CN106241381A - A kind of solid particle pipe riser - Google Patents
A kind of solid particle pipe riser Download PDFInfo
- Publication number
- CN106241381A CN106241381A CN201610638885.7A CN201610638885A CN106241381A CN 106241381 A CN106241381 A CN 106241381A CN 201610638885 A CN201610638885 A CN 201610638885A CN 106241381 A CN106241381 A CN 106241381A
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- CN
- China
- Prior art keywords
- solid particle
- solid
- liquid
- pipe riser
- transport 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.)
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65G—TRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
- B65G53/00—Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
- B65G53/30—Conveying materials in bulk through pipes or tubes by liquid pressure
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
Abstract
The invention discloses a kind of solid particle pipe riser, including liquid medium, transport pipeline, solid-liquid mixer and equipment for separating liquid from solid.The transport pipeline of device of the present invention uses closed circuit, with liquid medium as carrier, it is achieved the lifting operation to solid particle；According to different solid particle attributes, choose liquid mediums material, it is achieved efficient, the Pipeline lift process of environmental protection.The present invention greatly reduces the hardware requirement of solid particle Pipeline lift, reduces solid particle pipeline conveying energy consumption, improves raising efficiency, is particularly suitable for the Pipeline lift operation of the solid particle of big density, specific properties.
Description
Technical field
The present invention relates to solid particle pipeline transportation art, be specially a kind of solid particle pipe riser.
Background technology
Solid particle Pipeline lift is a kind of efficient, convenient, solid particle mode of movement of environmental protection.Lifting system typically with
Water or air are carrier, use current or the air driven Motion of solid particle of high-speed motion, it is achieved the lifting of solid particle,
The field important roles such as industry coal mining, Deep Sea Minerals exploitation.
Use the carrier that water or air promote as solid particle, especially for big density, the solid of specific properties
Grain promotes, and needs water or the air of very big flow velocity, produces huge energy consumption, promotes system effectiveness extremely low；Current at a high speed or air-flow
High to promoting system hardware equipment requirements, need, by special process, lifting means is carried out processing.Use is opened more
Put formula Pipeline lift system, for the carrier water after having carried or the discharge of air, process even across solid-liquid separation, to ring
Still there is huge pollution in border.
Therefore, those skilled in the art is devoted to develop a kind of solid particle pipe riser, it is achieved reduction energy consumption,
Improve efficiency and the Pipeline lift operation of protection environment.
Summary of the invention
Because the drawbacks described above of prior art, the technical problem to be solved is how to realize that energy consumption is little, effect
Rate is high and eco-friendly solid particle Pipeline lift operation.
For achieving the above object, the invention provides a kind of solid particle pipe riser, including liquid medium, transport
Pipeline, solid-liquid mixer and equipment for separating liquid from solid, described transport pipeline is configured to closed-loop arrangement, and described liquid is situated between
Matter is configured to close flow in described transport pipeline, has density contrast and mutual differences in viscosity with the solid particle promoted.
Further, described liquid medium is liquid mercury or water.
Further, described transport pipeline is steel pipe.
Further, it is characterised in that described steel pipe diameter 0.2m, duct height is 20m.
Further, the solid particle volumetric concentration of the solidliquid mixture in described transport pipeline is less than 10%.
Further, described solid-liquid mixer includes check valve and mixer.
Further, described equipment for separating liquid from solid includes filter.
Further, described transport pipeline, solid-liquid mixer and equipment for separating liquid from solid flange closure connect.
Further, described mixer is configured to according to injecting solid particle rate adaptation stir speed (S.S.).
Further, described filter is configured to the volumetric concentration regulation rate of departure according to solid particle.
This device uses the special liquid with particular density and viscosity as delivery vehicles, uses and adapts to special liquid
After solid particle to be conveyed is mixed with special liquid by solid-liquid mixer, inject the circulating line adapting to special liquid, pass through
The equipment for separating liquid from solid adapting to special liquid extracts solid particle, and the special liquid of isolated is refilled circulation pipe
In road, carry out solid particle conveying next time.
The present invention is directed to the deficiencies in the prior art, design provides a kind of solid particle pipe riser, including: special liquid
The solid-liquid of body, the circulating line of adaptation special liquid, the solid-liquid mixer adapting to special liquid and adaptation special liquid divides
From device.Described special liquid is enclosed within circulating line, adapts to solid-liquid mixer and the equipment for separating liquid from solid of special liquid
It is connected with the circulating line adapting to special liquid respectively, forms closed circulation.
This apparatus structure is simple, definite functions, can select different special liquid according to solid particle different attribute, greatly
Reduce solid particle Pipeline lift system energy consumption, improve raising efficiency.This device uses closed cycle system, it is achieved no pollution,
Environmental friendliness.
Below with reference to accompanying drawing, the technique effect of design, concrete structure and the generation of the present invention is described further, with
It is fully understood from the purpose of the present invention, feature and effect.
Accompanying drawing explanation
Fig. 1 is the device schematic diagram of a preferred embodiment of the present invention.
Detailed description of the invention
As it is shown in figure 1, the ultimate principle of the present invention is the special liquid utilizing particular density and viscosity realizes solid particle
Pipeline lift.This invention efficiently solves big density, the problem of specific properties solid particle pipeline conveying, reduces system energy
Consumption, improves raising efficiency.
In implementation process, first solid particle is injected in the solid-liquid mixer 1 adapting to special liquid；Pass through solid-liquid
Mixing arrangement 1 is sufficiently mixed solid particle to be hoisted and special liquid；Solidliquid mixture is injected the circulation adapting to special liquid
Pipeline 2；By adapting to the equipment for separating liquid from solid 3 of special liquid, isolated also exports solid particle, and by special liquid again
Inject circulating line 2.The most constantly circulation, it is achieved solid particle Pipeline lift.Utilize and be situated between more than the liquid of density of solid particles
Matter promotes solid particulate matter.
One preferred embodiment of the present invention is such as: on ground, land, utilizes liquid mercury to promote manganese ore.
With hydrargyrum (density 13600kg/m3) it is liquid medium, carry out manganese ore mining operations on land, to the manganese ore after crushing
Stone granule (density 4700kg/m3, particle size about 0.01m～0.05m) promote.Transport pipeline is high intensity, wear-resisting, resistance to
Compressed steel matter pipe, diameter 0.2m, duct height is 20m；In pipeline, the volumetric concentration of solid particle is less than 10%；Solid-liquid mixes
Device can bear highly pressurised liquid environment, device strict seal, and granule inlet uses check valve, prevents hydrargyrum from leaking；Solid-liquid mixes
Locking device is provided with high-power mixing stirring device, can be according to injecting particle velocity regulation stir speed (S.S.)；Equipment for separating liquid from solid is strict
Seal, and the rate of departure can be regulated according to the volumetric concentration of manganese ore, use special filtration means output ore particles and do not produce
Raw leaked liquid.Each parts carry out closing connection by flange, and carry out strict closed processes.
Lifting process by controlling manganese ore input rate, solid-liquid mixing rate, thus can control in conveying pipe
The concentration of manganese ore and the throughput of Ore.The strict sealing property controlling lifting system entirety in lifting process.Due to
The density contrast of liquid and solid is relatively big, therefore can be promoted by Ore buoyancy in a liquid, reduces in lifting process
Energy consumption.Integrated piping lifting device is isolated from the outside, and substantially accomplishes zero environmental.
Another embodiment, it is simply that the mineral promoting density less than water with the liquid (such as water) of common density (such as may be used
Combustion ice).
The preferred embodiment of the present invention described in detail above.Should be appreciated that the ordinary skill of this area is without wound
The property made work just can make many modifications and variations according to the design of the present invention.Therefore, all technical staff in the art
The most on the basis of existing technology by the available technology of logical analysis, reasoning, or a limited experiment
Scheme, all should be in the protection domain being defined in the patent claims.
Claims (10)
1. a solid particle pipe riser, it is characterised in that include liquid medium, transport pipeline, solid-liquid mixer
And equipment for separating liquid from solid, described transport pipeline is configured to closed-loop arrangement, and described liquid medium is configured to described
Close flow in transport pipeline, has density contrast and mutual differences in viscosity with the solid particle promoted.
2. solid particle pipe riser as claimed in claim 1, it is characterised in that described liquid medium be liquid mercury or
Water.
3. solid particle pipe riser as claimed in claim 1, it is characterised in that described transport pipeline is steel circle
Pipe.
4. solid particle pipe riser as claimed in claim 3, it is characterised in that described steel pipe diameter 0.2m,
Duct height is 20m.
5. solid particle pipe riser as claimed in claim 1, it is characterised in that the solid-liquid in described transport pipeline mixes
The solid particle volumetric concentration of compound is less than 10%.
6. solid particle pipe riser as claimed in claim 1, it is characterised in that described solid-liquid mixer includes list
To valve and mixer.
7. solid particle pipe riser as claimed in claim 1, it is characterised in that described equipment for separating liquid from solid included
Filter.
8. solid particle pipe riser as claimed in claim 1, it is characterised in that described transport pipeline, solid-liquid mix
Device and equipment for separating liquid from solid flange closure connect.
9. solid particle pipe riser as claimed in claim 6, it is characterised in that described mixer is configured to
According to injecting solid particle rate adaptation stir speed (S.S.).
10. solid particle pipe riser as claimed in claim 7, it is characterised in that described filter is configured to root
The rate of departure is regulated according to the volumetric concentration of solid particle.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610638885.7A CN106241381A (en) | 2016-08-05 | 2016-08-05 | A kind of solid particle pipe riser |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610638885.7A CN106241381A (en) | 2016-08-05 | 2016-08-05 | A kind of solid particle pipe riser |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106241381A true CN106241381A (en) | 2016-12-21 |
Family
ID=58078929
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610638885.7A Pending CN106241381A (en) | 2016-08-05 | 2016-08-05 | A kind of solid particle pipe riser |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106241381A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115228351A (en) * | 2022-07-29 | 2022-10-25 | 中南大学 | Integrated solid-liquid mixing-separating device and using method thereof |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3612615A (en) * | 1969-09-30 | 1971-10-12 | Water R Allen | Continuous hydraulic ore hoisting system |
| JPS58212524A (en) * | 1982-06-04 | 1983-12-10 | Hitachi Ltd | Horizontal hydro-hoist |
| JPS61119515A (en) * | 1984-11-15 | 1986-06-06 | Takeshi Hayashi | Solid material carrier |
| CN2245046Y (en) * | 1995-11-14 | 1997-01-15 | 淮南矿业学院 | Cyclic permutation type solid particulate material injection device |
| CN201983555U (en) * | 2011-02-21 | 2011-09-21 | 武汉星田热环境控制技术有限公司 | Hydraulic ice conveying system |
-
2016
- 2016-08-05 CN CN201610638885.7A patent/CN106241381A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3612615A (en) * | 1969-09-30 | 1971-10-12 | Water R Allen | Continuous hydraulic ore hoisting system |
| JPS58212524A (en) * | 1982-06-04 | 1983-12-10 | Hitachi Ltd | Horizontal hydro-hoist |
| JPS61119515A (en) * | 1984-11-15 | 1986-06-06 | Takeshi Hayashi | Solid material carrier |
| CN2245046Y (en) * | 1995-11-14 | 1997-01-15 | 淮南矿业学院 | Cyclic permutation type solid particulate material injection device |
| CN201983555U (en) * | 2011-02-21 | 2011-09-21 | 武汉星田热环境控制技术有限公司 | Hydraulic ice conveying system |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115228351A (en) * | 2022-07-29 | 2022-10-25 | 中南大学 | Integrated solid-liquid mixing-separating device and using method thereof |
| CN115228351B (en) * | 2022-07-29 | 2023-10-17 | 中南大学 | Integrated solid-liquid mixing-separating device and application method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20161221 |
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| RJ01 | Rejection of invention patent application after publication |