CN1927717A - Subsider feeding device - Google Patents
Subsider feeding device Download PDFInfo
- Publication number
- CN1927717A CN1927717A CN 200610051226 CN200610051226A CN1927717A CN 1927717 A CN1927717 A CN 1927717A CN 200610051226 CN200610051226 CN 200610051226 CN 200610051226 A CN200610051226 A CN 200610051226A CN 1927717 A CN1927717 A CN 1927717A
- Authority
- CN
- China
- Prior art keywords
- feed
- pipe
- subsider
- leading portion
- feeding device
- 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
- 238000005189 flocculation Methods 0.000 claims description 7
- 230000016615 flocculation Effects 0.000 claims description 7
- 210000005056 cell body Anatomy 0.000 claims description 6
- 230000008676 import Effects 0.000 claims description 2
- 239000007788 liquid Substances 0.000 abstract description 9
- 239000002002 slurry Substances 0.000 abstract description 4
- 238000005516 engineering process Methods 0.000 abstract description 3
- 239000000463 material Substances 0.000 abstract 1
- 238000010790 dilution Methods 0.000 description 2
- 239000012895 dilution Substances 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000006228 supernatant Substances 0.000 description 2
- 238000003325 tomography Methods 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
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 1
Images
Landscapes
- Treatment Of Sludge (AREA)
Abstract
One kind of feeder for settling tank is disclosed. The feeder has feeding pipe divided into two sections, including the back section with one bell connected and the front section stretched into the bell to form a Venturi tube structure, and can make the clear liquid layer in the settling tank generate self circulation to dilute the fed material slurry. Compared with available technology, the present invention has the advantages of improved red mud settling performance and other advantages.
Description
Technical field:
The invention belongs to red-mud settlement tripping device in the alumina producing, particularly a kind of subsider feeding device.
Background technology:
In aluminum oxide production process, the feeding manner of existing subsider is: slip is introduced into distribution box by fresh feed pump, and then directly enter subsider by feed-pipe, this subsider fed technology can not adapt to charging and contain the bigger condition of production of fluctuation admittedly, make subsider bear that risk ability reduces, processing power is low, rapid variation takes place in the fluctuation that subsider groove condition contains admittedly with charging, admittedly contain when increasing, red-mud settlement performance, compression performance variation, the subsider mud layer is increased, and muddy situation takes place to run in subsider.The frequent fluctuation of subsider groove condition is unfavorable for the control of technical indicator.
Summary of the invention:
The objective of the invention is to: a kind of effective feeding unit is provided, improves the processing power and the ability to ward off risks of subsider, make subsider when charging contains fluctuation admittedly, can steady running.
The present invention is achieved in that
This subsider feeding device comprises feed chute (6), pump (5), feed-pipe (3), subsider (1), feeding cylinder (2), feed chute (6) is connected by the import of pipeline with pump (5), the outlet of pump (5) is connected with feed-pipe (3) by pipeline, feed-pipe (3) is on the top of subsider (1), and the back segment feed-pipe (8) of feed-pipe (3) inserts in the feeding cylinder (2).The interior feed-pipe of subsider (1) (3) is two sections, and leading portion feed-pipe (7) stretches into back segment feed-pipe (8) forward hydraucone (9), forms the Venturi tube structure.When utilizing fluid in Venturi tube, to move, its trunnion place produces vacuum state, make trunnion produce the characteristic of pressure difference on every side, the clear liquid at tomography place is sucked trunnion and enter once more in the feeding cylinder (2), thereby make subsider (1) upper clear supernate layer produce self-circulation, reaching dilution, feed slurry is liquid-solid contains, and improves the purpose of red-mud settlement performance.
Be divided into two sections feed-pipe, leading portion feed-pipe (7) caliber is little, and back segment feed-pipe (8) caliber is big, and leading portion feed-pipe (7) caliber is: 200-350mm, the ratio of itself and back segment feed-pipe (8) caliber is: 1: 1.1-1.2, the ratio of leading portion duct length and back segment duct length is: 1: 0.8.
Slip in the feed chute (6) is squeezed in the feed-pipe (3) by pump (5), guarantees that slip has enough power in feed-pipe (7), can bring the clear liquid that enters once more by hydraucone (9) into feeding cylinder (2).
Flocculation agent adds pipeline (4) and is connected with cell body outside, cell body inside and (2) three of the feeding cylinders of leading portion feed-pipe (7) respectively, to guarantee the even interpolation of flocculation agent.
The present invention compares with existing subsider feeding device, has the following advantages:
(1) feed-pipe forms Venturi tube structure, makes the supernatant liquid clear liquid be brought into the subsider feed-pipe once more under action of pressure, makes the subsider supernatant liquid produce self-circulation, thereby dilutes fed slurry automatically, improves the red-mud settlement performance.
(2) adopt the direct and subsider feed-pipe method of attachment of fresh feed pump outlet, cancel original fresh feed pump and be introduced into distribution box, and then the flow process that enters the subsider feed-pipe, guarantee that slip has enough power in feed-pipe, can bring the clear liquid that enters once more in feed-pipe throat into feeding cylinder.
(3) flocculation agent feed-pipe leading portion, 3 interpolations of feeding cylinder in feed-pipe, the groove outside groove have respectively guaranteed the even interpolation of flocculation agent.
Description of drawings:
Accompanying drawing 1 is the structural representation of this device;
Accompanying drawing 2 is a feed-pipe enlarged view partly among Fig. 1.
Embodiment:
Embodiments of the invention:
Slip in the feed chute 6 is squeezed in the feed-pipe 3 by pump 5, guarantees that slip has enough power in feed-pipe 7, can bring the clear liquid that enters once more by hydraucone 9 into feeding cylinder 2.
Feed-pipe 3 is two sections on the top of subsider 1, and leading portion feed-pipe 7 stretches into back segment feed-pipe 8 forward hydraucones 9, forms the Venturi tube structure.When utilizing fluid in Venturi tube, to move, its trunnion place produces vacuum state, make trunnion produce the characteristic of pressure difference on every side, the clear liquid at tomography place is sucked trunnion and enter once more in the feeding cylinder 2, thereby make subsider 1 upper clear supernate layer produce self-circulation, reaching dilution, feed slurry is liquid-solid contains, and improves the purpose of red-mud settlement performance.
Be divided into two sections feed-pipe, leading portion feed-pipe 7 calibers are little, and back segment feed-pipe 8 calibers are big, and leading portion feed-pipe 7 calibers are 200-350mm, the ratio of itself and back segment feed-pipe 8 calibers is: 1: 1.1-1.2, the ratio of leading portion duct length and back segment duct length is: 1: 0.8.
Flocculation agent adds pipeline 4 and is connected with cell body outside, cell body inside and 2 three of the feeding cylinders of leading portion feed-pipe 7 respectively, to guarantee the even interpolation of flocculation agent.
Claims (4)
1, a kind of subsider feeding device, it comprises feed chute (6), pump (5), feed-pipe (3), subsider (1), feeding cylinder (2), feed chute (6) is connected by the import of pipeline with pump (5), the outlet of pump (5) is connected with feed-pipe (3) by pipeline, feed-pipe (3) is on the top of subsider (1), the back segment feed-pipe (8) of feed-pipe (3) inserts in the feeding cylinder (2), it is characterized in that: the interior feed-pipe of subsider (1) (3) is two sections, and leading portion feed-pipe (7) stretches into back segment feed-pipe (8) forward hydraucone (9).
2, subsider feeding device according to claim 1 is characterized in that: the leading portion caliber of feed-pipe (3) for the ratio with the back segment caliber is: 1: 1.1-1.2, the leading portion duct length with the ratio of back segment duct length is: 1: 0.8.
3, subsider feeding device according to claim 1 is characterized in that: the slip in the feed chute (6) is squeezed in the feed-pipe (3) by pump (5).
4, subsider feeding device according to claim 1, it is characterized in that: flocculation agent adds the top that pipeline (4) is located at subsider (1), and its discharge port is connected with cell body outside, cell body inside and (2) three of the feeding cylinders of leading portion feed-pipe (7) respectively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB200610051226XA CN100396355C (en) | 2006-09-25 | 2006-09-25 | Subsider feeding device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB200610051226XA CN100396355C (en) | 2006-09-25 | 2006-09-25 | Subsider feeding device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1927717A true CN1927717A (en) | 2007-03-14 |
| CN100396355C CN100396355C (en) | 2008-06-25 |
Family
ID=37857876
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB200610051226XA Active CN100396355C (en) | 2006-09-25 | 2006-09-25 | Subsider feeding device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100396355C (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102188841A (en) * | 2010-03-09 | 2011-09-21 | 沈阳铝镁设计研究院有限公司 | Sedimentation tank with diluting and mixing functions |
| CN103230684A (en) * | 2013-05-09 | 2013-08-07 | 中南大学 | Double-feed-pipe flat-bottom settling tank |
| CN103370278A (en) * | 2010-12-13 | 2013-10-23 | Fl史密斯公司 | Open-channel feed dilution system for a thickener or settling tank |
| CN104791005A (en) * | 2015-04-29 | 2015-07-22 | 北京科技大学 | Storage device and method for improving discharging concentration stability of vertical sand silo |
| CN106621482A (en) * | 2016-11-10 | 2017-05-10 | 北京金诚信矿山技术研究院有限公司 | Experimental device for simulating feeding process of deep-cone thickener |
| CN110090473A (en) * | 2018-01-31 | 2019-08-06 | 沈阳铝镁设计研究院有限公司 | A kind of separation of solid and liquid feeding device |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1020258C (en) * | 1990-08-02 | 1993-04-14 | 邯郸市第四瓷厂 | Separator for mud and water |
| AUPS118802A0 (en) * | 2002-03-19 | 2002-04-18 | Outokumpu Oyj | Dual zone feedwell for a thickener |
| CN1772678A (en) * | 2004-11-08 | 2006-05-17 | 祝培华 | Electromagnetically shielding cement |
-
2006
- 2006-09-25 CN CNB200610051226XA patent/CN100396355C/en active Active
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102188841A (en) * | 2010-03-09 | 2011-09-21 | 沈阳铝镁设计研究院有限公司 | Sedimentation tank with diluting and mixing functions |
| CN102188841B (en) * | 2010-03-09 | 2013-10-09 | 沈阳铝镁设计研究院有限公司 | Sedimentation tank with diluting and mixing functions |
| CN103370278A (en) * | 2010-12-13 | 2013-10-23 | Fl史密斯公司 | Open-channel feed dilution system for a thickener or settling tank |
| CN103370278B (en) * | 2010-12-13 | 2016-01-20 | Fl史密斯公司 | For the open channel charging dilution system of thickener or settling bowl |
| CN103230684A (en) * | 2013-05-09 | 2013-08-07 | 中南大学 | Double-feed-pipe flat-bottom settling tank |
| CN104791005A (en) * | 2015-04-29 | 2015-07-22 | 北京科技大学 | Storage device and method for improving discharging concentration stability of vertical sand silo |
| CN106621482A (en) * | 2016-11-10 | 2017-05-10 | 北京金诚信矿山技术研究院有限公司 | Experimental device for simulating feeding process of deep-cone thickener |
| CN110090473A (en) * | 2018-01-31 | 2019-08-06 | 沈阳铝镁设计研究院有限公司 | A kind of separation of solid and liquid feeding device |
Also Published As
| Publication number | Publication date |
|---|---|
| CN100396355C (en) | 2008-06-25 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN1927717A (en) | Subsider feeding device | |
| WO2017107944A1 (en) | Device and method for feeding methane fermentation material with high solid content | |
| CN2760056Y (en) | Filtering machine having internal circulation system | |
| CN200964876Y (en) | Low pressure condensed water reclamation system | |
| CN202542892U (en) | Settling tank for solid-liquid separation | |
| CN107376454A (en) | A kind of double barrels type vacuum equipment | |
| CN207608645U (en) | A kind of novel steel tube segmentation galvanizing rig | |
| CN101487459A (en) | Double-functional manual biogas liquid residue discharge pump | |
| CN201618551U (en) | Producing device of well drilling mud accessory agents | |
| CN205478266U (en) | Exit connection structure of pump body | |
| CN1775683A (en) | Method for diluting bayer process stripping ore pulp for alumina production by mixed joint process | |
| CN107989799A (en) | A kind of small farm pump | |
| CN220035049U (en) | Treatment recovery unit of papermaking tail stock | |
| CN2536390Y (en) | Isostatic press without ultrapressure pipeline | |
| CN211339109U (en) | Manual-automatic integrated remote control water treatment system device | |
| CN220435134U (en) | Hydraulic system of thickener | |
| CN207951719U (en) | A kind of magnetic tail bucket and tailing magnetic separation system | |
| CN220951359U (en) | Rare earth tailing recycling equipment | |
| CN208032521U (en) | A kind of feeding device for synthesizing amino nickel sulphonic acid | |
| CN220633147U (en) | Energy-saving convenient sludge extraction device | |
| CN107915055A (en) | A kind of sand delivering system | |
| CN201866452U (en) | Hydraulic adjustable right-angle connector | |
| CN212548435U (en) | Efficiency of sediment is improved store up mud pond | |
| CN2622258Y (en) | Water-pool free type complete water supply equipment | |
| CN207614502U (en) | Manufacturing of gelatin is with continuously washing cotton system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |