CN107694363A - A kind of material receiving device and conveying device for conveying solidliquid mixture - Google Patents
A kind of material receiving device and conveying device for conveying solidliquid mixture Download PDFInfo
- Publication number
- CN107694363A CN107694363A CN201710958930.1A CN201710958930A CN107694363A CN 107694363 A CN107694363 A CN 107694363A CN 201710958930 A CN201710958930 A CN 201710958930A CN 107694363 A CN107694363 A CN 107694363A
- Authority
- CN
- China
- Prior art keywords
- solid
- receiving device
- material receiving
- liquid
- conveying
- 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.)
- Granted
Links
- 239000000463 material Substances 0.000 title claims abstract description 45
- 239000000203 mixture Substances 0.000 title claims abstract description 34
- 239000007788 liquid Substances 0.000 claims abstract description 78
- 239000002245 particle Substances 0.000 claims abstract description 63
- 239000007787 solid Substances 0.000 claims abstract description 58
- 239000008187 granular material Substances 0.000 claims abstract description 12
- 239000006185 dispersion Substances 0.000 claims abstract description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 32
- 230000005484 gravity Effects 0.000 abstract description 7
- 238000001556 precipitation Methods 0.000 abstract description 3
- 239000000843 powder Substances 0.000 description 6
- 239000002002 slurry Substances 0.000 description 4
- 238000011010 flushing procedure Methods 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 238000005086 pumping Methods 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000002893 slag Substances 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/50—Mixing liquids with solids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/50—Mixing liquids with solids
- B01F23/56—Mixing liquids with solids by introducing solids in liquids, e.g. dispersing or dissolving
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/40—Static mixers
- B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
- B01F25/421—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions by moving the components in a convoluted or labyrinthine path
- B01F25/423—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions by moving the components in a convoluted or labyrinthine path by means of elements placed in the receptacle for moving or guiding the components
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/10—Maintenance of mixers
- B01F35/145—Washing or cleaning mixers not provided for in other groups in this subclass; Inhibiting build-up of material on machine parts using other means
- B01F35/1452—Washing or cleaning mixers not provided for in other groups in this subclass; Inhibiting build-up of material on machine parts using other means using fluids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/75—Discharge mechanisms
- B01F35/754—Discharge mechanisms characterised by the means for discharging the components from the mixer
- B01F35/7544—Discharge mechanisms characterised by the means for discharging the components from the mixer using pumps
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F2025/91—Direction of flow or arrangement of feed and discharge openings
- B01F2025/916—Turbulent flow, i.e. every point of the flow moves in a random direction and intermixes
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Dispersion Chemistry (AREA)
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
Abstract
The invention discloses a kind of material receiving device for conveying solidliquid mixture, including solid particle feed pipe, granule dispenser, solid-liquid blender and delivery pipe, solid-liquid blender is the tubular structure of top seal, the lower end of solid particle feed pipe at the top of solid-liquid blender by stretching into solid-liquid blender, the lower end that granule dispenser is arranged at solid particle feed pipe is used for the dispersion solid particle in solid-liquid blender, the side wall of solid-liquid blender is provided with feed liquor mesh, delivery pipe is from top entry to the tapered bend in one direction conical pipe of side outlet, the lower end of institute's solid-liquid blender and the top entry of delivery pipe connect, the charging aperture of solid particle feed pipe is the entrance of material receiving device, the side outlet of delivery pipe is the outlet of material receiving device.The device makes solidliquid mixture uniformly mix feeding Pulp pump and then realizes that material is stable to convey using the rapid precipitation and liquid of high specific gravity material in bend in one direction taper intraductal turbulance, avoids the generation of stifled pump.
Description
Technical field
The present invention relates to a kind of material receiving device of material and conveying device, more particularly to a kind of conveying solidliquid mixture
Material receiving device and conveying device.
Background technology
In the prior art, low-gravity solid particle, powder and aqueous mixtures (such as Iron Ore Powder, mine tailing, hydraulic coal mining, oxygen
Change alumina particles etc.) slurries conveying is used as means of delivery using horizontal or vertical slag slurry pump, and its effect, which can meet to convey, to be wanted
Ask.But above-mentioned means of delivery will such as convey to high specific gravity solid particle, powder (such as steel sand, steel ball, auriferous ore) slurries,
Then there is the features such as transfer efficiency is low, stability is poor.Tracing it to its cause predominantly, high specific gravity solid particle, powder be not in a liquid
State can be well mixed by (inlet flow rate for referring to pump is less than particle sinking speed) holding solid-liquid for a long time, even with agitator
Normal homogeneous feed status is extremely difficult to, there is also low concentration conveying sometimes, full liquid conveying (no solids occurs when serious
Conveying), it is final stifled pump phenomenon occur, cause certain difficulty for normal pumping.
The content of the invention
In order to overcome the above-mentioned deficiencies of the prior art, the invention provides it is a kind of convey solidliquid mixture material receiving device,
To solve the problems, such as high specific gravity solid particle with stifled pump phenomenon easily occurs during liquid blending transportation.
Technical solution of the present invention is as follows:It is a kind of convey solidliquid mixture material receiving device, including solid particle feed pipe,
Grain distributor, solid-liquid blender and delivery pipe, the solid-liquid blender are the tubular structure of top seal, and the solid particle enters
The lower end of expects pipe is arranged at the solid particle and entered by stretching into solid-liquid blender, the granule dispenser at the top of solid-liquid blender
The lower end of expects pipe is used for dispersion solid particle, the side wall of the solid-liquid blender in solid-liquid blender and is provided with feed liquor mesh, institute
It is from top entry to the tapered bend in one direction conical pipe of side outlet, the lower end of the solid-liquid blender and conveying to state delivery pipe
The top entry connection of pipe, the charging aperture of the solid particle feed pipe are the entrance of the material receiving device, the delivery pipe
Side outlet is the outlet of the material receiving device.
What is utilized due to material receiving device of the present invention is solid particle self gravitation and liquid in bend in one direction conical pipe
Turbulent flow solidliquid mixture is mixed and is smoothly entered pumping installations keeping more uniform, therefore in order to avoid material is in material feeding
The problem of solid-liquid layering occurs in device, further, the side outlet end of the axis of the bend in one direction conical pipe is whole
The minimum point of the axis of bend in one direction conical pipe.
Further, in order to strengthen the flowing of solidliquid mixture at the side outlet of bend in one direction conical pipe, avoid solid
Body particle is deposited at the side outlet of the bend in one direction conical pipe faster, and the bottom of the bend in one direction conical pipe is provided with
First pipeline, the interior side outlet pump liquid to the bend in one direction conical pipe of first pipeline.
Further, the granule dispenser includes umbrella shape diffusingsurface, the lower end output of the solid particle feed pipe
Solid particle is oriented to the side wall of the solid-liquid blender by the umbrella shape diffusingsurface.
Further, the granule dispenser includes being arranged at the umbrella hood above the umbrella shape diffusingsurface, the umbrella
Tapered channel is formed between shape cover and umbrella shape diffusingsurface.
Further, the material receiving device of the conveying solidliquid mixture includes being used for the water tank for holding liquid, the solid-liquid
Blender is arranged in water tank, and liquid is mixed by the mesh of the side wall of solid-liquid blender into the solid-liquid in the water tank
Device.
Further, including the second pipeline and water pump, the entrance of second pipeline are arranged at the bottom of the water tank, institute
State the outlet of the second pipeline and the entrance of water pump connects, the outlet of the water pump is connected with the first pipeline.
Further, the outlet of the water pump is connected with the 3rd pipeline, and the outlet of the 3rd pipeline is entered with solid particle
Expects pipe connects.
Another technical scheme of the present invention is a kind of conveying device for conveying solidliquid mixture, including above-mentioned material receiving device
And Pulp pump, the outlet of the material receiving device and the entrance of Pulp pump connect.
The advantages of technical scheme provided by the present invention, is:Main the characteristics of make use of high specific gravity material itself, pass through
Bend in one direction conical pipe directly exports the solid particle of rapid precipitation, and accelerates hair in bend in one direction conical pipe using liquid
Raw turbulent flow is formed to solid particle to be disturbed, and effectively prevent separation of the solidliquid mixture in receiver.Receiver exports and slag
Stock pump entrance is directly connected to, coordinate Pulp pump realize stabilization, it is reliable, equably high specific gravity slurry is conveyed, there is knot
The characteristics of structure is simple, reliable, energy-conservation, it is not necessary to it is another set agitator and can be achieved with normally convey high specific gravity material block up pump without generation
Problem.
Brief description of the drawings
Fig. 1 is the structural representation of the conveying device of present invention conveying solidliquid mixture.
Embodiment
With reference to embodiment, the invention will be further described, but not as a limitation of the invention.
It refer to shown in Fig. 1, conveying the conveying device of solidliquid mixture includes Pulp pump 1 and material receiving device 2, material receiving device
2 outlet is connected with the entrance of Pulp pump 1 by flange.Material receiving device 2 include solid particle feed pipe 3, granule dispenser 4,
Solid-liquid blender 5 and delivery pipe 6, in addition to water tank 7, water pump 8, the first pipeline 9, the second pipeline 10 and the 3rd pipeline 11.
Solid particle feed pipe 3 is the addition passage of solid particle, and its arrival end sets flow regulator 12 to be used to control
The number of solid particle.Solid particle is concentrated in feed bin, and feed bin is connected with solid particle feed pipe 3, passes through flow regulator
12 regulation enters solid-liquid blender 5 from the lower end of solid particle feed pipe 3.
Solid-liquid blender 5 is the tubular structure of top seal, and its side wall uniformly opens up some feed liquor mesh 13, is formed equal
Even liquid inlet channel.The lower end of solid particle feed pipe 3 is connected with granule dispenser 4, and by the top of solid-liquid blender 5
Stretch into solid-liquid blender 5.Solid particle backwardness under the lower end of solid particle feed pipe 3 is dispersed in by granule dispenser 4
In solid-liquid blender 5.The effect of granule dispenser 4 is to be used to dispersion solid particle, its structure in solid-liquid blender 5 include umbrella
Shape diffusingsurface and the umbrella hood being arranged above umbrella shape diffusingsurface, tapered channel is formed between umbrella hood and umbrella shape diffusingsurface.
The lower end that the structure also is understood as solid particle feed pipe 3 is horn-like for opening, in horn-like one taper of middle setting
Baffle element.Stop from the solid particle that the lower end of solid particle feed pipe 3 is fallen by taper baffle element i.e. umbrella shape diffusingsurface, and to
Surrounding is disperseed, and solid particle is mixed together whereabouts with the liquid entered from feed liquor mesh 13 close to the side wall of solid-liquid blender 5.
Because liquid is to enter solid-liquid blender 5, therefore the liquid of the side wall close to solid-liquid blender 5 from the side wall of solid-liquid blender 5
Flow velocity is larger, solid particle mixed herein with liquid compared to solid particle be directly entered liquid can more carry out it is sufficiently uniformly mixed
Close.
The lower end connection of solid-liquid blender 5 is delivery pipe 6, and it is connected with the top entry of delivery pipe 6.Delivery pipe 6 is
From top entry 14 to the tapered bend in one direction conical pipe of side outlet 15, what is utilized due to material receiving device 2 of the present invention is solid
The turbulent flow of particle self gravitation and liquid in bend in one direction conical pipe makes solidliquid mixture keep more uniform mixing simultaneously
Smoothly enter pumping installations, therefore in order to avoid the problem of solid-liquid is layered, bend in one direction taper occur in material receiving device 2 for material
The side outlet end of the axis of pipe is the minimum point of the axis of whole bend in one direction conical pipe.That is bend in one direction conical pipe
Latter end horizontal segment is not set, avoid solidliquid mixture in horizontal segment because flow rate of liquid is inadequate, and solid particle
Precipitation is very fast to form layering.The side outlet 15 of bend in one direction conical pipe is the outlet for forming material receiving device 2, directly and Pulp pump
1 entrance connects, and on the one hand solidliquid mixture sucks the pump housing by the suction formed of Pulp pump 1, another convenience relies on solid particle
Self gravitation, the curved surface of bend in one direction conical pipe is coordinated directly to slide to the pump housing,
In other the present embodiment, material receiving device 2 is provided with water tank 7 for holding liquid, at the same for convenience liquid from
The side wall of solid-liquid blender 5 enters solid-liquid blender 5, solid-liquid blender 5 is arranged in water tank 7, delivery pipe 6 is also disposed at water
In case, the side outlet 15 of delivery pipe 6 is then arranged on the side wall of water tank 7 close to the position of bottom.In order to strengthen bend in one direction taper
The flowing of solidliquid mixture at the side outlet 15 of pipe, avoids solid particle from being deposited in the bend in one direction conical pipe faster
At side outlet 15, the outlet of the first pipeline 9 is arranged on the bottom of bend in one direction conical pipe.In order to avoid solid particle is from solid-liquid
Blender 5 sheds, and falls into the bottom of water tank 7 and is precipitated, the entrance of the second pipeline 10 is arranged to the bottom of water tank 7, in addition will
The outlet of 3rd pipeline 11 is connected with solid particle feed pipe 3.The entrance of first pipeline 9 and the 3rd pipeline 11 goes out with water pump 8
Mouthful connection, the outlet of the entrance of water pump 8 then with the second pipeline 10 is connected.Therefore water pump 8 can directly draw the bottom liquid of water tank 7 simultaneously
It is pumped into bottom and the solid particle feed pipe 3 of bend in one direction conical pipe.In the first pipeline 9, the second pipeline 10 and
The first valve 16, the second valve 17 and the 3rd valve 18 is set to enter on demand to control the passage of each pipeline on three pipelines 11 respectively
Row rinses.
The solidliquid mixture conveying of the present apparatus and flushing process are such:Solid particle or powder enter from solid particle
Expects pipe 3 flows into solid-liquid blender 5 through flow regulator 12, and liquid enters from the side wall of solid-liquid blender 5, in solid-liquid blender 5
Interior solid particle mixes with liquid, material is uniformly mixed together into delivery pipe 6 by the self gravitation of material, works as mixing
During nearly 6 bottom of delivery pipe of logistics mixture enters in pump quickly in the presence of the attraction of Pulp pump 1, in the centrifugal force of pump
The lower mixture of effect is transported to pump discharge, so as to realize whole course of conveying.
Due to consideration that the proportion of particle or powder is larger, the particle or powder settling velocity into delivery pipe 6 are very fast, because
This can be rinsed operation with reference to each valve using water pump 8, the first pipeline 9, the second pipeline 10 and the 3rd pipeline 11 and place
Stifled pump.Water pump 8 is through the second valve 17 from the drawing wash liquid of the second pipeline 10;Enter the first valve through pump discharge in the presence of water pump 8
16 and first pipeline 9 and enter delivery pipe 6 bottom and realize flushing process, while another way flushing liquor is through the 3rd valve 18 and the 3rd pipe
Road 11 enters solid particle feed pipe 3 and granule dispenser 4 is rinsed, and the 3rd valve can be closed when such as need not normally rinse
18, the pump of water 8 is only rinsed to the bottom of delivery pipe 6.
Claims (9)
- A kind of 1. material receiving device for conveying solidliquid mixture, it is characterised in that:Including solid particle feed pipe, granule dispenser, Solid-liquid blender and delivery pipe, the solid-liquid blender is the tubular structure of top seal, under the solid particle feed pipe By stretching into solid-liquid blender at the top of solid-liquid blender, the granule dispenser is arranged under the solid particle feed pipe at end Hold in solid-liquid blender dispersion solid particle, the side wall of the solid-liquid blender be provided with feed liquor mesh, the delivery pipe It is from top entry to the tapered bend in one direction conical pipe of side outlet, the lower end of the solid-liquid blender and the top of delivery pipe Entrance connects, and the charging aperture of the solid particle feed pipe is the entrance of the material receiving device, the side outlet of the delivery pipe For the outlet of the material receiving device.
- A kind of 2. material receiving device for conveying solidliquid mixture according to claim 1, it is characterised in that:The bend in one direction The side outlet end of the axis of conical pipe is the minimum point of the axis of whole bend in one direction conical pipe.
- A kind of 3. material receiving device for conveying solidliquid mixture according to claim 1, it is characterised in that:The bend in one direction The bottom of conical pipe is provided with the first pipeline, and the interior side outlet to the bend in one direction conical pipe of first pipeline pumps liquid Body.
- A kind of 4. material receiving device for conveying solidliquid mixture according to claim 1, it is characterised in that:The particle distribution Device includes umbrella shape diffusingsurface, and the solid particle of the lower end output of the solid particle feed pipe is oriented to institute by the umbrella shape diffusingsurface State the side wall of solid-liquid blender.
- A kind of 5. material receiving device for conveying solidliquid mixture according to claim 4, it is characterised in that:The particle distribution Device includes being arranged at the umbrella hood above the umbrella shape diffusingsurface, and taper is formed between the umbrella hood and umbrella shape diffusingsurface and is led to Road.
- A kind of 6. material receiving device for conveying solidliquid mixture according to claim 3, it is characterised in that:The conveying solid-liquid The material receiving device of mixture includes being used for the water tank for holding liquid, and the solid-liquid blender is arranged in water tank, in the water tank Liquid enters the solid-liquid blender by the mesh of the side wall of solid-liquid blender.
- A kind of 7. material receiving device for conveying solidliquid mixture according to claim 6, it is characterised in that:Including the second pipeline And water pump, the entrance of second pipeline are arranged at the bottom of the water tank, the outlet of second pipeline and the entrance of water pump Connection, the outlet of the water pump is connected with the first pipeline.
- A kind of 8. material receiving device for conveying solidliquid mixture according to claim 7, it is characterised in that:The water pump goes out Mouth is connected with the 3rd pipeline, and the outlet of the 3rd pipeline is connected with solid particle feed pipe.
- A kind of 9. conveying device for conveying solidliquid mixture, it is characterised in that:Including any one in Pulp pump and claim 1-8 The material receiving device of conveying solidliquid mixture described in, the outlet of the material receiving device and the entrance of Pulp pump connect.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201710958930.1A CN107694363B (en) | 2017-10-16 | 2017-10-16 | Material receiving device for conveying solid-liquid mixture and conveying device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201710958930.1A CN107694363B (en) | 2017-10-16 | 2017-10-16 | Material receiving device for conveying solid-liquid mixture and conveying device |
Publications (2)
Publication Number | Publication Date |
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CN107694363A true CN107694363A (en) | 2018-02-16 |
CN107694363B CN107694363B (en) | 2023-12-12 |
Family
ID=61183832
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201710958930.1A Active CN107694363B (en) | 2017-10-16 | 2017-10-16 | Material receiving device for conveying solid-liquid mixture and conveying device |
Country Status (1)
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Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1347614A (en) * | 1971-09-23 | 1974-02-27 | Otto & Co Gmbh Dr C | Apparatus for conveying pellets |
JPH10249179A (en) * | 1997-03-14 | 1998-09-22 | Nippon Oil Co Ltd | Mixing device |
CN1438961A (en) * | 2000-06-28 | 2003-08-27 | 齐柏林料仓和设备技术有限公司 | Method for conveying solid substance |
CN101480266A (en) * | 2008-05-30 | 2009-07-15 | 内蒙古伊利实业集团股份有限公司 | Granule-adding method and device for granule-containing liquid drink processing technique |
CN101480267A (en) * | 2008-05-30 | 2009-07-15 | 内蒙古伊利实业集团股份有限公司 | Method for producing granule-containing liquid drink |
CN102698625A (en) * | 2012-07-04 | 2012-10-03 | 中国石油大学(华东) | High-pressure rotational flow mixing device |
CN203291791U (en) * | 2013-04-13 | 2013-11-20 | 淄博王煤矿业有限公司 | Preparing and conveying self-service integrated equipment of slurry material |
CN206027469U (en) * | 2016-08-31 | 2017-03-22 | 蔚林新材料科技股份有限公司 | System for powder material dissolves with liquid mixing |
CN207385228U (en) * | 2017-10-16 | 2018-05-22 | 江苏鑫华能环保工程股份有限公司 | A kind of material receiving device and conveying device for conveying solidliquid mixture |
-
2017
- 2017-10-16 CN CN201710958930.1A patent/CN107694363B/en active Active
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1347614A (en) * | 1971-09-23 | 1974-02-27 | Otto & Co Gmbh Dr C | Apparatus for conveying pellets |
JPH10249179A (en) * | 1997-03-14 | 1998-09-22 | Nippon Oil Co Ltd | Mixing device |
CN1438961A (en) * | 2000-06-28 | 2003-08-27 | 齐柏林料仓和设备技术有限公司 | Method for conveying solid substance |
CN101480266A (en) * | 2008-05-30 | 2009-07-15 | 内蒙古伊利实业集团股份有限公司 | Granule-adding method and device for granule-containing liquid drink processing technique |
CN101480267A (en) * | 2008-05-30 | 2009-07-15 | 内蒙古伊利实业集团股份有限公司 | Method for producing granule-containing liquid drink |
CN102698625A (en) * | 2012-07-04 | 2012-10-03 | 中国石油大学(华东) | High-pressure rotational flow mixing device |
CN203291791U (en) * | 2013-04-13 | 2013-11-20 | 淄博王煤矿业有限公司 | Preparing and conveying self-service integrated equipment of slurry material |
CN206027469U (en) * | 2016-08-31 | 2017-03-22 | 蔚林新材料科技股份有限公司 | System for powder material dissolves with liquid mixing |
CN207385228U (en) * | 2017-10-16 | 2018-05-22 | 江苏鑫华能环保工程股份有限公司 | A kind of material receiving device and conveying device for conveying solidliquid mixture |
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