CN201791591U - Separation device for block material and powder material - Google Patents
Separation device for block material and powder material Download PDFInfo
- Publication number
- CN201791591U CN201791591U CN2010205032909U CN201020503290U CN201791591U CN 201791591 U CN201791591 U CN 201791591U CN 2010205032909 U CN2010205032909 U CN 2010205032909U CN 201020503290 U CN201020503290 U CN 201020503290U CN 201791591 U CN201791591 U CN 201791591U
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- separator
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- lump
- granular material
- lifting device
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Abstract
The utility model discloses a separation device for block material and powder material. The separation device is characterized in that more than one lifting device is arranged in a water tank; one end of the lifting device is immersed in water and the other end is higher than the water surface; the lifting device is inclined; the end immersed in water is close to a water tank feed end, and the end higher than the water surface is close to a water tank discharge end; the lifting device includes a chain, a chain wheel and a transmission device; and an elutriating apparatus is mounted on the chain. Under the condition that the block materials have the net powder contents of 25% and 30% and the water contents of 7.5% and 6.5%, the block materials processed by the separation device can have the net powder contents about 3.5%, and the screening effect can achieve 90%.
Description
Technical field
The utility model belongs to the feed separation field, relates in particular to the device of mine, field of metallurgy separation lump material and granular material.
Background technology
Lump material and granular material use vibratory sieve to sieve usually, but granular material bonds mutually with lump material when high humidity or material water ratio are high, adopt that vibratory sieve is very difficult to be separated lump material with granular material at this moment.In the mine, field of metallurgy, often the fine ore in the lump ore need be separated.Along with the iron ore resource turn of the market, iron and steel enterprise improves constantly the lump ore demand, it is more and more lower that requirement contains the powder rate directly into the stove lump ore, and actual inlet block mineral ground is softer relatively, transportation range is far away, have bad luck often, arrive user Shi Qi and contain the powder rate generally about 25%, be up to 35%.At present, domestic iron and steel enterprises adopts vibratory sieve that lump ore is sieved substantially, and oversize enters blast furnace process, and screenings returns the sintering utilization.This bolting method screening efficiency when non-rainy season or lump ore former moisture low (＜4%) is higher, and operate simple and easy, with low cost, be that a kind of mature economy effectively reduces the mode that lump ore contains the powder rate, but when rainy season or lump ore water content are high, fine ore in the lump ore is the mud shape, bonds mutually with lump ore, adopts this moment vibratory sieve to be difficult to the fine ore of lump ore is removed effectively, finally cause containing powder rate height, influence the stable smooth operation of blast furnace into the stove lump ore.Therefore, for reducing the influence to blast furnace of the fine ore that contains in the lump ore, what enterprise have to reduce lump ore in this case goes into the stove ratio, causes the blast furnace ironmaking cost to increase.Domestic iron and steel enterprises also has the hydroblasting of employing mode that lump ore is carried out gumming, as the draw point that helps is to containing the higher lump ore of powder, set up a cover off-line jigging method washing classification treatment system, but its floor space is big, the washup time is longer, disposal ability is less relatively, and water consumption and sewage load are big, and operating cost is higher relatively.
The utility model content
For solving the prior art existing problems, the utility model provides the separator of a kind of lump material and granular material, utilizes granular material to meet water dilution back viscosity decline and lump material and water water in the motion process is realized separating of lump material and granular material to the elutriation of the powder that sticks to the lump material surface.
For achieving the above object, the lump material that the utility model provides and the separator of granular material are the lifting devices that is provided with in tank more than 1, one end of described lifting device immerses in the water, the other end exceeds the water surface, described lifting device is in tilted layout, and a water-immersed end is near the tank feed end, and an end that exceeds the water surface is near the tank discharge end, described lifting device comprises chain, sprocket wheel and transmission device, installs on described chain and eluriates device.
Further improvement of the utility model is, the feed end top of described tank is vertical plane, and the bottom is 60 °～85 ° inclined-plane, and discharge end is 45 °～60 ° inclined-planes.
Further improvement of the utility model is that described lifting device angle of inclination is 45 °～60 °.
Further improvement of the utility model is, the chain of described lifting device is a strand plate chain, described strand plate chain comprises axle, bearing, carrier bar and connecting rod, and two axles are connected to form rectangular frame by two carrier bars, are connected to form chain by two connecting rods between the described rectangular frame.
Further improvement of the utility model is, described elutriation device is the dustpan shape, and the bottom is a screen cloth.
Further improvement of the utility model is, described elutriation device is the basket shape, and bottom and four limits are screen cloth.
Further improvement of the utility model is at the tank discharge end finished product material-transporting system to be set.
Further improvement of the utility model is at bottom of gullet underflow thing conveying device to be set.
Further improvement of the utility model is, connects equipment for separating liquid from solid after described underflow thing conveying device, is made up of in proper order high frequency sieve, mud regulating reservoir, delivery pump, dewaterer at described equipment for separating liquid from solid.
High moisture height contains powder agglomates shape material and why is difficult to screening, mainly is because powder wherein is the mud shape, and has certain viscosity, and behind the screening certain hour, sieve aperture by sticking stifled, cause the screening system screening efficiency to descend, even loses its screening function gradually.The utility model contains the characteristic of powder agglomates shape material according to the moisture height of height, utilize its powder to meet water dilution back viscosity decline and lump material and water to the elutriation of water in the motion process to the powder that sticks to the lump material surface, invented to soak and eluriated device, the realization lump material separates with granular material.
Technical characterstic of the present utility model is:
(1) adopt strand plate chain as the lifting device attaching parts, to prevent that the bulky grain material from blocking chain and the chain phenomenon occurring taking off, the parts that reduce wear simultaneously, the service life of improving chain.
(2) eluriate device and be dustpan shape or basket shape, the bottom is a screen cloth, and screen cloth can be a long strip type, also can be pattern, can also be circular hole, and the mesh size is set according to the requirement to the lump material granularity.
(3) tank is designed to have and eluriates and the water storage unit of sedimentation dual-use function one, utilize the powder eluriating out than great, sinking speed fast and tank in the metastable characteristics of water body, make the top water body contain solid phase to low, guarantee the requirement of elutriation water; The bottom water body is static relatively, guarantees that the effective sedimentation of powder concentrates, and has reduced system's occupation of land and investment.Sink structure as shown in Figure 2.Feed end tank top is vertical plane, and the bottom is 60 °～85 ° inclined-plane; Discharge end adopts 45 °～60 ° inclined-planes.Because feed end powder amount is big, fine powder is many, discharge end powder amount is few, meal is many, and this kind structure had both guaranteed to soak the least quantity of eluriating material, also helped powder sedimentation and concentrated, was convenient to the processing of underflow thing (being deposited on the powder of bottom of gullet).
(4) at bottom of gullet auger conveyor is set, in time height is contained solid underflow thing and send tank, guarantee the elutriation water quality in the tank.
(5) adopt the high frequency sieve that height is contained solid underflow thing and sieve, remove wherein＞the coarse granule powder of 3mm, reduce the treating capacity of underflow thing, reduce dewaterer wearing and tearing and energy consumption at follow-up dehydration procedure.
(6) design of coarse fodder stockyard has drainage and drain function, to stack the coarse granule powder that high frequency sifts out, is convenient to further reclaim and eluriates water.
(7) back pool is set, collects the supernatant of dewaterer and the water liquid that the meal stockyard leaches, carry return flume by water pump again, realize the recycling of water resource.Back pool has both pooling feature, for elutriation provides continuous recirculated water.
The utility model imports lump material to be separated and granular material in the undersurface elutriation device of tank, to eluriate device by lifting device then leaves the water to certain altitude, lump material and the granular material that to eluriate after the upset in the device are poured in the next stage elutriation device, after repeatedly eluriating, before leaving tank after leaving the water the last time, utilizing additional new water and recirculated water that the lump material after eluriating is washed, forward finished product material induction system then to and be transported to finished product stockpile field.Tank underflow thing is transported to high frequency by auger conveyor and sieves, oversize is transported to the meal stockyard, screenings enters in the mortar regulating reservoir and stirs, being delivered to dewaterer by the mortar delivery pump handles, fine powder material after the dehydration is transported to the fine powder stockyard, the supernatant of dewaterer enters back pool, is back in the tank by water pump, realizes the recycling of water.Compared with prior art, the utlity model has following effect:
(1) gumming is effective, the screening efficiency height.Lump material is containing powder rate 25%, 30% only, and moisture is under 7.5%, 6.5% the situation, contains powder only after separating through this device and can drop to about 3.5%, and screening efficiency reaches 90%, and the powder that contains only after the screening of actual production relatively at present hangs down 7～13 percentage points.(illustrate: contain powder only and refer to that lump material contains all ratios less than the particle of eluriating device screen cloth spacing and adhesion fine powder.Test determination shows, conventional screening material contain the powder rate only more than 7%)
(2) circulating water treatment amount is low.The circulating water treatment amount is 97.8t/h, and quantity of circulating water is 44t/h.
(3) compare with Ji steel jigging method water wash system, under the suitable condition of investment cost, disposal ability is big, can satisfy the material treating capacity of 400t/h.
(4) but on-line operation, operating cost is low, about 1.78 yuan/t.The washing of Ji steel jigging method is an off-line operation, and operating cost is about 20 yuan/t.
(5) floor space is few, and system's investment cost is low.Press the lump material disposal ability of 500t/h, soak the elutriation method system and take up an area of about 500m
2, invest about 1,000 ten thousand yuan.
Description of drawings
Fig. 1: the separator schematic diagram of lump material and granular material
Fig. 2: strand plate chain belt structural representation
Fig. 3: sink structure schematic diagram
The specific embodiment:
Be example to contain the powder agglomates ore deposit below, in conjunction with the accompanying drawings the utility model done detailed explanation.。
As shown in Figure 1, with contain only powder rate 25%, moisture be that 7.5% lump ore is imported in tank (19) the undersurface elutriation devices (3) through bar grizzl(e)y chute (2) by vibra feeder (1), realize soaking; Move the lump ore that to eluriate in the device (3) by lifting device (4) obliquely with 0.1m/s～1.0m/s speed then and leave the water, pour the elutriation device of next stage elevator (4) after the upset into, realize eluriating to 0.3m～2.0m.Lump ore is left the water by lifting device (4) through after repeatedly eluriating, and forwards finished product ore deposit conveyer belt (9) to by receiving hopper (8) then, is transported to stockyard, finished product ore deposit; By Fig. 1 and Fig. 3 as can be known, one end of described lifting device (4) immerses in the water, the other end exceeds the water surface, described lifting device (4) is in tilted layout, a water-immersed end is near tank (19) feed end A, an end that exceeds the water surface is near tank (19) discharge end B, and described lifting device comprises chain, sprocket wheel and transmission device, installs on described chain and eluriates device; Described elutriation device is the dustpan shape, and the bottom is a screen cloth.
Only contain the powder rate through the lump ore after the separation of this device and can drop to about 3.5%, screening efficiency reaches 90%.
As shown in Figure 1, with contain only powder rate 30%, moisture be that 6.5% lump ore is imported in tank (19) the undersurface elutriation devices (3) through bar grizzl(e)y chute (2) by vibra feeder (1), realize soaking; Move the lump ore that to eluriate in the device (3) by lifting device (4) obliquely with 0.1m/s～1.0m/s speed then and leave the water, pour the elutriation device of next stage elevator (4) after the upset into, realize eluriating to 0.3m～2.0m.Lump ore is left the water by lifting device (4) through after repeatedly eluriating, and forwards finished product ore deposit conveyer belt (9) to by receiving hopper (8) then, is transported to stockyard, finished product ore deposit; One end of described lifting device immerses in the water, and the other end exceeds the water surface, and described lifting device is in tilted layout, and a water-immersed end is near the tank feed end, and an end that exceeds the water surface is near the tank discharge end, and described lifting device angle of inclination is 45 °～60 °; Described lifting device comprises chain, sprocket wheel and transmission device, as shown in Figure 2, the chain of described lifting device is a strand plate chain, described strand plate chain comprises axle 201, bearing 202, carrier bar 203 and connecting rod 204, two axles are connected to form rectangular frame by two carrier bars, are connected to form chain by two connecting rods between the described rectangular frame, install on described chain and eluriate device, described elutriation device is the basket shape, and bottom and four limits are screen cloth; As shown in Figure 3, the feed end A top of described tank is vertical plane, and the bottom is 60 °～85 ° inclined-plane, and discharge end B is 45 °～60 ° inclined-planes.
Only contain the powder rate through the lump ore after the separation of this device and can drop to about 3.5%, screening efficiency reaches 90%.
As seen from Figure 1, lump material is identical with embodiment 1 or 2 with other parts of separator of granular material, in order to improve separating effect, lump ore is through after repeatedly eluriating, when leaving the water for the last time, adopt additional new water (5) and recirculated water (7) to chew (6) lump ore is washed, forward finished product ore deposit conveyer belt (9) to by receiving hopper (8) then, be transported to stockyard, finished product ore deposit by flushing.
Lump material is identical with embodiment 1 or 2 with other parts of separator of granular material, handle tank underflow thing for convenience, at bottom of gullet underflow thing conveying device is set, connect equipment for separating liquid from solid after described underflow thing conveying device, described equipment for separating liquid from solid is made of in proper order high frequency sieve, mud regulating reservoir, delivery pump, dewaterer.As seen from Figure 1, underflow thing conveying device is auger conveyor (18), tank (19) underflow thing is transported to high frequency sieve (17) by auger conveyor (18), oversize enters meal stockyard (16), and screenings flows in the ore pulp regulating reservoir (15) and stirs, and is delivered to dewaterer (12) by ore pulp delivery pump (14) and handles, fine powder after the dehydration enters fine powder stockyard (13), supernatant enters back pool (11), is back in the tank (19) by water pump (10), realizes the recycling of water.
Claims (10)
1. the separator of lump material and granular material, it is characterized in that, lifting device more than 1 is set in tank, one end of described lifting device immerses in the water, and the other end exceeds the water surface, and described lifting device is in tilted layout, a water-immersed end is near the tank feed end, an end that exceeds the water surface is near the tank discharge end, and described lifting device comprises chain, sprocket wheel and transmission device, installs on described chain and eluriates device.
2. the separator of lump material as claimed in claim 1 and granular material is characterized in that, the feed end top of described tank is vertical plane, and the bottom is 60 °～85 ° inclined-plane, and discharge end is 45 °～60 ° inclined-planes.
3. the separator of lump material as claimed in claim 1 and granular material is characterized in that, described lifting device angle of inclination is 45 °～60 °.
4. the separator of lump material as claimed in claim 1 and granular material, it is characterized in that, the chain of described lifting device is a strand plate chain, described strand plate chain comprises axle, bearing, carrier bar and connecting rod, two axles are connected to form rectangular frame by two carrier bars, are connected to form chain by two connecting rods between the described rectangular frame.
5. the separator of lump material as claimed in claim 1 and granular material is characterized in that, described elutriation device is the dustpan shape, and the bottom is a screen cloth.
6. the separator of lump material as claimed in claim 1 and granular material is characterized in that, described elutriation device is the basket shape, and bottom and four limits are screen cloth.
7. the separator of lump material as claimed in claim 1 and granular material is characterized in that, at the tank discharge end finished product material-transporting system is set.
8. the separator of lump material as claimed in claim 1 and granular material is characterized in that, at bottom of gullet underflow thing conveying device is set.
9. the separator of lump material as claimed in claim 1 and granular material is characterized in that, connects equipment for separating liquid from solid after described underflow thing conveying device.
10. the separator of lump material as claimed in claim 9 and granular material is characterized in that, is made up of in proper order high frequency sieve, mud regulating reservoir, delivery pump, dewaterer at described equipment for separating liquid from solid.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205032909U CN201791591U (en) | 2010-08-20 | 2010-08-20 | Separation device for block material and powder material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205032909U CN201791591U (en) | 2010-08-20 | 2010-08-20 | Separation device for block material and powder material |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201791591U true CN201791591U (en) | 2011-04-13 |
Family
ID=43846511
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010205032909U Expired - Fee Related CN201791591U (en) | 2010-08-20 | 2010-08-20 | Separation device for block material and powder material |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201791591U (en) |
-
2010
- 2010-08-20 CN CN2010205032909U patent/CN201791591U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP02 | Change in the address of a patent holder |
Address after: 243003 intellectual property department, technology center, No. 8 Hunan West Road, Yushan, Ma'anshan, Anhui Patentee after: Ma'anshan Iron and Steel Co., Ltd. Address before: 243003 intellectual property department, technology center, No. 8 Hunan West Road, Ma'anshan, Anhui Patentee before: Ma'anshan Iron and Steel Co., Ltd. |
|
| CP02 | Change in the address of a patent holder | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110413 Termination date: 20170820 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |