CN205223306U - Blast furnace grain slag pulp water isolator - Google Patents
Blast furnace grain slag pulp water isolator Download PDFInfo
- Publication number
- CN205223306U CN205223306U CN201520960160.0U CN201520960160U CN205223306U CN 205223306 U CN205223306 U CN 205223306U CN 201520960160 U CN201520960160 U CN 201520960160U CN 205223306 U CN205223306 U CN 205223306U
- Authority
- CN
- China
- Prior art keywords
- sealing coat
- grain slag
- water
- isolator
- solid filler
- 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.)
- Expired - Fee Related
Links
Landscapes
- Processing Of Solid Wastes (AREA)
Abstract
The utility model belongs to grain slag splitter field, concretely relates to blast furnace grain slag pulp water isolator. The utility model discloses a blast furnace grain slag pulp water isolator, the isolator be located the grain slag pond, a serial communication port, the isolator includes separation net and the three -layer isolation layer of compriseing the solid filler that is located separation net below. Adopt the utility model discloses an isolator, set up the isolation layer that the three -layer has the solid filler below the separation net, through each isolation layer effect, be arranged in the pipe continuous extraction of water of grain slag on to the isolation layer under the effect of suction pump that absorbs water of grain slag bottom of the pool portion and isolator below, reach quick realization residue and water separation's mesh, the dehydration of foretell isolator rapidly, dewatering effect is good, grain slag dehydration back moisture content <= 12 percent, can be directly through the car transportation, and operation cost is low, stable operation is achieved, the drainage pump is highly reliable, can not fall off and can be repeatedly used.
Description
Technical field
The utility model belongs to grain slag separating device field, is specifically related to a kind of blast furnace granulated slag pulp water shield retaining.
Background technology
In the processes such as ironmaking and copper metallurgy, nickel, lead, zinc, can produce the slag of a large amount of high temperature fused states, the treatment process of these slags roughly has two kinds: a kind of is traditional grain slag water quenching and natural cooling; Two is the broken and evaporations of Bao Er Water Company of Luxembourg grain slag water.These grain slags are former is a kind of waste produced in smelting, but if select water quenching process, the heat of grain slag just can be made to be fully utilized, turn waste into wealth.
Adopt above-mentioned grain slag water quenching, after grain slag dehydration, because the water ratio of grain slag is higher, can not transport immediately, in order to avoid the sewage in transport road in grain slag spills on road surface, affect environmental health, therefore, need to arrange control water grain slag field, grain slag is placed in grain slag field control water and reaches requirement to the water ratio of grain slag and just can be transported to other place, can not realize disposablely online completing dehydration in grain slag control water process, reach moisture requirement and directly to set out on a journey transport.
Mainly there is following defect in above-mentioned grain slag treatment process:
1, control grain slag field floor space large, the control water time is long, meets wind and plays dust pollution environment;
2, dewatering system maintenance is large, and labor strength is large, and running cost is high;
3, the calorific loss of washing slag water in dehydration, heat energy is not all recycled.
Method conventional is at present that grain slag is delivered to water slag groove, then delivers to the condensation of granulation tower, is expelled to granulating pit, then is delivered to grain slag field control water.Above-mentioned system and method, still can not solve moisture content height in grain slag needs special grain slag field to grain slag control water problem.
The people such as Wang Maohua deliver " Treating Methods for BF Slag " in the 2nd phase in 2006 total 338th phase " Anshan iron and steel plant technology ", disclose in this article, end filter method is adopted to process blast furnace slag, its technical process is: after the high pressure water that blast furnace slag is sprayed by porous nozzle in Punched box carries out shrend, Water Quenching Slag flows through shot tank and enters detritus pool, grain slag in detritus pool is caught by grab bucket and is deposited in the continuation dehydration of dry slag field, water in detritus pool and suspended substance flow into isolation tank by channel of allocation, gravel sealing coat is laid in isolation tank, and establish shaped steel to protect, washing slag water after isolation is reused after header is pressurizeed the cooling of feeding cooling tower by pump.
In above-mentioned method, the speed that grain slag is separated is still slow, generally needs the time of 3-4 days.Therefore, need to improve for above-mentioned defect, design a kind of pulp water shield retaining that can realize blast furnace granulated slag fast and be separated.
Utility model content
In order to solve above-mentioned technical problem, the utility model provides a kind of pulp water shield retaining that can realize blast furnace granulated slag sharp separation.
The purpose of this utility model is exactly for the defect existing for existing processed technique, and a kind of blast furnace granulated slag pulp water shield retaining is provided, do not change existing iron-smelting process, do not affect ironmaking production prerequisite under, coordinate blast-furnace slag online negative pressure processed technique, pulp water shield retaining device be installed in granulating pit, realize the sharp separation of slag and water, water ratio≤12% after grain slag dehydration, direct Automobile Transportation, running cost is low, stable, good reliability, reusable.
Blast furnace granulated slag pulp water shield retaining of the present utility model is positioned at granulating pit, and this shield retaining comprises separation net and is positioned at the three layers of sealing coat be made up of solid filler below separation net.
Improve as one of the present utility model, above-mentioned three layers of sealing coat are set to the sealing coat I, sealing coat II and the sealing coat III that arrange from top to bottom successively.
The thickness of sealing coat I is 30-50cm, and the thickness of sealing coat II is 40-60cm, and the thickness of sealing coat III is 50-70cm.
Preferably, in sealing coat I be the solid filler of diameter 40-60mm; It is the solid filler of diameter 60-80mm in sealing coat II; It is the solid filler of diameter 80-100mm in sealing coat III.
Solid filler in above-mentioned sealing coat I is any one in steel ball, nylon ball, pebbles;
Same, the solid filler in sealing coat II is any one in steel ball, nylon ball, pebbles;
Solid filler in sealing coat III is any one in steel ball, nylon ball, pebbles.
The material of separation net is DN50 steel pipe, and separation net is square frame-shaped fenestral fabric, and the specification of grid is 1m × 1m.
Blast furnace granulated slag pulp water shield retaining carries out the method for grain slag separation, comprises following step:
Enter the slag-water slurry in granulating pit, act on layer by layer through the sealing coat I of shield retaining, sealing coat II and sealing coat III, by water suction pump and the water absorption tube be arranged in bottom granulating pit, the water of above-mentioned three layers of sealing coat is pumped out, realize grain slag and be separated.
The beneficial effects of the utility model are, adopt shield retaining of the present utility model, three layers of sealing coat with solid filler are set below separation net, through isolating layer by layer, to be positioned at bottom granulating pit and water absorption tube below shield retaining under the effect of water suction pump to sealing coat isolate the water got off and constantly extract, reach the object realizing pulp water fast and be separated, above-mentioned shield retaining dehydration rapidly, dehydrating effect is good, water ratio≤12% after grain slag dehydration, directly can pass through Automobile Transportation, running cost is low, stable, good reliability, reusable.
accompanying drawing illustrates:
Fig. 1 is a kind of blast furnace granulated slag pulp water shield retaining of the utility model and using method schematic diagram;
Fig. 2 is the structural representation of separation net in the utility model;
In figure, 1-granulating pit, 2-blast-furnace slag, 3 is separation net, 4-sealing coat I, 5-water absorption tube, 6-sealing coat II, 7-sealing coat III.
Embodiment
Below in conjunction with specific embodiment, the utility model is further described, so that those skilled in the art more understands the utility model, but does not therefore limit the utility model.
Embodiment 1
In granulating pit 1, pulp water shield retaining is set, three layers of sealing coat that this shield retaining comprises separation net 3 and is positioned at below separation net 3, three layers of sealing coat are the sealing coat I 4, sealing coat II 6 and the sealing coat III 7 that arrange from top to bottom successively, and sealing coat I 4, sealing coat II 6 and sealing coat III 7 are solid filler---pebbles.
The thickness of sealing coat I 4 is about 40cm, and the thickness of sealing coat II 6 is about 50cm, and the thickness of sealing coat III 7 is about 60cm.
It is the solid filler of diameter about 50mm in sealing coat I; It is the solid filler of diameter about 70mm in sealing coat II; It is the solid filler of diameter about 90mm in sealing coat III.
The material of separation net 3 is DN50 steel pipes, and separation net 3 is in square frame-shaped fenestral fabric, and the specification of grid is 1m × 1m.
Bottom granulating pit 1, below shield retaining, have water absorption tube 5, this water absorption tube 5 is connected with water suction pump, and by water suction pump effect, the water in the sealing coat above it pumps out by water absorption tube 5 fast, realizes pulp water and is separated.
Adopt above-mentioned pulp water shield retaining, pulp water can be realized be separated fast, the 72 hours original grain slag control water time is shortened to about 15 minutes by the utility model, process grain slag dewatering time is short, do not need grain slag field, grain slag dehydration after water ratio≤12%, direct Automobile Transportation, in transport, grain slag does not drip, floor space is little, and running cost is low, stable, good reliability, in dehydration, the heat of washing slag water can be recycled, and is a kind of energy-saving environment protecting waste processed technique.
Comparative example 1
If sealing coat is set to from top to bottom: sealing coat II, sealing coat I, sealing coat III; It is the solid filler of diameter about 50mm in sealing coat I; It is the solid filler of diameter about 70mm in sealing coat II; It is the solid filler of diameter about 90mm in sealing coat III.
Namely change the position of sealing coat, in every layer of sealing coat, the diameter of solid filler is constant;
Due to sealing coat II is arranged on the top, along with the carrying out of isolation, slag can fill the space of the solid filler of sealing coat II, slows down the isolation speed of pulp water; Result shows, in comparative example 1, isolation time can 30-40% longer than embodiment 1.
Comparative example 2
If sealing coat is set to from top to bottom: sealing coat III, sealing coat II, sealing coat I; It is the solid filler of diameter about 50mm in sealing coat I; It is the solid filler of diameter about 70mm in sealing coat II; It is the solid filler of diameter about 90mm in sealing coat III.
Namely change the position of sealing coat, in every layer of sealing coat, the diameter of solid filler is constant;
Result shows, in comparative example 2, isolation time can 50-60% longer than embodiment 1.
Comparative example 3
If sealing coat to be set to the thickness of 150mm, identical with embodiment 1 thickness, but only lay the solid filler that diameter is about 50mm in whole sealing coat; Dewater same slag, and the time in comparative example 3 is 1 hours; Longer than the time of embodiment 1.
Comparative example 4
If sealing coat to be set to the thickness of 150cm, identical with embodiment 1 thickness, but only lay the solid filler that diameter is about 70mm in whole sealing coat; Dewater same slag, and the time in comparative example 3 is 2 hours; Treatment time is longer than embodiment 1 far away.Analyzing, may be because solid filler diameter is comparatively large, the space of slag in isolation processes between the easy blocking of the carrying out along with isolation solid filler, thus slows down the speed of dehydration.
Comparative example 5
With comparative example 1 unlike, the thickness of sealing coat I 4 is set to about 25cm, and the thickness of sealing coat II 6 is about 30cm, the thickness of sealing coat III 7 is about 45cm, the thickness of whole sealing coat is 100cm, and the time of dehydration is 1.5 hours, also will be longer than the dewatering time in embodiment 1 far away.
As can be seen from above contrast, the setting of sealing coat of the present utility model be dewatering speed the most fast.Change the diameter of solid filler or the thickness of sealing coat, all can have an impact for dewatering speed.
Claims (2)
1. blast furnace granulated slag pulp water shield retaining, described shield retaining is positioned at granulating pit, it is characterized in that, described shield retaining comprises separation net and is positioned at the three layers of sealing coat be made up of solid filler below separation net;
Three layers of sealing coat comprise the sealing coat I, sealing coat II and the sealing coat III that arrange from top to bottom successively;
The thickness of described sealing coat I is 30-50cm, and the thickness of described sealing coat II is 40-60cm, and the thickness of described sealing coat III is 50-70cm;
It is the solid filler of diameter 40-60mm in sealing coat I; It is the solid filler of diameter 60-80mm in described sealing coat II; It is the solid filler of diameter 80-100mm in described sealing coat III;
Solid filler in described sealing coat I is any one in steel ball, nylon ball, pebbles;
Solid filler in described sealing coat II is any one in steel ball, nylon ball, pebbles;
Solid filler in described sealing coat III is any one in steel ball, nylon ball, pebbles.
2. blast furnace granulated slag pulp water shield retaining as claimed in claim 1, it is characterized in that, the material of described separation net is DN50 steel pipe, and described separation net is square frame-shaped fenestral fabric, and the specification of grid is 1m × 1m.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201520960160.0U CN205223306U (en) | 2015-11-27 | 2015-11-27 | Blast furnace grain slag pulp water isolator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201520960160.0U CN205223306U (en) | 2015-11-27 | 2015-11-27 | Blast furnace grain slag pulp water isolator |
Publications (1)
Publication Number | Publication Date |
---|---|
CN205223306U true CN205223306U (en) | 2016-05-11 |
Family
ID=55898383
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201520960160.0U Expired - Fee Related CN205223306U (en) | 2015-11-27 | 2015-11-27 | Blast furnace grain slag pulp water isolator |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN205223306U (en) |
-
2015
- 2015-11-27 CN CN201520960160.0U patent/CN205223306U/en not_active Expired - Fee Related
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN100445399C (en) | Environment friendly blast furnace slag treating process and system | |
CN102312024B (en) | Method and system for mechanical granulation of metallurgy slag and waste heat recovery | |
CN207159250U (en) | Filter blast furnace grain slag processing system in a kind of hydrocone type bottom | |
CN1311089C (en) | Method of bulk infusion extracting nickel cobalt from low grade red soil nickel ore | |
CN201817499U (en) | Water processing system for blast-furnace slag granulation | |
CN205223306U (en) | Blast furnace grain slag pulp water isolator | |
CN200996021Y (en) | Environmental-protecting blast-furnace cinder treating system | |
CN105603136A (en) | Water-slag isolator for water granulated slag of blast furnace and water-slag separation method | |
CN105567993B (en) | A kind of beneficiation method of low-grade oxidized form mine tailing containing gold and silver | |
CN206304385U (en) | A kind of condensation vapor well construction for landfill gas collection system | |
CN205188319U (en) | Online negative pressure dewatering system of blast furnace grain slag | |
CN105256088A (en) | Online negative pressure dewatering system and dewatering method for blast furnace granulated slag | |
CN101781691B (en) | Blast-furnace slag processing system | |
CN207561028U (en) | A kind of afforestation equipment for alkaline land improving | |
CN202201908U (en) | System for mechanically granulating metallurgical slag and recovering waste heat | |
CN207102047U (en) | A kind of anti-erosion water and soil separator | |
CN201214664Y (en) | Environment-friendly blast furnace slag processing system | |
CN208151458U (en) | A kind of dump leaching field heelpiece subregion collection flow guide system | |
CN203678826U (en) | Water quenching equipment for yellow phosphorous furnace slag | |
CN105032030B (en) | Fine iron breeze fast dewatering method in a kind of sedimentation tank | |
CN210030481U (en) | Phosphogypsum stacking and collecting device | |
CN203429012U (en) | Efficient energy-saving pollution-free dry processing system of bauxite washing tailing pulp | |
CN2795216Y (en) | Lifting and dewatering device for blast furnace slag granulation device | |
CN103801549B (en) | A kind of method and apparatus of shrend yellow phosphorus furnace slag | |
CN115231802A (en) | Dehydration equipment and bauxite tailing recycling method |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160511 Termination date: 20171127 |