CN207856693U - Gas-liquid material mixer and gas-liquid material mixing equipment - Google Patents
Gas-liquid material mixer and gas-liquid material mixing equipment Download PDFInfo
- Publication number
- CN207856693U CN207856693U CN201721802601.XU CN201721802601U CN207856693U CN 207856693 U CN207856693 U CN 207856693U CN 201721802601 U CN201721802601 U CN 201721802601U CN 207856693 U CN207856693 U CN 207856693U
- Authority
- CN
- China
- Prior art keywords
- gas
- liquid material
- liquid
- water tank
- pipeline
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Abstract
The utility model provides a kind of gas-liquid material mixer and gas-liquid material mixing equipment, it is related to gas-liquid material mixer and gas-liquid material mixing equipment technical field, the gas-liquid material mixer includes material blending tank, the gas pipeline equipped with multiple sintered filter cores and the fluid pipeline equipped with multiple nozzles, sintered filter core and nozzle are connected to material blending tank, and fluid pipeline is circulating line, multiple nozzles are circumferentially equidistantly mounted on fluid pipeline.The gas-liquid material mixer of the utility model has the characteristics that mixed effect and versatility are good.
Description
Technical field
The utility model is related to gas-liquid material mixer and gas-liquid material mixing equipment technical field more particularly to a kind of gas
Liquid material mixer and gas-liquid material mixing equipment.
Background technology
In recent decades, due to traditional industry and infant industry, such as chemical engineering, metallurgical engineering, nuclear engineering, aviation and boat
The rapid development of its engineering etc., the research and application of two-phase flow have also obtained the development across epochal character, and develop into one
Independent research branch, has obtained extensive attention.Wherein, biphase gas and liquid flow is a kind of shape the most universal in Multiphase Flow
Formula is widely present in each industrial processes, and very important effect is played in national economy and daily life.Example
Such as, the boiler in energy source and power industrial process, heat exchanger, steam-water separator and reboiler, condenser in chemical industry process
Etc. equipment, the vapour compression refrigeration equipment in refrigeration low-temperature industrial process and the oil-gas mining in petroleum industry, oil and gas multiphase flow
Deng during, all there is biphase gas and liquid flow kinety system.The system of well known liquid material and gas material mixed dissolution in existing
Static mixer, Venturi tube are mainly used, liquid fluidized bed mixer is penetrated etc. and achievees the purpose that mixed dissolution.
Although existing Liqiud-gas mixing device can reach the mixing purpose of gas material and liquid material, due to
Therefore gas material and the intrinsic complexity of liquid material, the limitation of diversity and measurement means lead to existing gas-liquid
Mixing arrangement hybrid parameter is single, mixed material is not uniformly mixed, there is technical issues that mixed effect and.
Utility model content
The purpose of this utility model is to provide a kind of gas-liquid material mixer and gas-liquid material mixing equipment, with alleviate by
Therefore lead to existing gas in the intrinsic complexity of gas material and liquid material, the limitation of diversity and measurement means
Liquid mixing arrangement hybrid parameter is single, mixed material is not uniformly mixed, and there are the technologies of mixed effect and poor universality to ask
Topic.
A kind of gas-liquid material mixer provided by the utility model, including material blending tank, equipped with multiple sintered filter cores
Gas pipeline and fluid pipeline equipped with multiple nozzles, the sintered filter core and the nozzle connect with the material blending tank
It is logical, and the fluid pipeline is circulating line, multiple nozzles are circumferentially equidistantly mounted on the fluid pipeline.
Further, the nozzle includes first jet and second nozzle, and the first jet divides with the second nozzle
The both sides of the ring-shaped liquid pipeline are not set, and the sintered filter core is arranged in the first jet and the second nozzle
Top.
Further, the first jet and the second nozzle are jet rose.
Further, it is respectively connected with motor-driven valve on the fluid pipeline and the gas pipeline.
Further, it is respectively connected on the fluid pipeline and the gas pipeline and is connected with flowmeter and pressure inverting meter.
Further, further include providing the solution feed pump of power for the fluid pipeline and being taken out for air in the solution feed pump
From vacuum unit;
The vacuum unit includes gas water separation tank and the vacuum pump that is detached for air in the solution feed pump, the air water
Knockout drum and the solution feed pump are connected to the vacuum pump.
Further, the fluid pipeline is communicated with liquid supply box, and the liquid supply box includes shell, is arranged in the shell
Water tank cavity, the water tank box that is arranged in the water tank cavity and the side wall in the water tank cavity and the water tank are set
Liquid level unit between the side wall of babinet.
Further, the liquid level unit includes spring and capacitance liquid level meter, and the short transverse of the water tank box is equipped with
The spring, the capacitance liquid level meter are pressed on the spring.
Further, it is provided with water suction cavity in the water tank box, the water suction cavity is hollow tubular structure, and institute
The one end for stating water suction cavity is connect with the top of the water tank box, and the other end extends to the bottom of the water tank box.
The beneficial effects of the utility model are:
The gas-liquid material mixer include material blending tank, the gas pipeline equipped with multiple sintered filter cores and be equipped with multiple sprays
The fluid pipeline of mouth, sintered filter core and nozzle are connected to material blending tank, and staff divides gas material and liquid material
It Dui Ying not be passed through in gas pipeline and fluid pipeline, wherein gas pipeline is equipped with multiple sintered filter cores, and fluid pipeline is equipped with more sprays
Mouth, when carrying out gas-liquid mixed, gas material and liquid material correspond to flowed out from corresponding sintered filter core and nozzle respectively, due to
Sintered filter core is suppressed by lamination using multilayer stainless (steel) wire, and therefore, the mesh of each layer silk screen is interlaced, gas material
Can be pure and the mesh evenly along sintered filter core at flow into material blending tank, meanwhile, between multiple nozzles are circumferentially equal
Away from fluid pipeline, fluid pipeline is circulating line, when liquid material flows into ring-shaped liquid pipeline along main pipeline, annular
Fluid pipeline enables to liquid material along its circumferential flow, so that liquid material mixing is more uniform, via annular
In the uniform gentle inflow material blending tank of liquids and gases after fluid pipeline and sintered filter core difference alignment processing, and in object
It is adequately mixed in material blending tank.
In addition to this, since gas material and liquid material are corresponding mixed via sintered filter core and nozzle inflow material
It closes in tank, and then the mixing of a variety of gas-liquid materials can be suitble to, without considering that gas material and liquid material are corresponding solid
There is characteristic, it is therefore prevented that gas material and the corresponding inherent characteristic of liquid material cause the gas-liquid in mixer pipeline that can not put down
Slow the problem of smoothly flowing out, or need to prepare the feelings that cannot achieve when the product of different component, different ratio simultaneously
Condition improves the versatility of the gas-liquid material mixer.
Gas-liquid material mixer provided by the utility model is sprayed by the way that liquid to be passed through in the fluid pipeline of annular by nozzle
Go out and flows into material blending tank, meanwhile, gas material via the processing of sintered filter core enables gas material pure and equal
It is flowed into material blending tank along at the mesh of sintered filter core evenly, distinguishes corresponding position via ring-shaped liquid pipeline and sintered filter core
Liquids and gases after reason can be uniformly in gentle inflow material blending tank, and is adequately mixed in material blending tank
It closes, meanwhile, which is suitble to the mixing of a variety of gas-liquid materials, it is therefore prevented that gas material and liquid material are respectively right
The problem of inherent characteristic answered causes the gas-liquid in mixer pipeline not flow out smoothly gently, or need to make simultaneously
Standby different component, different ratio product when the case where cannot achieve, improve the versatility of the gas-liquid material mixer.
The utility model provides a kind of gas-liquid material mixing equipment with above-mentioned gas-liquid material mixer.
The beneficial effects of the utility model are:
The gas-liquid material mixing equipment is identical as advantage possessed by above-mentioned gas-liquid material mixer, and details are not described herein.
Description of the drawings
It, below will be right in order to illustrate more clearly of specific embodiment of the present invention or technical solution in the prior art
Specific implementation mode or attached drawing needed to be used in the description of the prior art are briefly described, it should be apparent that, it is described below
In attached drawing be that some embodiments of the utility model are not paying creativeness for those of ordinary skill in the art
Under the premise of labour, other drawings may also be obtained based on these drawings.
Fig. 1 is the structural schematic diagram for the gas-liquid material mixer that the utility model embodiment one provides;
Fig. 2 is the vertical view of Fig. 1;
Fig. 3 is the position relationship structural diagram of solution feed pump, vacuum unit and fluid pipeline three;
Fig. 4 is the structural schematic diagram of the liquid supply box in Fig. 3;
Fig. 5 is the enlarged drawing at the A in Fig. 4.
Icon:1- gas pipelines;2- fluid pipelines;3- solution feed pumps;4- vacuum units;5- liquid supply box;6- water suction cavitys;
11- sintered filter cores;21- first jets;22- second nozzles;41- gas water separation tanks;42- vacuum pumps;51- shells;52- water tank casees
Body;53- liquid level units;531- springs;532- capacitance liquid level meters;The first capacitor boards of 5321-;The second capacitor boards of 5322-.
Specific implementation mode
The technical solution of the utility model is clearly and completely described below in conjunction with attached drawing, it is clear that described
Embodiment is the utility model a part of the embodiment, instead of all the embodiments.Based on the embodiments of the present invention, originally
The every other embodiment that field those of ordinary skill is obtained without making creative work, belongs to this practicality
Novel protected range.
It is in the description of the present invention, it should be noted that term "center", "upper", "lower", "left", "right", " perpendicular
Directly ", the orientation or positional relationship of the instructions such as "horizontal", "inner", "outside" is to be based on the orientation or positional relationship shown in the drawings, and is only
The utility model and simplifying describes for ease of description, do not indicate or imply the indicated device or element must have it is specific
Orientation, with specific azimuth configuration and operation, therefore should not be understood as limiting the present invention.In addition, term " the
One ", " second ", " third " are used for description purposes only, and are not understood to indicate or imply relative importance.
In the description of the present invention, it should be noted that unless otherwise clearly defined and limited, term " is pacified
Dress ", " connected ", " connection " shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection, or integrally
Connection;It can be mechanical connection, can also be electrical connection;Can be directly connected, can also indirectly connected through an intermediary,
It can be the connection inside two elements.For the ordinary skill in the art, it can understand above-mentioned art with concrete condition
The concrete meaning of language in the present invention.
Embodiment one
As depicted in figs. 1 and 2, a kind of gas-liquid material mixer provided in this embodiment, including material blending tank, be equipped with it is more
The gas pipeline 1 of a sintered filter core 11 and fluid pipeline 2 equipped with multiple nozzles, sintered filter core 11 and nozzle are mixed with material
Tank is connected to, and fluid pipeline 2 is circulating line, and multiple nozzles are circumferentially equidistantly mounted on fluid pipeline 2.
The gas-liquid material mixer includes material blending tank, the gas pipeline 1 equipped with multiple sintered filter cores 11 and is equipped with more
The fluid pipeline 2 of a nozzle, sintered filter core 11 and nozzle are connected to material blending tank, and staff is by gas material and liquid
Material is corresponding respectively to be passed through in gas pipeline 1 and fluid pipeline 2, wherein gas pipeline 1 is equipped with multiple sintered filter cores 11, liquid
Pipeline 2 is equipped with multiinjector, and when carrying out gas-liquid mixed, gas material and liquid material are corresponded to respectively from corresponding sintered filter core 11
It is flowed out with nozzle, since sintered filter core 11 is suppressed by lamination using multilayer stainless (steel) wire, the mesh of each layer silk screen
Interlaced, gas material can be pure and be flowed into material blending tank evenly along at the mesh of sintered filter core 11, meanwhile,
Multiple nozzles are circumferentially equidistantly mounted on fluid pipeline 2, and fluid pipeline 2 is circulating line, and liquid material is along main pipeline stream
When entering ring-shaped liquid pipeline 2, ring-shaped liquid pipeline 2 enables to liquid material along its circumferential flow, so that liquid material
What is mixed is more uniform, and the liquids and gases after alignment processing are distinguished via ring-shaped liquid pipeline 2 and sintered filter core 11 and are uniformly put down
In slow inflow material blending tank, and adequately mixed in material blending tank.
In addition to this, since gas material and liquid material are corresponding via sintered filter core 11 and nozzle inflow material
In blending tank, and then the mixing of a variety of gas-liquid materials can be suitble to, without considering that gas material and liquid material are corresponding
Inherent characteristic, it is therefore prevented that gas material and the corresponding inherent characteristic of liquid material cause the gas-liquid in mixer pipeline can not
Gentle the problem of smoothly flowing out, or need to prepare simultaneously and cannot achieve when the product of different component, different ratio
Situation improves the versatility of the gas-liquid material mixer.
The gas-liquid material mixer provided in the present embodiment is by the way that liquid to be passed through in the fluid pipeline 2 of annular, by nozzle
It sprays and flows into material blending tank, meanwhile, gas material enables gas material pure via the processing of sintered filter core 11
And flowed into material blending tank evenly along at the mesh of sintered filter core 11, via ring-shaped liquid pipeline 2 and sintered filter core 11
The liquids and gases after alignment processing can be uniformly in gentle inflow material blending tank respectively, and is carried out in material blending tank
Adequately mixing, meanwhile, which is suitble to the mixing of a variety of gas-liquid materials, it is therefore prevented that gas material and liquids
Expect the problem of corresponding inherent characteristic causes the gas-liquid in mixer pipeline not flow out smoothly gently, Huo Zhetong
When the case where needing to cannot achieve when preparing the product of different component, different ratio, improve the logical of the gas-liquid material mixer
The property used.
As depicted in figs. 1 and 2, specifically, nozzle includes first jet 21 and second nozzle 22, first jet 21 and second
Nozzle 22 is respectively set the both sides of ring-shaped liquid pipeline 2, and sintered filter core 11 is arranged in first jet 21 and second nozzle 22
Top.
In the present embodiment, nozzle includes first jet 21 and second nozzle 22, and first jet 21 divides with second nozzle 22
Not She Zhi ring-shaped liquid pipeline 2 both sides, being equipped with first jet 21 and second nozzle 22 in 2 both sides of fluid pipeline of annular can
Increase fluid flow, and then improves gas-liquid mixed efficiency, meanwhile, sintered filter core 11 is arranged in first jet 21 and second nozzle
22 top enables to gas-liquid material that can be come into full contact with each other with liquid material, further improves gas material and liquid
The mixed effect of material.
Wherein, first jet 21 and second nozzle 22 are jet rose.
In this embodiment, be can further such that liquid material can uniformly gentle ejection, and then fully and liquid
Material is sufficiently mixed, and first jet 21 and second nozzle 22 are jet rose.
Wherein, it is respectively connected with motor-driven valve on fluid pipeline 2 and gas pipeline 1.
In the present embodiment, it is that can adjust the flow of gas material and liquid material, and then preferably realize different groups
Divide, the product mix of different ratio.
Wherein, it is respectively connected on fluid pipeline 2 and gas pipeline 1 and is connected with flowmeter and pressure inverting meter.
In this embodiment, flowmeter can detect and control in real time the stream in 1 pipe of corresponding fluid pipeline 2 and gas pipeline
Amount, and then realize the flow value for adjusting and detecting in fluid pipeline 2 and 1 pipe of gas pipeline.
Wherein, pressure inverting meter can detect and control in real time the pressure in 1 pipe of corresponding fluid pipeline 2 and gas pipeline
Value, to realize the random adjustment of the gas-liquid material mixer overpressure and flow, and then meets entire gas-liquid material mixer
Demand to pressure and changes in flow rate improves the practicability and functionality of the gas-liquid material mixer.
As shown in figure 3, specifically, the gas-liquid material mixer further includes 3 He of solution feed pump for providing power for fluid pipeline 2
The vacuum unit 4 detached for air in solution feed pump 3.
Vacuum unit 4 includes gas water separation tank 41 and the vacuum pump 42 detached for air in solution feed pump 3, gas water separation tank
41 and solution feed pump 3 be connected to vacuum pump 42.
In the present embodiment, which further includes providing the solution feed pump 3 of power for fluid pipeline 2 and being used for
The vacuum unit 4 that air detaches in solution feed pump 3, vacuum unit 4 include the vacuum pump 42 detached for air in solution feed pump 3,
Gas water separation tank 41 and solution feed pump 3 are connected to vacuum pump 42, when the liquid material access of fluid pipeline 2 flows into the gas-liquid material
After the main pipeline of mixer, start vacuum pump 42, vacuum pump 42 can be by the sky in the pipeline before solution feed pump 3 and vacuum pump 42
Gas evacuates, and after the air in pipeline before solution feed pump 3 and vacuum pump 42 is evacuated, liquid material will be in the work of atmospheric pressure
The gradually flow forward under, when liquid material under the action of atmospheric pressure full of the pipeline before solution feed pump 3 and vacuum pump 42,
The valve closed vacuum pump 42 and be arranged on vacuum pump 42, the work of centrifugal force can be generated in solution feed pump 3 by opening liquid material just
It is sprayed along nozzle with lower, it is ingenious in design, it is reasonable for structure.
Wherein, vacuum unit 4 further includes gas water separation tank 41, and the air after being detached via vacuum pump 42 contains steam, contains
Have the air of steam via gas water separation tank 41 after, air is along the outlet stream outwardly air of gas water separation tank 41, and steam is then
It stays in tank body.
As shown in Figure 4, wherein fluid pipeline 2 is communicated with liquid supply box 5, and liquid supply box 5 includes shell 51, is arranged in shell 51
Interior water tank cavity, the water tank box 52 being arranged in water tank cavity and the side wall and water tank box 52 in water tank cavity are set
Liquid level unit 53 between side wall.
In the present embodiment, due to being provided with water tank cavity in shell 51, and water tank box 52 is provided in water tank cavity,
After being packed into liquid material in water tank box 52, liquid material generates pressure to 52 side wall of water tank box, and pressure passes through water tank case
52 side wall of body is transmitted to the liquid level unit 53 being arranged between the side wall and the side wall of water tank box 52 of water tank cavity, liquid level unit
53 can detect the liquid level in water tank box 52, and then staff can detect water tank box according to liquid level unit 53
The time liquid level of liquid material chooses whether the adding liquid material into water tank box 52 in 52.
As shown in figure 5, specifically, liquid level unit 53 includes spring 531 and capacitance liquid level meter 532, the height of water tank box 52
It spends direction and is equipped with spring 531, capacitance liquid level meter 532 is pressed on spring 531.
In the present embodiment, the short transverse of water tank box 52 be equipped with spring 531, spring 531 be it is multiple, it is multiple along water tank
On the spring 531 of the short transverse setting of babinet 52, capacitance liquid level meter 532 includes two pieces of first capacitor boards 5321 being oppositely arranged
With the second capacitor board 5322, when liquid level changes in water tank box 52, multiple springs 531 also deform upon therewith, to change
The distance between first capacitor board 5321 and the second capacitor board 5322, and then change the capacitance between two plates, capacitance liquid level meter 532
The height of liquid level in water tank box 52 can be identified according to the variation of capacitance, to be sent out when water level is too low in water tank box 52
The case where going out alarm or cut off the power, avoiding the idle running of solution feed pump 3 that the pump housing is caused to damage.
As shown in Figure 4, wherein water suction cavity 6 is provided in water tank box 52, water suction cavity 6 is hollow tubular structure, and
One end of water suction cavity 6 is connect with the top of water tank box 52, and the other end extends to the bottom of water tank box 52.
In this embodiment, it in order to utmostly utilize the liquid material in water tank box 52, is provided in water tank box 52
Absorb water cavity 6, and the cavity 6 that absorbs water is hollow tubular structure, and water suction cavity 6 is vertically arranged in water tank box 52, and water sucting cavity
One end of body 6 is connect with the top of water tank box 52, and the other end of water suction cavity 6 extends to the bottom of water tank box 52, uses
Such setting, water suction cavity 6 can persistently keep inhaling before liquid level is flushed with 6 bottom of water suction cavity in water tank box 52
Water state can farthest utilize water tank to ensure after it will fill liquid material in water tank box 52 each time
Liquid material in babinet 52, under same amount of liquid material, reduce the adding liquid material into water tank box 52
Number improves the functionality and practicability of the gas-liquid material mixer.
Embodiment two
The present embodiment provides a kind of gas-liquid material mixing equipment, which has one institute of above-described embodiment
The gas-liquid material mixer stated.
The gas-liquid material mixing equipment is identical as advantage possessed by above-mentioned gas-liquid material mixer, and details are not described herein.
Finally it should be noted that:The above various embodiments is only to illustrate the technical solution of the utility model, rather than limits it
System;Although the utility model has been described in detail with reference to the foregoing embodiments, those skilled in the art should
Understand:It still can be with technical scheme described in the above embodiments is modified, either to which part or whole
Technical characteristic carries out equivalent replacement;And these modifications or replacements, this practicality that it does not separate the essence of the corresponding technical solution are new
The range of each embodiment technical solution of type.
Claims (10)
1. a kind of gas-liquid material mixer, which is characterized in that the gas including material blending tank, equipped with multiple sintered filter cores (11)
Pipeline (1) and fluid pipeline (2) equipped with multiple nozzles, the sintered filter core (11) and the nozzle are mixed with the material
Tank is connected to, and the fluid pipeline (2) is circulating line, and multiple nozzles are circumferentially equidistantly mounted on the fluid pipeline
(2) on.
2. gas-liquid material mixer according to claim 1, which is characterized in that the nozzle include first jet (21) and
Second nozzle (22), the first jet (21) are separately positioned on the two of the fluid pipeline (2) with the second nozzle (22)
Side, and the sintered filter core (11) is arranged in the top of the first jet (21) and the second nozzle (22).
3. gas-liquid material mixer according to claim 2, which is characterized in that the first jet (21) and described second
Nozzle (22) is jet rose.
4. gas-liquid material mixer according to claim 3, which is characterized in that the fluid pipeline (2) and the gas
Pipeline is respectively connected with motor-driven valve on (1).
5. gas-liquid material mixer according to claim 4, which is characterized in that the fluid pipeline (2) and the gas
It is respectively connected on pipeline (1) and is connected with flowmeter and pressure inverting meter.
6. according to claim 1-5 any one of them gas-liquid material mixers, which is characterized in that further include for the liquid line
The vacuum unit (4) that road (2) provides the solution feed pump (3) of power and detached for the solution feed pump (3) interior air;
The vacuum pump that the vacuum unit (4) includes gas water separation tank (41) and detaches for the solution feed pump (3) interior air
(42), the gas water separation tank (41) and the solution feed pump (3) are connected to the vacuum pump (42).
7. gas-liquid material mixer according to claim 6, which is characterized in that the fluid pipeline (2) is communicated with feed flow
Case (5), the liquid supply box (5) include shell (51), the water tank cavity being arranged in the shell (51), are arranged in the water tank
Water tank box (52) in cavity and it is arranged between the side wall and the side wall of the water tank box (52) of the water tank cavity
Liquid level unit (53).
8. gas-liquid material mixer according to claim 7, which is characterized in that the liquid level unit (53) includes spring
(531) and capacitance liquid level meter (532), the short transverse of the water tank box (52) are equipped with the spring (531), the capacitive liquid
Position meter (532) is pressed on the spring (531).
9. gas-liquid material mixer according to claim 8, which is characterized in that be provided with suction in the water tank box (52)
Water chamber (6), the water suction cavity (6) are hollow tubular structure, and one end and the water tank box of the water suction cavity (6)
(52) top connection, the other end extend to the bottom of the water tank box (52).
10. a kind of gas-liquid material mixing equipment, which is characterized in that mixed including the gas-liquid material as described in claim any one of 1-9
Clutch.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201721802601.XU CN207856693U (en) | 2017-12-21 | 2017-12-21 | Gas-liquid material mixer and gas-liquid material mixing equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201721802601.XU CN207856693U (en) | 2017-12-21 | 2017-12-21 | Gas-liquid material mixer and gas-liquid material mixing equipment |
Publications (1)
Publication Number | Publication Date |
---|---|
CN207856693U true CN207856693U (en) | 2018-09-14 |
Family
ID=63465701
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201721802601.XU Active CN207856693U (en) | 2017-12-21 | 2017-12-21 | Gas-liquid material mixer and gas-liquid material mixing equipment |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN207856693U (en) |
-
2017
- 2017-12-21 CN CN201721802601.XU patent/CN207856693U/en active Active
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN103410718B (en) | The multi-function test stand of a kind of Liquid-Gas Jet Pump Perfqrmance and application | |
CN111346589B (en) | Micro-nano bubble gas-liquid reactor | |
CN208066329U (en) | A kind of microvesicle formula gas-liquid reactor and system | |
CN106474950A (en) | A kind of Liqiud-gas mixing device | |
CN105944511A (en) | Liquid seal draining U-shaped pipe | |
CN207856693U (en) | Gas-liquid material mixer and gas-liquid material mixing equipment | |
CN216703991U (en) | Gas-liquid mixing device for multiphase flow experiment | |
CN219423763U (en) | Can prevent rectifying column tower cauldron of dry combustion method | |
CN205913883U (en) | Horizontal gas -liquid separation | |
CN109675476B (en) | Two-phase bubble flow mixing device and method for bottom inlet of vertical rod bundle channel | |
CN107297160A (en) | A kind of steam-water mixing device with automatic drainage function | |
CN203978955U (en) | A kind of full automatic high efficiency miniature power energy-conserving and environment-protective vacuum system | |
CN204017541U (en) | The rotating knockout drum of a kind of new type auto stream | |
CN207401438U (en) | A kind of mixing arrangement for being used to produce motor vehicle antifreeze fluid | |
CN103754971B (en) | High-efficiency energy-saving thermal deaerator | |
CN215876914U (en) | Gas-liquid mixing device | |
CN203154669U (en) | Positive pressure type foam proportioning unit | |
CN203079704U (en) | Device for synthesizing superfine magnesium hydroxide flame retardant | |
CN205026794U (en) | Pressure stabilizing and water supplementing device | |
CN208449084U (en) | A kind of built-in agitating device | |
CN102049152B (en) | Novel external-power-free laminar flow water shearing device and water shearing method | |
CN203209062U (en) | Hydraulic reaction device | |
CN204637656U (en) | A kind of Horizontal oil-water separator | |
CN203916604U (en) | A kind of constant temperature granulation device of multicolor finish | |
CN104179729A (en) | Full-automatic efficient oligodynamic energy-saving and environment-friendly vacuum system |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant |