CN109279256A - Washed-out sand multichannel depiler - Google Patents
Washed-out sand multichannel depiler Download PDFInfo
- Publication number
- CN109279256A CN109279256A CN201811262206.6A CN201811262206A CN109279256A CN 109279256 A CN109279256 A CN 109279256A CN 201811262206 A CN201811262206 A CN 201811262206A CN 109279256 A CN109279256 A CN 109279256A
- Authority
- CN
- China
- Prior art keywords
- pylon
- washed
- material tank
- sub
- sand
- 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
- 239000004576 sand Substances 0.000 title claims abstract description 38
- 206010016256 fatigue Diseases 0.000 title claims abstract description 21
- 239000000463 material Substances 0.000 claims abstract description 19
- 239000012530 fluid Substances 0.000 claims description 6
- 238000005096 rolling process Methods 0.000 claims description 2
- 238000005406 washing Methods 0.000 abstract description 4
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 abstract description 2
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 229910052710 silicon Inorganic materials 0.000 abstract description 2
- 239000010703 silicon Substances 0.000 abstract description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 40
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- 239000000377 silicon dioxide Substances 0.000 description 4
- 238000005265 energy consumption Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000003321 amplification Effects 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000003199 nucleic acid amplification method Methods 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
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
- B65G11/00—Chutes
- B65G11/02—Chutes of straight form
-
- 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
- B65G65/00—Loading or unloading
- B65G65/28—Piling or unpiling loose materials in bulk, e.g. coal, manure, timber, not otherwise provided for
-
- 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
- B65G2201/00—Indexing codes relating to handling devices, e.g. conveyors, characterised by the type of product or load being conveyed or handled
- B65G2201/04—Bulk
- B65G2201/045—Sand, soil and mineral ore
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
- Air Transport Of Granular Materials (AREA)
Abstract
The present invention relates to one kind to wash husky equipment, i.e. a kind of washed-out sand multichannel depiler, including conveyance conduit (1) and pylon (4), its main feature is that: the pylon (4) has multiple, the end of the conveyance conduit (1) connects with the entrance of a sub-material tank (2), it is equipped with more dispensings around sub-material tank (2) and manages (3), each dispensing pipe (3) communicates with a pylon (4).The beneficial effect is that: washed-out sand can be distributed to stock ground everywhere, reach piling height, and do not have to loading machine, significantly reduce carrying cost, and structure is simple, it is low in cost, it is expected to the indispensable facility as silicon sand washing choosing industry.
Description
Technical field
The present invention relates to one kind to wash husky equipment, i.e., a kind of washed-out sand multichannel depiler.
Background technique
Natural silica Sand obtains industrial sand by washing removal impurity, and industrial sand will be sent to stock ground and stack storage before selling
It deposits.From washed-out sand workshop end to washed-out sand conveyance conduit is equipped with stock ground, washed-out sand is sent to by pipeline by stock ground.Due to product volume
Greatly, in order to save land used and convenient for transhipment, the washed-out sand in stock ground will accumulate very high as far as possible.In addition, washed-out sand is mixed into water
Flow-like is conveyed, and needs to carry out girt-water separation by seperator after being sent to stock ground.Therefore, up to ten numbers are equipped in stock ground
Rice pylon, pylon upper end equipped with rotation extension set, conveyance conduit water sand mixture out of, workshop is sent to rotation extension set, big portion
Moisture, which is separated and passes through return pipe, sends water source back to, and the finished sand through being dehydrated is put down from drain hole.Due to the sky below pylon
Between it is limited, the washed-out sand of releasing will also by loading machine to surrounding send.The workload for sending washed-out sand is very big, and one medium scale
Stock ground is also required to several loading machines and works continuously.In addition loading machine inconvenient walking on sandy ground, energy consumption is very high, and efficiency is very low, adds
Big production cost.
Summary of the invention
The object of the present invention is to provide one kind washed-out sand can be distributed to stock ground everywhere, and realizes that specified accumulation is high
Degree, and loading machine is used no or little, reduce the washed-out sand multichannel depiler that cost is stacked in washed-out sand.
Above-mentioned purpose is realized by the following technical solutions: propose a kind of washed-out sand multichannel depiler, including conveyance conduit and
Pylon, its main feature is that: the pylon has multiple, and the end of the conveyance conduit connects with the entrance of a sub-material tank, sub-material tank
Surrounding is equipped with more dispensings pipes, and each Guan Yuyi pylon of dispensing communicates.
Homocline frame is added in the sub-material tank, homocline frame has the column being fixedly connected with sub-material tank, and the upper end of the column is equipped with
The middle part of the fluid dividing cover of one taper, column connects a balanced ball by rolling bearing.
The beneficial effects of the present invention are: washed-out sand can be distributed to stock ground everywhere, reach piling height, and does not have to load
Machine significantly reduces carrying cost, and structure is simple, low in cost, it is expected to the indispensable facility as silicon sand washing choosing industry.
Detailed description of the invention
Fig. 1 is the main view of the first embodiment；
Fig. 2 is the top view of the first embodiment；
Fig. 3 is the use state main view of the first embodiment；
Fig. 4 is the use state top view of the first embodiment；
Fig. 5 is the top view of second of embodiment；
Fig. 6 is the main view of the third embodiment；
Fig. 7 is the top view of the third embodiment.
Visible in figure: conveyance conduit 1, sub-material tank 2 send pipe 3, and pylon 4 divides spigot 5, drain hole 6, return pipe 7, homocline
Frame 8, column 9, balanced ball 10, fluid dividing cover 11.
The first embodiment: Fig. 1, Fig. 2 illustrate a kind of washed-out sand multichannel depiler, in figure as it can be seen that have one from washing husky vehicle
Between end pick out come conveyance conduit 1, conveyance conduit 1 be equipped with delivery pump do not drawn in figure because belonging to conventional equipment.It is defeated
It send the end of pipeline 1 and the entrance of a sub-material tank 2 to connect, more dispensing pipes 3 is equipped with around sub-material tank 2.It can in conjunction with Fig. 3
See, each dispensing pipe 3 is communicated with a pylon 4.Here pylon 4 is also a kind of conventional pylon 4, and height will be more than sand heap
Height, the stock ground of general scale, sand heap is up to 20m, and the height of pylon will reach 22m or more.The installation of pylon upper end divides spigot
5, dispensing pipe 3 is upwardly extended along pylon, is above terminated to cyclone separator entrance, is equipped with drain hole 6 below cyclone separator, side picks out return water
Pipe 7.
In conjunction with Fig. 4 as it can be seen that pylon 4 has multiple, it is distributed in stock ground.When work, delivery pump is started by delivery pipe 1
The silica sand selected shifts sub-material tank 2 onto together with water, then be sent to each pylon from each dispensing pipe 3 divide spigot 5.Divide spigot big
Partial water is separated, and sends original place back to by return pipe 7, is recycled.The silica sand separated is released from drain hole 6, heap
Product is around pylon.Since pylon multiple spot is distributed, what silica sand can be relatively uniform is deposited in stock ground, thus the loading machine omitted
Transport process.Through experimental results demonstrate, on long 300m, wide 100 meters of stock ground, scraper cost of this mode than loading machine
60% or more is reduced, there is significant economic benefit.
Second of embodiment: it is improved on the basis of the first embodiment.As shown in figure 5, each dispensing pipe 3 is all towards powder
The side of batch can extends, and this mode, sub-material tank 2 can be located at the side in stock ground, and the centre without being placed on stock ground, powder material tank accounts for
Ground area is smaller, and the sand heap accumulated can join together, and can preferably utilize place, store more products.
The third embodiment: improving on the basis of previous embodiment, mainly solves asking for each dispensing tube efficiency unevenness
Topic.In previous embodiment, the internal resistance of each dispensing pipe is difficult unanimously, and because parallel with one another, fluid is by the pipeline small to resistance
It concentrates, fraction of internal resistance difference can all form very big difference in flow.Therefore, the fortune sand amount of each dispensing pipe of previous embodiment is very different
It causes, the sand drift that heap goes out is not perfectly flat whole, cannot make full use of the space in stock ground.In order to solve this problem, it is necessary to increase conveying
The discharge pressure of pipeline.Under conditions of discharge pressure abundance or even surplus, the big pipeline internal resistance amplification of flow is increased, Cai Nengke
It takes that each dispensing pipe internal resistance is poor, makes each entrance can work at full capacity.Obviously, energy consumption certainly will be increased by doing so, and
It is difficult to control, needs to be aided with the balance that secondary transhipment is just able to maintain sand drift height toward contact.
In order to solve above-mentioned problem, this example has added homocline frame 8 in sub-material tank 2.As shown in Figure 6, Figure 7, homocline frame 8 has
One column 9 being fixedly connected with sub-material tank, 9 upper end of column are equipped with the fluid dividing cover 11 of a taper, and the middle part of column 9 is hinged one
Balanced ball 10.
When work, washed-out sand and water directly fall in the tip of fluid dividing cover 11 from the entrance suitable for reading of sub-material tank, then to week
Diffusion is enclosed, then is sent out from each dispensing pipe 3.If the flow of each dispensing pipe is relatively uniform, balanced ball uniform rotation.If each
The mass flow discrepancy of a dispensing pipe, and be more than certain value, then balanced ball 10 will go to point of maximum flow with maximum flow of water
Tube inlet is sent, makes the flow of this entrance by certain obstruction, the flow of the entrance of other dispensing pipes just will increase, and pass through this
The equilibrium for adjusting each flow for sending pipe will be opposite of sample, the sand drift accumulated also can be just consistent, and reduction is transported again
Workload, even completely eliminated secondary transhipment, the capacity in stock ground is fully utilized.
Claims (2)
1. a kind of washed-out sand multichannel depiler, including conveyance conduit (1) and pylon (4), it is characterised in that: the pylon (4) has more
A, the end of the conveyance conduit (1) connects with the entrance of a sub-material tank (2), and more dispensing pipes are equipped with around sub-material tank (2)
(3), each dispensing pipe (3) communicates with a pylon (4).
2. washed-out sand multichannel depiler according to claim 1, it is characterised in that: add homocline frame in the sub-material tank (2)
(8), homocline frame (8) has the column (9) being fixedly connected with sub-material tank (2), and column (9) upper end is equipped with the fluid dividing cover of a taper
(11), the middle part of column (9) connects a balanced ball (10) by rolling bearing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811262206.6A CN109279256B (en) | 2018-10-27 | 2018-10-27 | Sand washing multipath distributor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811262206.6A CN109279256B (en) | 2018-10-27 | 2018-10-27 | Sand washing multipath distributor |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN109279256A true CN109279256A (en) | 2019-01-29 |
| CN109279256B CN109279256B (en) | 2024-04-26 |
Family
ID=65177550
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811262206.6A Active CN109279256B (en) | 2018-10-27 | 2018-10-27 | Sand washing multipath distributor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109279256B (en) |
Citations (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR921047A (en) * | 1946-02-01 | 1947-04-24 | Pesco Products Company | Improvements to flow rate equalization devices |
| GB1159307A (en) * | 1967-04-25 | 1969-07-23 | Young Machinery Company Inc | Solids Flow Rate Equalizer |
| KR200254373Y1 (en) * | 2001-08-24 | 2001-11-24 | 배종호 | Intermediate Tank of Sand Pump Line |
| CN101907185A (en) * | 2009-06-08 | 2010-12-08 | 正大能源材料(大连)有限公司 | Multichannel slurry distributor |
| CN203370636U (en) * | 2012-11-01 | 2014-01-01 | 北京华德创业环保设备有限公司 | Equal-distribution constant-current pulp distributor |
| CN203382487U (en) * | 2013-07-16 | 2014-01-08 | 江苏淮河化工有限公司 | Multi-channel liquid distributor with uniform flow rate |
| CN203582033U (en) * | 2013-12-07 | 2014-05-07 | 通辽矽砂工业公司 | Distance-increasing silica sand discharge tower |
| CN105173781A (en) * | 2015-09-24 | 2015-12-23 | 陈锦鹏 | Raw material storage distributing device |
| CN105971963A (en) * | 2016-07-19 | 2016-09-28 | 宁波文泽机电技术开发有限公司 | Flow type balancing valve |
| CN106902992A (en) * | 2017-03-20 | 2017-06-30 | 中江中通机电科技有限公司 | A kind of energy-efficient sandstone piece-rate system |
| CN108317896A (en) * | 2018-04-19 | 2018-07-24 | 大连理工大学 | Multi-channel type light-gas gun flow equilibrium control high speed enters water emission system |
| CN208882668U (en) * | 2018-10-27 | 2019-05-21 | 中建材通辽矽砂工业有限公司 | Washed-out sand multichannel depiler |
-
2018
- 2018-10-27 CN CN201811262206.6A patent/CN109279256B/en active Active
Patent Citations (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR921047A (en) * | 1946-02-01 | 1947-04-24 | Pesco Products Company | Improvements to flow rate equalization devices |
| GB1159307A (en) * | 1967-04-25 | 1969-07-23 | Young Machinery Company Inc | Solids Flow Rate Equalizer |
| KR200254373Y1 (en) * | 2001-08-24 | 2001-11-24 | 배종호 | Intermediate Tank of Sand Pump Line |
| CN101907185A (en) * | 2009-06-08 | 2010-12-08 | 正大能源材料(大连)有限公司 | Multichannel slurry distributor |
| CN203370636U (en) * | 2012-11-01 | 2014-01-01 | 北京华德创业环保设备有限公司 | Equal-distribution constant-current pulp distributor |
| CN203382487U (en) * | 2013-07-16 | 2014-01-08 | 江苏淮河化工有限公司 | Multi-channel liquid distributor with uniform flow rate |
| CN203582033U (en) * | 2013-12-07 | 2014-05-07 | 通辽矽砂工业公司 | Distance-increasing silica sand discharge tower |
| CN105173781A (en) * | 2015-09-24 | 2015-12-23 | 陈锦鹏 | Raw material storage distributing device |
| CN105971963A (en) * | 2016-07-19 | 2016-09-28 | 宁波文泽机电技术开发有限公司 | Flow type balancing valve |
| CN106902992A (en) * | 2017-03-20 | 2017-06-30 | 中江中通机电科技有限公司 | A kind of energy-efficient sandstone piece-rate system |
| CN108317896A (en) * | 2018-04-19 | 2018-07-24 | 大连理工大学 | Multi-channel type light-gas gun flow equilibrium control high speed enters water emission system |
| CN208882668U (en) * | 2018-10-27 | 2019-05-21 | 中建材通辽矽砂工业有限公司 | Washed-out sand multichannel depiler |
Also Published As
| Publication number | Publication date |
|---|---|
| CN109279256B (en) | 2024-04-26 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104829150B (en) | Thickening method and thickening system of whole tailing material slurry paste | |
| CN202655105U (en) | Iron mine tailing dry pile device | |
| CN208882668U (en) | Washed-out sand multichannel depiler | |
| CN102979571A (en) | All tailing sand dry discharge bonding filling system and filling method of filling system | |
| CN212535754U (en) | Paste filling full-tailing preparation system | |
| CN109761396A (en) | A kind of shield dregs processing method and equipment | |
| CN102367741A (en) | Mortar making system and process suitable for large horizontal sand silo of mine filling station | |
| CN204620184U (en) | A kind of multi-pipeline surely expects mine-separating box to ore deposit | |
| CN109279256A (en) | Washed-out sand multichannel depiler | |
| CN100534588C (en) | Complete equipment for flue gas desulfurization and method for arranging technological process thereof | |
| CN206985167U (en) | A kind of mixing air-transport system for rice husk removal of impurities | |
| CN204769204U (en) | Pond method of filling out sediment thick liquid conveyor that builds a dam | |
| CN113908972A (en) | Method for recovering fine slime ore in phosphorite slime | |
| CN109340572A (en) | Ore pulp gives mine system | |
| CN103252286A (en) | Method for using dense medium to sort coal-series kaolinite rocks in gangues | |
| CN101823017A (en) | Laterite washing method | |
| CN209287534U (en) | A kind of Swirling flow sand-removing transportation system | |
| CN114017109A (en) | Step-type gravity-flow separation layer grouting filling waste rock pulping and slurry conveying process | |
| CN104495388B (en) | A kind of pneumatic conveying method being provided with the separation of three-level foreign matter | |
| CN2894807Y (en) | Flue gas desulfurizing complete apparatus | |
| CN206857723U (en) | Draw pump big output continuous conveying system in formula storehouse under one kind | |
| CN217026569U (en) | Stepped asphalt stirring equipment | |
| CN101823059A (en) | Laterite washing equipment | |
| CN219540987U (en) | Equipment for transporting zinc calcine | |
| CN104763468A (en) | Tailing slurry collection buffering feeding device and method |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |