specification and claims means at least one of connected objects, a character "/" generally means that a preceding and succeeding related objects are in an "or" relationship.
In the description of the present application, it is to be understood that the terms "center," "longitudinal," "lateral," "length," "width," "thickness," "upper," "lower," "front," "rear," "left," "right," "vertical," "horizontal," "top," "bottom," "inner," "outer," "clockwise," "counterclockwise," "axial," "radial," "circumferential," and the like are used in the orientations and positional relationships indicated in the drawings for convenience in describing the present application and for simplicity in description, and are not intended to indicate or imply that the referenced devices or elements must have a particular orientation, be constructed and operated in a particular orientation, and are therefore not to be considered limiting of the present application.
In the description of the present application, it is to be noted that, unless otherwise explicitly specified or limited, the terms "mounted," "connected," and "connected" are to be construed broadly, e.g., as meaning either a fixed connection, a removable connection, or an integral connection; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meaning of the above terms in the present application can be understood in a specific case by those of ordinary skill in the art.
As described in the background of the application, at present, stirring equipment utilizes the mode of mechanical stirring to stir the material more, sets up the pivot that has the paddle usually inside stirring equipment, the pivot is connected with the outside motor of stirring equipment, and the pivot rotates and drives the paddle rotation under the drive of motor to the realization is to the stirring of material. However, the mechanical stirring mode often has a better stirring effect on the area involved by the blade, and the stirring of the materials in the corner area inside the stirring equipment is not obvious, so that the materials in the stirring equipment are not sufficiently mixed, and the stirring effect is not ideal.
In view of the above, the embodiment of the present application provides a stirring apparatus 10, which is used for solving the technical problem that the stirring effect is not ideal due to insufficient mixing of materials in the current stirring manner. As shown in fig. 1, the stirring device 10 comprises a stirring vessel 101 provided with a liquid inlet pipe 102, a flow distribution pipe 103 and a fluid power conveying device 104; wherein the flow distribution pipe 103 is provided in the agitation vessel 101; the fluid power transmission device 104 is arranged outside the stirring container 101 and is connected with one end of the flow distribution pipe 103.
The liquid inlet pipe 102 may be used to introduce a material into the stirring container 101, where the material may be a gas, a liquid, and a solid, or a mixture of at least two of them, and the material is preferably a liquid.
The stirring container 101 is a container for containing materials to be stirred, and provides a space for stirring the materials. The stirring container 101 may be made of carbon steel anticorrosive material, glass fiber reinforced plastic material, or polypropylene material, and the material may be selected according to the property of the contained material. The shape of the stirring container 101 may be a cylinder, and when the material in the stirring container 101 is stirred, the cylindrical stirring container may reduce a stirring dead angle. Of course, the specific shape of the stirring container 101 can be set according to actual needs.
The flow distribution pipe 103 is used for introducing fluid into the liquid in the stirring container 101 to generate disturbance on the liquid. The flow distribution pipe 103 may be used for stirring only, or may be used for adding other materials to be mixed with the materials in the stirring container 101. For example, the materials to be mixed include two materials, namely liquid a and liquid B, and the liquid a may be introduced into the stirring container 101 from the liquid inlet pipe 102, and then the liquid B is introduced into the liquid a in the stirring container 101 through the flow distribution pipe 103 to disturb the liquid a; the flow distribution pipe 103 simultaneously performs the functions of adding the material liquid B and stirring the liquid a and the liquid B. In practical applications, the materials to be mixed may also include more materials, for example, the materials include liquid a, liquid B and liquid C, and then the liquid a may be introduced into the stirring container 101 from the liquid inlet pipe 102, and then the liquid B and the liquid C are introduced into the liquid a in the stirring container through the flow distribution pipe 101, so as to disturb the liquid a, thereby achieving mixing and stirring of the liquid a, the liquid B and the liquid C. The liquid B and the liquid C may be introduced into the liquid a through the flow distribution pipe 103, the liquid B and the liquid C may be introduced into the liquid a sequentially and separately, or a mixture of the liquid B and the liquid C may be introduced into the liquid a. In addition, there are various ways of mixing the liquid a, the liquid B and the liquid C in the stirring vessel 102, for example, the liquid a and the liquid B are introduced first, and the liquid C is introduced through the flow distribution pipe 103; alternatively, the liquid a, the liquid B, and the liquid C are introduced first, and the other fluid is introduced through the flow distribution pipe 103. The arrangement position of the flow distribution pipe 103 in the stirring container 101 can also be set according to actual needs, for example, the flow distribution pipe 103 can be arranged at the bottom of the stirring container 101, or can be arranged at the middle part of the stirring container 101.
The fluid power transmission device 104 is used for transmitting fluid into the flow distribution pipe 103 at a certain pressure, and it is understood that the fluid power transmission device 104 includes a power device, and can transmit fluid into the pipe of the flow distribution pipe 103 at a certain pressure, so that the fluid coming out of the flow distribution pipe 103 forms a jet state, and can generate disturbance to the liquid in the stirring container 101, so as to realize stirring. The fluid delivered by the fluid power delivery device 104 to the flow distribution pipe 103 may be a liquid, a gas, or a mixture of a liquid and a gas. The power means may be a delivery pump.
By last knowing, agitated vessel equipment 10 that this application embodiment provided, when needs stir, the material is followed inlet pipe 102 gets into stirred vessel 101, and fluid power delivery device 104 is with certain pressure with fluid transport income distributing pipe 103, during the fluid forms the material that the efflux was squeezed into in stirred vessel 101 via distributing pipe 103, it is right the material forms the disturbance, causes the flow of material in stirred vessel 101, and it is right to realize the stirring of material, each composition mixes more evenly in enabling the material, and then improves stirring effect.
In order to further increase the pressure of the fluid flowing out of the flow distribution pipe 103, the disturbance intensity of the material in the stirring container 101 is enhanced, and the stirring effect is further improved. In one embodiment, the wall of the flow distribution pipe 103 is provided with a gap 1031, and the gap 1031 is arranged along the length direction of the pipe, as shown in fig. 2.
The width of the gap 1031 may be set according to actual needs. The number of the gaps 1031 and the orientation in the agitation vessel 101 may be set according to the arrangement position of the flow distribution pipe 103 in the agitation vessel 101. For example, when the flow distribution pipe 103 is provided at the bottom of the stirring vessel 101, only one gap may be provided in the flow distribution pipe 103, the gap extending from one end of the flow distribution pipe 103 to the other end of the flow distribution pipe, and the gap may face the top of the stirring vessel 101; under the condition that the flow distribution pipe is arranged in the middle of the stirring container 101, two gaps penetrating from one end of the flow distribution pipe 103 to the other end of the flow distribution pipe can be arranged on the flow distribution pipe 103, the two gaps are positioned on the opposite sides of the flow distribution pipe 103, the direction of one gap is opposite to the top of the stirring container 101, and the direction of the other gap is opposite to the bottom of the stirring container 101, so that jet flow can be generated and simultaneously driven into materials above the flow distribution pipe 103 and materials below the flow distribution pipe 103, the materials above the flow distribution pipe 103 and the materials below the flow distribution pipe 103 can be simultaneously stirred, and the stirring efficiency is improved.
In one embodiment, the gap 1031 is flared in cross-section, as shown in fig. 3.
The interface of the gap 1031 is arranged to be horn-shaped, so that the jet flow column can be helped to maintain high pressure to be driven into the material. If the gap 1031 is configured as a conventional straight line, the jet stream column coming out of the gap 1031 can only maintain a high pressure of a short path, and the pressure of the jet stream column at a position farther from the gap 1031 may be small, so that the stirring effect on the material farther from the gap 1031 is not ideal. The gap 1031 is flared, the section of the fluid ejected from the flow distribution pipe 103 is narrowed and widened again, and the path of the flared section provides an acceleration runway for the fluid ejection, so that the ejection pressure of the jet flow column can be further increased, the jet flow column can maintain the high pressure of a long path in the material in the stirring container 101, and the stirring effect is improved.
However, the flared section is formed on the wall of the flow distribution pipe 103, and the "acceleration track" provided by the flared section is limited by the wall thickness of the flow distribution pipe 103. Thus, in one embodiment, a sheet of material is rolled into the flow tube 103 with a gap between the first and second ends 1032, 1033, and the second end 1033 overlaps the first end 1032 a predetermined length to form the trumpet-shaped gap 1031.
As shown in fig. 4 (a cross-sectional view of the flow distribution pipe 103), the second end 1033 overlaps the first end 1032 for a predetermined length to form the trumpet-shaped gap 1031, and the trumpet-shaped gap 1031 corresponding to the overlapped predetermined length forms an "acceleration runway". On the other hand, the pipe section of the flow distribution pipe 103 is configured as shown in fig. 4, so that a fluid "squeezing out" effect can be formed at the gap 1031 on the pipe wall of the flow distribution pipe 103 based on the coanda (Conada) effect, the fluid is squeezed out into the stirring container through the gap 1031 after entering the flow distribution pipe 103, the process is that the section through which the fluid passes is narrowed and widened again, the moving direction of the fluid in the flow distribution pipe 103 in the curved pipe wall corresponding to the gap 1031 is along the curve of the curved inner wall under the action of the venturi principle, and the flow velocity is rapidly increased, as shown by the arrow in fig. 4, and then a jet with larger pressure is formed through the gap 1031, and when the direction of the gap 1031 is opposite to the top of the stirring container 101, an upward vertical jet is formed. The pipe diameter of the flow distribution pipe 103 may be 6cm, and the width of the gap 1031 may be 0.5 cm.
The arrangement of the flow distribution pipe 103 in the stirring vessel 101 may be set according to actual conditions, for example, the flow distribution pipe 103 may be a straight line type, a net type, a divergent type, or the like. In a preferred mode, the flow distribution pipe 103 is disposed at the bottom of the stirring vessel 101 in an archimedean spiral shape, as shown in fig. 5.
In the embodiment, the distribution pipe 103 is in the shape of an archimedean spiral, when fluid is injected into the material in the stirring container 101, a spiral annular flow state with a high flow speed is formed above the distribution pipe 103 in the shape of the archimedean spiral, and due to the upward movement of the fluid from the distribution pipe 103, the pressure in the middle area of the spiral annular flow state is reduced, so that the material in the middle area of the spiral annular flow state also forms a vertical upward flow state with a relatively low flow speed. That is, the flow distribution pipe 103 is set to be in the shape of an archimedean spiral, which can drive the material in the middle area of the spiral annular flow state to move, thereby improving the stirring effect. The diameter of the outermost circle of the flow distribution pipe 103 can be 1/3-1/2 of the diameter of the stirring container 101, and the flow distribution pipe 103 can be arranged for 2-3 circles.
On this basis, in order to further improve the stirring effect, in an embodiment, the stirring device 10 further includes a flow guide baffle 105, and the flow guide baffle 105 is disposed inside the stirring container 101 and above the corresponding inlet of the liquid inlet pipe 102 on the stirring container 101, as shown in fig. 5.
Through setting up drainage baffle 105 on stirred vessel 101 upper portion, flow to upper drainage baffle 105 together when the regional relatively slower flow state of velocity of flow in the middle of spiral annular quick flow state and spiral annular flow state, under drainage baffle 105's effect, the regional relatively slower flow state of velocity of flow all changes the direction in the middle of spiral annular quick flow state and spiral annular flow state, form to flow state all around and below, form the circulation flow state jointly with the regional relatively slower upward flow state of velocity of flow in the middle of spiral annular quick and spiral annular flow state, as shown by the arrow in fig. 5, thereby realize stirred vessel 101 interior material intensive mixing, the stirring effect is improved. On the other hand, the flow regime that the regional velocity of flow is relatively slow in the middle of the spiral annular flow regime can also eliminate the downward misorientation fluid that regional fluid flow direction drainage baffle produced in the middle of the spiral annular flow regime for the material forms regular cyclic motion state in stirred vessel 101, upwards flows to the drainage baffle from stirred vessel 101 middle part, then changes the flow direction, flows downwards at stirred vessel 101's periphery, thereby realizes the intensive mixing of material in stirred vessel 101.
As mentioned above, the fluid delivered to the flow distribution pipe 103 by the fluid power delivery device 104 may be a liquid, a gas or a mixture of a liquid and a gas, and then when the fluid delivered to the flow distribution pipe 103 by the fluid power delivery device 104 is a liquid, the fluid power delivery device 104 may be a liquid delivery device. When the fluid to be transported is one of the materials to be mixed, the fluid power transportation device 104 may include a power device and a fluid storage device, the power device is respectively connected with the distribution pipe 103 and the fluid storage device, and transports the fluid in the fluid storage device to the distribution pipe 103, wherein the power device may be a transportation pump. When all the materials to be mixed are introduced into the stirred vessel 101, if the liquid is used to continue stirring the materials in the stirred vessel 101 without causing a change in the volume of the materials in the stirred vessel 101, in an embodiment, the fluid power transmission device 104 is a liquid transmission device, and the fluid power transmission device 104 includes an inlet valve 1041, a transmission pump 1042 and an outlet valve 1043; wherein the inlet valve 1041 and the outlet valve 1043 are both disposed on the stirring vessel 101, the inlet valve 1041 is connected to the outlet valve 1043 through the delivery pump 1042, and the inlet valve 1041 is connected to one end of the flow pipe 103, as shown in fig. 6.
Through the scheme of this application embodiment, can pass through partial material in the agitator vessel 101 is followed by delivery pump 1042 the outlet valve 1042 drains outside the agitator vessel 101, and will again partial material is followed inlet valve 1041 lets in the flow distribution pipe 103, in the agitator vessel 101 is squeezed into again via the flow distribution pipe 103, has realized utilizing the material in the agitator vessel 101 to carry out the purpose of stirring, can reach and utilize liquid to stir the material in the agitator vessel 101, does not cause the effect of the change of material volume in the agitator vessel 101 simultaneously.
When the fluid conveyed by the fluid power conveying device 104 to the flow distribution pipe 103 is gas, the fluid power conveying device 104 may be a gas conveying device, and then in one embodiment, the fluid power conveying device 104 is a gas conveying device, and the fluid power conveying device includes an inlet valve 1041 and a gas feeding device 1044; the inlet valve 1041 is provided on the agitation vessel 101, the inlet valve 1041 is connected to the air supply means 1044, and the inlet valve 1041 is connected to one end of the flow tube 103, as shown in fig. 7.
Wherein, the air supply device 1044 can be a blower, and more specifically, the air supply device 1044 can be an electromagnetic air blower.
Through the scheme of this application embodiment, can squeeze into stirred tank 101 with gas in, realize the gas-liquid stirring in stirred tank 101. The liquid in the stirring container 101 is stirred by gas, and particularly in winter or under the condition that the stirring effect is not good when the liquid is driven into the stirring container by the gas distribution pipe 103, the stirring degree can be enhanced by introducing gas for stirring, and the stirring effect is further improved.
When the fluid delivered to the flow distribution pipe 103 by the fluid power delivery device 104 is a mixture of gas and liquid, the fluid power delivery device 104 may be a gas-liquid delivery device, and then in one embodiment, the fluid power delivery device 104 is a gas-liquid delivery device, and the fluid power delivery device includes an outlet valve 1043, a delivery pump 1042, a gas-liquid mixer 1045, an inlet valve 1041, and an air supply device 1044; wherein the inlet valve 1041 and the outlet valve 1043 are both arranged on the stirring vessel 101, and the outlet valve 1043 is connected with the inlet valve 1041 sequentially through the delivery pump 1042 and the gas-liquid mixer 1045; the air supply device 1044 is connected to the inlet valve 1041 through the air-liquid mixer 1045, and the inlet valve 1041 is connected to one end of the flow distribution pipe 103, as shown in fig. 8.
According to the scheme provided by the embodiment of the application, when the liquid in the stirred vessel 101 needs to be stirred by using the gas-liquid mixture, part of the liquid in the stirred vessel 101 can be guided from the outlet valve 1042 to the gas-liquid mixer 1045 by the delivery pump 1042, meanwhile, the gas is also input into the gas-liquid mixer 1045 by the gas feeding device 1044, the liquid and the gas are fully mixed in the gas-liquid mixer 1045 to obtain the gas-liquid mixture, and then the gas-liquid mixture is introduced into the flow distribution pipe 103 from the inlet valve 1041 and is then pumped into the stirred vessel 101 through the flow distribution pipe 103. Moreover, through the scheme provided by the embodiment of the application, liquid conveying, gas conveying and gas-liquid mixture conveying can be realized, namely, conveying of different fluids is realized through switching lines. For example, when fluid delivery is desired, outlet valve 1043, delivery pump 1042, and inlet valve 1041 are opened; when gas needs to be delivered, the inlet valve 1041 and the gas supply device 1044 are opened; when the gas-liquid mixture needs to be delivered, the inlet valve 1041, the outlet valve 1043, the delivery pump 1042, the gas-liquid mixer 1045, and the air supply device 1044 are opened.
In one embodiment, the stirring device 10 further comprises a gas exhaust 106, and the gas exhaust 106 is disposed at the top of the stirring vessel 101, as shown in fig. 8.
The exhaust device 106 is arranged at the top of the stirring container 101, so that the gas in the stirring container 101 can be exhausted, and particularly, when the gas is introduced into the liquid in the stirring container 101 through the distribution pipe 103 for stirring, the exhaust device 106 is arranged so that the distribution pipe 103 can continuously introduce the gas into the stirring container 101 for stirring, and meanwhile, the pressure in the stirring container 101 can be ensured to be stable. The exhaust 106 may be an exhaust conduit.
In practical application, the stirring container 101 may further be provided with a liquid outlet pipe for discharging the material stirred in the stirring container 101 out of the stirring container 101 for subsequent processes.
It should be noted that, the "connection" of the components in the stirring device 10 provided in the embodiment of the present application may be a connection through a pipe. For example, the outlet valve 1043 may be connected to the inlet valve 1041 sequentially through the delivery pump 1042 and the gas-liquid mixer 1045, the outlet valve 1043 may be connected to the delivery pump 1042 through a pipe, the delivery pump 1042 is connected to the gas-liquid mixer 1045 through a pipe, and the gas-liquid mixer 1045 is connected to the inlet valve 1041 through a pipe.
The stirring device provided in the examples of the present application will be explained below with reference to specific embodiments, and it should be understood that the following embodiments are only examples and do not represent limitations of the stirring device provided in the examples of the present application.
A stirring device 10, as shown in FIG. 9, comprises a stirring container 101 provided with a liquid inlet pipe 102 and a liquid outlet pipe 211, a flow distribution pipe 103, a flow guide baffle 105, an exhaust pipe 205, an outlet valve 1043, a delivery pump 1042, a gas-liquid mixer 1045, an inlet valve 1041 and a blower 210.
Wherein, the flow distribution pipe 103 be the spiral setting of archimedes in stirred vessel 101's bottom, just be provided with the clearance on the pipe wall of flow distribution pipe 103, the clearance is arranged along pipeline length direction (see fig. 2), the cross-section in clearance is the loudspeaker form, and panel curls into flow distribution pipe 103, the interval has between the first end and the second end of panel, the second end with first end overlaps to predetermine length and forms loudspeaker form's clearance (see fig. 4), just the orientation in clearance is just to stirred vessel 101's top. The outlet valve 1043 and the inlet valve 1041 are both provided on the agitation vessel 101, and the inlet valve 1041 is connected to one end of the flow distribution pipe 103. The outlet valve 1043 is connected to the inlet valve 1041 sequentially through the delivery pump 1042 and the gas-liquid mixer 1045, and the blower 210 is connected to the inlet valve 1041 through the gas-liquid mixer 1045.
Through the agitated vessel 10 that this application embodiment provided, when needs are to stirring, liquid is followed inlet pipeline 102 gets into stirred vessel 101, and liquid, gas or gas-liquid mixture can certain pressure with fluid transport feed distribution pipe 103 to in forming the liquid that the efflux was squeezed into stirred vessel 101 via distribution pipe 103, right in the liquid forms the disturbance, cause the flow of liquid in stirred vessel 101, it is right to realize the stirring of liquid. Simultaneously, can make the material form regular circular motion state in stirred vessel 101, from stirred vessel 101 middle part upflow to drainage baffle, then change the flow direction, peripheral downflow at stirred vessel 101 to realize the intensive mixing of material in stirred vessel 101, can improve stirring effect to a very big degree.
It should also be noted that the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus. Without further limitation, an element defined by the phrase "comprising an … …" does not exclude the presence of other like elements in a process, method, article, or apparatus that comprises the element.
Finally, it should be noted that: the above embodiments are only used to illustrate the technical solution of the present invention, and not to limit it; although the present invention has been described in detail with reference to the foregoing embodiments, it should be understood by those skilled in the art that: the technical solutions described in the foregoing embodiments may still be modified, or some technical features may be equivalently replaced; such modifications and substitutions do not depart from the spirit and scope of the present invention in its corresponding aspects.

Claims (10)

1. The stirring equipment is characterized by comprising a stirring container provided with a liquid inlet pipeline, a flow distribution pipe and a fluid power conveying device;
wherein the flow distribution tube is disposed in the stirred vessel;
the fluid power conveying device is arranged outside the stirring container and is connected with one end of the flow distribution pipe.
2. The stirring device according to claim 1, wherein the walls of the flow distribution pipe are provided with gaps, and the gaps are arranged along the length direction of the pipe.
3. Stirring device according to claim 2, characterised in that the gap has a trumpet-shaped cross-section.
4. The stirring apparatus of claim 3, wherein a sheet material is crimped into the distribution tube with a space between a first end and a second end of the sheet material, the second end overlapping the first end by a predetermined length to form the flared gap.
5. The mixing apparatus of claim 1, wherein the flow distribution pipe is disposed at the bottom of the mixing vessel in an archimedean spiral.
6. The mixing apparatus of claim 1, wherein the fluid power delivery device is a liquid delivery device, the fluid power delivery device comprising an inlet valve, a delivery pump, and an outlet valve;
wherein, the inlet valve with the outlet valve all sets up on the stirred vessel, the inlet valve passes through the delivery pump with the outlet valve links to each other, and the inlet valve with one end of flow distribution pipe links to each other.
7. The mixing apparatus of claim 1, wherein the fluid power delivery device is a gas delivery device, the fluid power delivery device comprising an inlet valve and a gas delivery device;
wherein the inlet valve is arranged on the stirring container and is connected with one end of the flow distribution pipe, and the inlet valve is connected with the air supply device.
8. The mixing apparatus of claim 1, wherein the fluid power delivery device is a gas-liquid delivery device, the fluid power delivery device comprising an outlet valve, a delivery pump, a gas-liquid mixer, an inlet valve, and a gas delivery device;
wherein the inlet valve and the outlet valve are both arranged on the stirring container, and the outlet valve is connected with the inlet valve through the delivery pump and the gas-liquid mixer in sequence;
the gas supply device is connected with the inlet valve through the gas-liquid mixer, and the inlet valve is connected with one end of the flow distribution pipe.
9. The mixing apparatus of any of claims 7-8, further comprising a vent disposed at a top of the mixing vessel.
10. The mixing apparatus according to any one of claims 1 to 8, further comprising a flow directing baffle disposed within the mixing vessel above a corresponding inlet of the liquid inlet conduit on the mixing vessel.
CN202023119195.1U 2020-12-22 2020-12-22 Stirring equipment Expired - Fee Related CN214915026U (en)

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Application Number Priority Date Filing Date Title
CN202023119195.1U CN214915026U (en) 2020-12-22 2020-12-22 Stirring equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202023119195.1U CN214915026U (en) 2020-12-22 2020-12-22 Stirring equipment

Publications (1)

Publication Number Publication Date
CN214915026U true CN214915026U (en) 2021-11-30

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN202023119195.1U Expired - Fee Related CN214915026U (en) 2020-12-22 2020-12-22 Stirring equipment

Country Status (1)

Country Link
CN (1) CN214915026U (en)

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