CN106088694A - Lateritic nickel ore raw material storage and lateritic nickel ore stock preparation system - Google Patents
Lateritic nickel ore raw material storage and lateritic nickel ore stock preparation system Download PDFInfo
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- CN106088694A CN106088694A CN201610402785.4A CN201610402785A CN106088694A CN 106088694 A CN106088694 A CN 106088694A CN 201610402785 A CN201610402785 A CN 201610402785A CN 106088694 A CN106088694 A CN 106088694A
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- E—FIXED CONSTRUCTIONS
- E04—BUILDING
- E04H—BUILDINGS OR LIKE STRUCTURES FOR PARTICULAR PURPOSES; SWIMMING OR SPLASH BATHS OR POOLS; MASTS; FENCING; TENTS OR CANOPIES, IN GENERAL
- E04H5/00—Buildings or groups of buildings for industrial or agricultural purposes
- E04H5/02—Buildings or groups of buildings for industrial purposes, e.g. for power-plants or factories
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B1/00—Preliminary treatment of ores or scrap
- C22B1/14—Agglomerating; Briquetting; Binding; Granulating
- C22B1/16—Sintering; Agglomerating
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Abstract
The present invention relates to a kind of lateritic nickel ore raw material storage, including storehouse, in storehouse, space includes storing area and dispensing district;Including lateritic nickel ore storehouse, calculogenesis ash silo and reducing agent storehouse in storing area, storing area has the feed(raw material)inlet to the corresponding raw material of each raw material cabin conveying;Including dry territory and dispensing territory in dispensing district, vexed heap to carry out dehydrate to lateritic nickel ore in dry territory for lateritic nickel ore and quick lime, and dispensing territory receives the raw material in self-desiccation territory and reducing agent storehouse to prepare raw materials for sintering;Dispensing district has formulation outlet, dispensing territory and formulation outlet.In the present invention, the operation such as material storage and dispensing is all carried out, not by wind and rain climatic effect in closing storehouse, it is ensured that the normal table of production operation is carried out;Without material loss, production operation to external environment condition without airborne dust, noise, contaminated wastewater.Lateritic nickel ore all processes through quick lime dehydrate, for follow-up sintering, smelts and saves energy resource consumption.
Description
Technical field
The invention belongs to use the technical field of lateritic nickel ore ironmaking, be specifically related to a kind of lateritic nickel ore raw material storage and laterite
Nickel minerals stock preparation system.
Background technology
Lateritic nickel ore, as the primary raw material of production ferronickel, all needs to store up raw material in the raw material preparatory stage before smelting
Deposit, be dried, granulate, dispensing, mixing etc. just can be sent to sintering for agglumeration after processing.Saying from the property of raw material of lateritic nickel ore, raw ore contains
Free water and water of crystallization are typically at about 30% (free water of about 20% and the water of crystallization of about 10%) so that smelt tired
Difficulty, raw material must be calcined through oversintering, is fully dried and can enter stove after prereduction and smelts.Ore nickel content improves according to statistics
0.1%, production cost can reduce by 3%~4%, otherwise the most then;Make raw material drying, granularity, composition uniform in the raw material preparatory stage,
Facilitate scale-up, raising equipment and heat utilization coefficient.Therefore, lateritic nickel ore stock preparation system technique is directly closed
It is tied to quality and the performance of enterprises of ferro-nickel product.
Compared with the conventional metallurgical raw material preparation huge with scale and production capacity, relative Ferrous Metallurgy yield rule smelted by dilval
Mould is less, the user of raw material service is the most single.Owing to being affected by Feedstock treating scale, extensively should in traditional raw material field
Cannot play the advantage processed in big handling capacity with large-scale heap reclaimer device do mechanization operation, the preparation of existing lateritic nickel ore processes
Basic is exactly to rely on artificial and engineering truck operation freely on vacant lot, uses knowhow substitute technology, can without the system integration
Speech, the parametrization of scientific quantification produces and does not knows where to begin especially, there is presently no a kind of whole process, integrated, scientific based on
The raw materials for sintering preparation system of lateritic nickel ore.
Being affected by property of raw material, the moisture content of lateritic nickel ore is high and viscous soil characteristics, it is impossible to realize storage, in storage shape
Master is saved as with bulk storage heap naturally in formula.The randomness stored up and the do mechanization operation that cannot launch, on the one hand cause production effect
Rate low, on the other hand, airborne dust in production, noise, waste water severe contamination environment;For using small furnace method to produce nickel
The enterprise of ferrum, it is particularly problematic that this extensive mode of production is brought.
Summary of the invention
The embodiment of the present invention provides a kind of lateritic nickel ore raw material storage and lateritic nickel ore stock preparation system, at least can solve existing
There is the segmental defect of technology.
The present embodiments relate to a kind of lateritic nickel ore raw material storage, including storehouse, in described storehouse, space includes storing
District and dispensing district;Including lateritic nickel ore storehouse, calculogenesis ash silo and reducing agent storehouse in described storing area, described storing area has to respectively
The feed(raw material)inlet of the corresponding raw material of raw material cabin conveying;Dry territory and dispensing territory is included, from described laterite nickel in described dispensing district
The lateritic nickel ore of ore storage bin and the quick lime of calculogenesis ash silo in described dry territory vexed heap lateritic nickel ore to be carried out dehydrate, institute
State the dispensing territory reception raw material from described dry territory and described reducing agent storehouse to prepare raw materials for sintering;Described dispensing district has joins
System material outlet, described dispensing territory and described formulation outlet.
As one of embodiment, described lateritic nickel ore storehouse and described calculogenesis ash silo arranged adjacent, and all adjacent to described dry
Dry territory.
As one of embodiment, described dry territory and described reducing agent storehouse are all adjacent to described dispensing territory.
As one of embodiment, being formed with raw material carrier vehicle and run passage in described storehouse, described operation passage is from described
Feed(raw material)inlet extends to the storehouse headwall side being right against this feed(raw material)inlet, and is separated to form space in described storehouse into described storage
Material district and described dispensing district;Each raw material cabin in described storing area is arranged along described operation channel-length direction, described dry territory
Arrange along described operation channel-length direction with described dispensing territory.
As one of embodiment, described dry territory includes two stockpile fields, and stockpile field described in two divides row described dispensing territory two
Side;Described lateritic nickel ore storehouse and described calculogenesis ash silo are all correspondingly arranged two, and there is a described laterite every side, described reducing agent storehouse
Nickel minerals storehouse and a described calculogenesis ash silo.
As one of embodiment, it is provided with, in described dispensing territory, the granulating mechanism that lateritic nickel ore is carried out granulate classification, and right
The big granularity mineral aggregate stockyard that should configure and small grain size mineral aggregate stockyard, granularity is stored up 10~30mm in described big granularity mineral aggregate stockyard
Big granularity mineral aggregate, the small grain size mineral aggregate of granularity≤10mm is stored up in described small grain size mineral aggregate stockyard.
As one of embodiment, it is provided with in described dispensing territory:
For being connected to the formulation output device of sintering machine, described formulation output device extend out to described formulation and goes out
Outside Kou;
For exporting described big granularity mineral aggregate using as the first dosage bunker of hearth layer for sintering and export described small grain size ore deposit
Second dosage bunker of material, described first dosage bunker is connected with described formulation output device, and described second dosage bunker passes through first
Metering device is connected with described formulation output device;
Reducing agent dosage bunker, described reducing agent dosage bunker arrival end is held in the mouth with described reducing agent storehouse by material transfer device
Connecing, the port of export is connected with described formulation output device by the second metering device;
Flux dosage bunker, described flux dosage bunker arrival end is connected with described calculogenesis ash silo by material transfer device, goes out
Mouth end is connected with described formulation output device by the 3rd metering device.
As one of embodiment, described formulation output device includes the first deferent segment for connecting each dosage bunker and use
In being connected to the second deferent segment of sintering machine, it is provided with between described first deferent segment and described second deferent segment for by described little
Mixing arrangement that granularity mineral aggregate and reducing agent and flux mix also is connected by this mixing arrangement.
As one of embodiment, described lateritic nickel ore raw material storage also includes automatic control system, described automatic control system
Including central controller, described central controller internal memory contains the nature parameters of each raw material and is calculated by the nature parameters of each raw material
The proportion scheme generated;
Being equipped with the material level detection mechanism that the corresponding raw material of detection is measured in storehouse in each raw material cabin, each described material level detection mechanism is equal
Electrically connect with the input of described central controller, described first metering device, described second metering device, the 3rd
The operating circuit of metering device and each dosage bunker all electrically connects with described central controller input.
The present embodiments relate to a kind of lateritic nickel ore stock preparation system, including lateritic nickel ore raw material storage as above
And sintering machine, described sintering machine is connected with the outlet of described formulation.
The embodiment of the present invention at least achieves following beneficial effect:
(1) operation such as material storage and dispensing is all carried out, not by wind and rain climatic effect in closing storehouse, it is ensured that produces and makees
The normal table of industry is carried out;Without material loss, production operation without airborne dust, noise, contaminated wastewater, does not increase production to external environment condition
Cost, does not cause environmental pollution.
(2) lateritic nickel ore all processes through quick lime dehydrate, for follow-up sintering, smelts and saves energy resource consumption.
(3) storing area and main plot, dispensing district divide, and be closely connected but do not interfere with each other between twoth district, it is achieved big unification, little not
Same planning general layout, facilitates centralized management and interval coordinated management in the district in storing area and dispensing district, manage including physical state,
Environmental managements etc., wherein, environmental management includes again the management of managing dust removal, discharge of wastewater, clunk management etc..
(4) the heap feeding mode that vexed heap operation uses tiling to intercept is puddled, it is ensured that dewatering efficiency and mixed effect.Stockpile
Arranging 2, it is achieved a pile one takes alternately operating, one has been the stockpile of dehydrate, it is ensured that producing feeding, another is
The stockpile being just dehydrated at vexed heap, it is ensured that have the enough dehydration time inside stockpile.
(5) the smooth and easy docking of each inter process, cancels the conveying linking flow process between conventional processes, it is achieved system highly integrated,
Thus storehouse floor space can be reduced, raw material reserves about 20%, unit are soil profit can be improved under equal land area
Decrease primary construction investment with the raising of rate, reduce later stage material loss and production and operation cost.
Accompanying drawing explanation
In order to be illustrated more clearly that the embodiment of the present invention or technical scheme of the prior art, below will be to embodiment or existing
In having technology to describe, the required accompanying drawing used is briefly described, it should be apparent that, the accompanying drawing in describing below is only this
Some embodiments of invention, for those of ordinary skill in the art, on the premise of not paying creative work, it is also possible to
Other accompanying drawing is obtained according to these accompanying drawings.
The plane figure schematic diagram of the lateritic nickel ore raw material storage that Fig. 1 provides for the embodiment of the present invention;
Fig. 2 is the sectional view in Fig. 1 along A-A;
Fig. 3 is the sectional view in Fig. 1 along B-B;
Fig. 4 is the sectional view in Fig. 1 along C-C;
Fig. 5 is the sectional view in Fig. 1 along D-D;
Fig. 6 is the sectional view in Fig. 1 along E-E;
The schematic flow sheet using lateritic nickel ore ironmaking that Fig. 7 provides for the embodiment of the present invention;
The schematic flow sheet of the lateritic nickel ore sieving approach that Fig. 8 provides for the embodiment of the present invention.
Detailed description of the invention
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear, complete
Describe, it is clear that described embodiment is only a part of embodiment of the present invention rather than whole embodiments wholely.Based on
Embodiment in the present invention, those of ordinary skill in the art obtained on the premise of not making creative work all its
Its embodiment, broadly falls into the scope of protection of the invention.
Such as Fig. 1-Fig. 6, the embodiment of the present invention provides a kind of lateritic nickel ore raw material storage, and including storehouse 1, this storehouse 1 is surrounding
If wall skin, roof set the building of roof system.In described storehouse 1, space includes storing area and dispensing district;Described storing area Nei Bao
Having included lateritic nickel ore storehouse 2, calculogenesis ash silo 3 and reducing agent storehouse 4, it is former that described storing area has to each raw material cabin corresponding raw material of conveying
Material entrance;Wherein, lateritic nickel ore storehouse 2 is used for storing lateritic nickel ore, and calculogenesis ash silo 3 is used for storing quick lime, and reducing agent storehouse 4 is used for
Store reducing agent;Usually, each raw material is conveyed in storehouse 1 by transport vehicle, i.e. above-mentioned raw materials entrance is for can hold transport vehicle
Current entrance.Dry territory and dispensing territory is included, from lateritic nickel ore and the life in described lateritic nickel ore storehouse 2 in described dispensing district
The quick lime of lime silo 3 in described dry territory vexed heap lateritic nickel ore to be carried out dehydrate, described dispensing territory receive from
The raw material in described dry territory and described reducing agent storehouse 4 is to prepare raw materials for sintering;Described dispensing district have formulation outlet, described in join
Material territory and described formulation outlet.In dry territory, lateritic nickel ore and quick lime puddle vexed heap, and above-mentioned quick lime is preferably
Using the quick lime of purity more than 90%, addition is to account for 5~20% (percentage by weight) of lateritic nickel ore, the most not only can be right
Lateritic nickel ore carries out dehydrate, moreover it is possible to pre-heat mixture, and in follow-up sintering, quick lime can continue to act as flux
With.In the present embodiment, lateritic nickel ore about mixes in dry territory by weight the proportioning for 10:1 with quick lime, is preferably and uses
Tile mode layer, to fully absorb the free water in lateritic nickel ore.
Continue the arrangement of above-mentioned lateritic nickel ore raw material storage, it is preferable that described lateritic nickel ore storehouse 2 and described calculogenesis ash silo
3 arranged adjacent, and all adjacent to described dry territory;Described dry territory and described reducing agent storehouse 4 all adjacent to described dispensing territory, by
Raw material cabin feeding, at dry territory cloth, be closely connected at each procedures such as dispensing territory dispensings and do not interfere with each other, be effectively improved life
Produce efficiency.Further preferably, such as Fig. 1, being formed with raw material carrier vehicle and run passage in described storehouse 1, described operation passage is from institute
State feed(raw material)inlet to extend to the storehouse 1 headwall side being right against this feed(raw material)inlet, and space in described storehouse 1 is separated to form as institute
State storing area and described dispensing district;Each raw material cabin in described storing area is arranged along described operation channel-length direction, described dry
Arrange along described operation channel-length direction in dry territory and described dispensing territory.Wherein, in the present embodiment, described dry territory is preferably bag
Include two stockpile fields 6, row both sides, described dispensing territory, 6 points, stockpile field described in two;Described lateritic nickel ore storehouse 2 and described calculogenesis ash silo 3
All being correspondingly arranged two, there are a described lateritic nickel ore storehouse 2 and a described calculogenesis ash silo 3 in every side, described reducing agent storehouse 4.When
So, the arrangement in above-mentioned storing area and dispensing district also can have following manner: includes by dry territory, as a example by two stockpile fields 6, joining
Material territory is positioned at storehouse 1 centre position, and two both sides, row dispensing territory, 6 points, stockpile field, each stockpile field 6 is adjacent away from the side in dispensing territory
It is disposed with a lateritic nickel ore storehouse 2 and lime silo 3 in all one's life.
Such as Fig. 1, in the present embodiment, plant arrangement, i.e. storing area and dispensing before using and distinguish the operation of row raw material carrier vehicle
Passage both sides, dispensing territory is positioned at storehouse 1 centre position, each raw material cabin and two stockpile fields 6 and arranges around dispensing territory.This layout side
Formula has the following advantages:
(1) operation such as material storage and dispensing is all carried out, not by wind and rain climatic effect in closing storehouse 1, it is ensured that produce
The normal table of operation is carried out;Without material loss, production operation without airborne dust, noise, contaminated wastewater, does not increase life to external environment condition
Produce cost, do not cause environmental pollution.
(2) storing area and main plot, dispensing district divide, and be closely connected but do not interfere with each other between twoth district, it is achieved big unification, little not
Same planning general layout, facilitates centralized management and interval coordinated management in the district in storing area and dispensing district, manage including physical state,
Environmental managements etc., wherein, environmental management includes again the management of managing dust removal, discharge of wastewater, clunk management etc..As raised in storehouse 1
Dirt pits sets dispersion dedusting, makes airborne dust situation be controlled;Inside and outside storehouse 1, unification arranges pumping equipment, arranges the unifications such as sedimentation tank
Collection processes the waste water of outer row.Wherein, in the present embodiment, between adjacent feed storehouse, the storage being separated to form correspondence with barricade is empty
Between so that arrange between raw material cabin closely, save space, shorten work flow simultaneously;Osculum, material are set bottom barricade
Separate out water by this osculum arrange outside storehouse 1, by storehouse 1 outside draining collection is set, above-mentioned osculum is mainly for red
Soil nickel minerals storehouse 2 is arranged.Depending in storehouse 1, head room is according to production scale, in the present embodiment, in storehouse 1, head room is at 11m
Left and right, material stack height about 6m in each raw material cabin, wall height can realize the compartmentation between different material at about 3m.
(3) the smooth and easy docking of each inter process, cancels conveying linking flow process (such as rear kind of arrangement) between conventional processes, it is achieved
System highly integrated, thus storehouse 1 floor space can be reduced, raw material reserves 20% can be improved under equal land area left
The right side, the raising of unit are land utilization ratio decreases primary construction investment, reduces later stage material loss and production and operation cost.
(4) lateritic nickel ore all processes through quick lime dehydrate, for follow-up sintering, smelts and saves energy resource consumption.Mixed
Mix the heap feeding mode that vexed heap operation uses tiling to intercept, it is ensured that dewatering efficiency and mixed effect.Stockpile field 6 arranges 2, real
Existing a pile one takes alternately operating, and one has been the stockpile of dehydrate, it is ensured that producing feeding, another is for be just dehydrated at vexed heap
Stockpile, it is ensured that have the enough dehydration time inside stockpile.
Continue the structure of above-mentioned lateritic nickel ore raw material storage, and usually, lateritic nickel ore is by the more soil property of weathering
Fine ore and the less stone mass ore deposit of rate of decay are constituted, and both are respectively arranged with feature: the nickeliferous taste of fine ore is higher and composition uniform, but contains
Free water is more, it is not necessary to broken;The nickeliferous taste of lump ore is relatively low and uneven, but less containing free water, need to be crushed to close accordingly
Lattice granularity.To this end, be provided with the granulating mechanism that lateritic nickel ore carries out granulate classification in described dispensing territory, and corresponding configuration is big
Granularity mineral aggregate stockyard 7 and small grain size mineral aggregate stockyard 8, the big granularity that granularity is 10~30mm is stored up in described big granularity mineral aggregate stockyard 7
Mineral aggregate, the small grain size mineral aggregate of granularity≤10mm is stored up in described small grain size mineral aggregate stockyard 8.Above-mentioned granulating mechanism include screening plant and
Disintegrating apparatus, such as Fig. 1, Fig. 6 and Fig. 8, specifically includes: the first screening plant the 9, second screening plant 10 and the first breaker
11, wherein, the first screening plant 9, for sieving lateritic nickel ore raw ore, obtains the first oversize and the first minus mesh, the
One oversize enters the first breaker 11 to carry out broken obtaining broken material, and the first minus mesh is delivered to above-mentioned with above-mentioned broken material
Second screening plant 10 sieves, and obtains the second oversize and the second minus mesh, the second oversize as hearth layer for sintering,
Sintering machine sintering is delivered in two minus mesh with other adjuvant after then mixing.Wherein, the particle diameter of the first oversize is more than 30mm, first
The particle diameter of minus mesh is then≤30mm;First oversize is crushed to particle diameter≤30mm by the first breaker 11;Second oversize
Particle diameter be 10~30mm, the particle diameter of the second minus mesh is≤10mm.Above-mentioned first screening plant 9 and the second screening plant 10 are excellent
Electing all employing circular cone rotary screens as, above-mentioned first breaker 11 preferably uses jaw crusher.
Such as Fig. 1, above-mentioned first screening plant the 9, second screening plant 10 and the first breaker 11 are preferably along raw material transport
Defeated car runs channel-length direction arrangement, and wherein, the first screening plant 9 is preferably located at the second screening plant 10 and first and crushes
Between device 11, in order to the first breaker 11 and the second screening plant is delivered in the first oversize and the first minus mesh respectively
10, improve treatment effeciency;Above-mentioned big granularity mineral aggregate stockyard 7 and small grain size mineral aggregate stockyard 8 are preferably to run along raw material carrier vehicle and lead to
Road length direction is arranged in order, and all arranges adjacent to above-mentioned second screening plant 10, it is considered to the amount of the second oversize compared to
The amount of the second minus mesh is little, and the subsequent treatment operation of the second minus mesh compared with the second oversize want complexity, therefore, big granularity ore deposit
Stockpile field 7 is positioned at the side that small grain size mineral aggregate stockyard 8 exports away from formulation.It addition, above-mentioned first screening plant 9, second sieves
Separating device 10 and the first breaker 11 are positioned at above-mentioned big granularity mineral aggregate stockyard 7 and small grain size mineral aggregate stockyard 8 and transport near raw material
(above-mentioned first screening plant the 9, second screening plant 10 and the first breaker 11 are preferably close to former in the side of car operation passage
Material transport vehicle runs passage and arranges, to save space, shortens handling process), owing to the first screening plant 9 is from two of dry territory
Stockpile field 6 feeding, above-mentioned layout i.e. makes the corresponding close raw material carrier vehicle in two stockpile fields 6 in above-mentioned dry territory run passage cloth
Put, be i.e. dried two stockpile fields 6 in territory and the distance of lateritic nickel ore storehouse 2 and calculogenesis ash silo 3 closer to, handling process can be shortened.
As one of embodiment, it is provided with in described dispensing territory:
For being connected to the formulation output device 14 of sintering machine, described formulation output device 14 extend out to described preparation
Outside material outlet;
For exporting described big granularity mineral aggregate using as the first dosage bunker of hearth layer for sintering and export described small grain size ore deposit
Second dosage bunker of material, described first dosage bunker is connected with described formulation output device 14, and described second dosage bunker passes through the
A certain amount of charging gear is connected with described formulation output device 14;
Reducing agent dosage bunker, described reducing agent dosage bunker arrival end is held in the mouth with described reducing agent storehouse 4 by material transfer device
Connecing, the port of export is connected with described formulation output device 14 by the second metering device;
Flux dosage bunker, described flux dosage bunker arrival end is connected with described calculogenesis ash silo 3 by material transfer device, goes out
Mouth end is connected with described formulation output device 14 by the 3rd metering device.
Above-mentioned formulation output device 14, each dosage bunker 12 and each charging gear i.e. constitute formulation pipeline;Usually,
Lateritic nickel ore sintering needs to configure adhesive, for using quick lime as flux and the production technology of adhesive, it is not necessary to additionally
Adhesive dosage bunker is set, for using bentonite etc. as the technique of adhesive, then needs additionally to arrange adhesive dosage bunker, phase
Ying Di, can set up adhesive storehouse in storing area;It addition, returning charge dosage bunker also can be set up, for by dedusting ash, the returning charge such as return mine
Allocate in lateritic nickel ore.Wherein, above-mentioned formulation output device 14 preferably uses ribbon conveyer, and it is transported along raw material carrier vehicle
Row of channels length direction is disposed to extend;Above-mentioned first metering device preferably comprises frequency control disk feeder and electronics
Belt conveyer scale, above-mentioned second metering device, the 3rd metering device are preferably and all use belted electronic balance or helix balance.On
State each metering device and ensure lateritic nickel ore and the accurate proportioning of each adjuvant, it is ensured that dispensing effect, to avoid dispensing weak effect
And affect the reproducibility of subsequent production ferronickel.Wherein, coal or coke powder as reducing agent are by a certain amount of ferrum and whole nickel element
The required reduction dosage that reduced is allocated into;Quick lime as flux and adhesive is allocated into by basicity requirement, according to swelling
Soil as adhesive, its amount of allocating into be generally formulation output (i.e. the gross weight of lateritic nickel ore and each adjuvant) 1%~
2%;The returning charges such as dedusting ash, are typically allocated into by 5% (percentage by weight) of dispensing base unit weight.The quantity of each dosage bunker 12 depends on actual work
Depending on condition, in the present embodiment, the quantity of the second dosage bunker for carrying small grain size lateritic nickel ore is 5, reducing agent dosage bunker
It is 2, dosage bunker 2 of returning mine, dedusting ash dosage bunker 1, flux dosage bunker 1 or 2.
Further, described formulation output device 14 include the first deferent segment for connecting each dosage bunker 12 and for
It is connected to the second deferent segment of sintering machine, is provided with for by described granule between described first deferent segment and described second deferent segment
Degree mineral aggregate and reducing agent and the mixing arrangement 13 of flux mixing are also connected by this mixing arrangement 13.I.e. on formulation pipeline
It is provided with mixing arrangement 13, so that the raw material allocated into through each metering device is mixed, it is ensured that the mixed effect of each raw material, fall
The impact that subsequent production is caused by the fluctuation of low material quality inequality, to improve follow-up sintering effect and ferronickel production effect.Above-mentioned
Mixing arrangement 13 can use the conventional mixing arrangements 13 such as trommel mixer;Above-mentioned mixing arrangement 13 can be located in storehouse 1, it is possible to sets
Outside storehouse 1, such as Fig. 1 and Fig. 3, in the present embodiment, this mixing arrangement 13 is located at outside storehouse 1 near the outlet of above-mentioned formulation.
Further illustrate the structure of this raw material storage, puddle the dehydration of vexed heap for using two stockpile fields 6 to carry out lateritic nickel ore
Situation, i.e. to having two lateritic nickel ore storehouses 2 and two calculogenesis ash silos 3, can arrange above-mentioned raw materials transport vehicle run passage pass through
Logical storehouse 1, i.e. Jun Youyi feed(raw material)inlet, storehouse 1 two ends.In storehouse 1 make heap, feeding operation can be by wheel loader 15, wheeled
Excavator 16 etc. completes, concrete, each raw material cabin windrow, is puddled to stockpile field 6 by lateritic nickel ore storehouse 2 and calculogenesis ash silo 3 feeding
Vexed heap operation etc. can be completed by wheel excavator 16, can be by wheeled dress to the first screening plant 9 by puddling vexed windrow stockyard 6 feeding
Carrier aircraft 15 completes, and can be completed by wheel loader 15 to each dosage bunker 12 feeding.Raw material carrier vehicle runs passage can be as above-mentioned
Wheel loader 15, the operation passage of wheel excavator 16.Additionally, it is possible to motor grab, bridge crane are set in storehouse 1
Deng operation at least partly to substitute the function of above-mentioned vehicle operation.First screening plant the 9, second screening plant 10 and first crushes
Can be connected by ribbon conveyer between device 11.It addition, configurable second breaker 5 near reducing agent storehouse 4, with by reducing agent
Being crushed to qualified granularity, this second breaker 5 is preferably located at the other raw material that reducing agent storehouse 4 is adjacent with wherein side
Between storehouse, to ensure uniformity and the smoothness of storing area structure layout, this second breaker 5 is preferably and uses four rollers to crush
Machine.
The present embodiment, by the layout of making rational planning in space in storehouse 1, solves lateritic nickel ore raw material system in prior art
The extensive unordered production status of standby process;The smooth and easy docking of each inter process, work flow shortens, and working performance is effectively promoted,
And each inter process operation does not interfere with each other, do mechanization operation is launched.
As one of embodiment, described lateritic nickel ore raw material storage also includes automatic control system, described automatic control system
Including central controller, described central controller internal memory contains the nature parameters of each raw material and is calculated by the nature parameters of each raw material
The proportion scheme generated;
Being equipped with the material level detection mechanism that the corresponding raw material of detection is measured in storehouse in each raw material cabin, each described material level detection mechanism is equal
Electrically connect with the input of described central controller, described first metering device, described second metering device, the 3rd
The operating circuit of metering device and each dosage bunker 12 all electrically connects with described central controller input.
For above-mentioned automatic control system, control room can be set in storehouse 1;Above-mentioned central controller uses computer;
Above-mentioned proportion scheme is automatically generated according to database data by computer, after operator confirm, can automatically send operating and refer to
Make and generate runs form, controlled each raw material cabin by system and measured tracking, dosage bunker 12 feed, dosing in storehouse
The operations such as amount control.Wherein, for meeting proportioning accuracy requirement, the feeding coal of each metering device uses closed circuit control, it is achieved
The Automated condtrol of blending process.
Following picture is included but not limited to: process monitoring picture, parameter setting screen, equipment and control in above-mentioned control room
System diagnostics picture, fault alarm picture, trend record picture, accounting logging picture.
By above-mentioned automatic control system, in conjunction with the topology layout in dispensing district and being connected in order and fixed of material transferring equipment
The automated job of amount weighing equipment etc. so that this raw material storage can obtain the control of scientific quantification, and precise and stable dispensing is raw
Product is achieved.It addition, can according to engineering actual conditions etc., adjust layout structure in storehouse 1 size, storehouse 1, material stack height,
The parameter such as raw material type and reserves, to reach the purpose of production stable, effective, efficient.
Embodiment two
The present embodiments relate to a kind of lateritic nickel ore stock preparation system, including the lateritic nickel ore provided such as embodiment one
Raw material storage and sintering machine, described sintering machine is connected with the outlet of described formulation.Such as Fig. 7, by joining that lateritic nickel ore raw material storage is prepared
After system material enters sintering machine sintering, enter blast furnace for smelting ferronickel.
The foregoing is only presently preferred embodiments of the present invention, not in order to limit the present invention, all essences in the present invention
Within god and principle, any modification, equivalent substitution and improvement etc. made, should be included within the scope of the present invention.
Claims (10)
1. a lateritic nickel ore raw material storage, it is characterised in that:
Including storehouse, in described storehouse, space includes storing area and dispensing district;
Including lateritic nickel ore storehouse, calculogenesis ash silo and reducing agent storehouse in described storing area, described storing area has to each raw material cabin
The feed(raw material)inlet of the corresponding raw material of conveying;
Dry territory and dispensing territory is included, from the lateritic nickel ore in described lateritic nickel ore storehouse and calculogenesis ash silo in described dispensing district
Vexed heap to carry out dehydrate to lateritic nickel ore in described dry territory for quick lime, and described dispensing territory receives from described dry territory
And the raw material in described reducing agent storehouse is to prepare raw materials for sintering;Described dispensing district has formulation outlet, and described dispensing territory is with described
Formulation outlet.
Lateritic nickel ore raw material storage the most according to claim 1, it is characterised in that: described lateritic nickel ore storehouse and described quick lime
Storehouse arranged adjacent, and all adjacent to described dry territory.
Lateritic nickel ore raw material storage the most according to claim 2, it is characterised in that: described dry territory and described reducing agent storehouse are equal
Adjacent to described dispensing territory.
Lateritic nickel ore raw material storage the most according to claim 3, it is characterised in that:
Being formed with raw material carrier vehicle in described storehouse and run passage, described operation passage is former to being right against this from described feed(raw material)inlet
The storehouse headwall side of material entrance extends, and is separated to form in space in described storehouse as described storing area and described dispensing district;
Each raw material cabin in described storing area is arranged along described operation channel-length direction, described dry territory and edge, described dispensing territory
Described operation channel-length direction is arranged.
Lateritic nickel ore raw material storage the most according to claim 4, it is characterised in that: described dry territory includes two stockpile fields,
Row both sides, described dispensing territory are divided in stockpile field described in two;Described lateritic nickel ore storehouse and described calculogenesis ash silo are all correspondingly arranged two, institute
State every side, reducing agent storehouse and have a described lateritic nickel ore storehouse and a described calculogenesis ash silo.
Lateritic nickel ore raw material storage the most according to any one of claim 1 to 5, it is characterised in that: set in described dispensing territory
There is a granulating mechanism that lateritic nickel ore is carried out granulate classification, and the big granularity mineral aggregate stockyard of corresponding configuration and small grain size mineral aggregate heap
, the big granularity mineral aggregate that granularity is 10~30mm is stored up in described big granularity mineral aggregate stockyard, and grain is stored up in described small grain size mineral aggregate stockyard
The small grain size mineral aggregate of degree≤10mm.
Lateritic nickel ore raw material storage the most according to claim 6, it is characterised in that be provided with in described dispensing territory:
For being connected to the formulation output device of sintering machine, described formulation output device extend out to the outlet of described formulation
Outward;
For exporting described big granularity mineral aggregate using as the first dosage bunker of hearth layer for sintering and export described small grain size mineral aggregate
Second dosage bunker, described first dosage bunker is connected with described formulation output device, and described second dosage bunker is quantitative by first
Charging gear is connected with described formulation output device;
Reducing agent dosage bunker, described reducing agent dosage bunker arrival end is connected with described reducing agent storehouse by material transfer device, goes out
Mouth end is connected with described formulation output device by the second metering device;
Flux dosage bunker, described flux dosage bunker arrival end is connected with described calculogenesis ash silo by material transfer device, the port of export
It is connected with described formulation output device by the 3rd metering device.
Lateritic nickel ore raw material storage the most according to claim 7, it is characterised in that: described formulation output device include for
Connect the first deferent segment of each dosage bunker and for being connected to the second deferent segment of sintering machine, described first deferent segment and described
It is provided with the mixing arrangement for being mixed with reducing agent and flux by described small grain size mineral aggregate between two deferent segments and is mixed by this
Device is connected.
Lateritic nickel ore raw material storage the most according to claim 7, it is characterised in that: described lateritic nickel ore raw material storage also includes certainly
Autocontrol system, described automatic control system includes that central controller, described central controller internal memory contain the character of each raw material
Parameter and the proportion scheme generated by the nature parameters calculating of each raw material;
Being equipped with the material level detection mechanism that the corresponding raw material of detection measure in storehouse in each raw material cabin, each described material level detection mechanism is equal and institute
State the input electrical connection of central controller, described first metering device, described second metering device, the 3rd quantitative
The operating circuit of charging gear and each dosage bunker all electrically connects with described central controller input.
10. a lateritic nickel ore stock preparation system, it is characterised in that: include as according to any one of claim 6 to 9 is red
Soil nickel minerals raw material storage and sintering machine, described sintering machine is connected with the outlet of described formulation.
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106676261A (en) * | 2017-01-23 | 2017-05-17 | 宝钢德盛不锈钢有限公司 | Efficient uniform mixing process for laterite nickel ore |
Citations (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2002008477A1 (en) * | 2000-07-21 | 2002-01-31 | Nichromet Extraction Inc. | Method for recovering nickel and cobalt from laterite ores |
CN101575654A (en) * | 2009-02-05 | 2009-11-11 | 丁家伟 | Process and device for preparing iron alloy containing nickel and nickel-chromium |
CN102010985A (en) * | 2010-12-27 | 2011-04-13 | 山东泰山钢铁集团有限公司 | Method for smelting ferronickel by laterite-nickel ore added by circular sintering machine-submerged arc furnace |
CN102312081A (en) * | 2011-09-23 | 2012-01-11 | 王凯 | Method of preparing nickel alloy from nickel laterite ores with vehicle rapid reducing furnace |
CN202181335U (en) * | 2011-07-11 | 2012-04-04 | 攀枝花泓兵钒镍有限责任公司 | Transfer device for joining rotary kiln and ore smelting furnace in production of ferronickel with lateritic nickel ore |
CN102912209A (en) * | 2012-10-19 | 2013-02-06 | 四川金广技术开发有限公司 | Process for producing bead ferronickel by rotary hearth furnace through coal-based reduction of red soil nickel oxide ores |
WO2013026093A1 (en) * | 2011-08-22 | 2013-02-28 | Newamu Ip Holdings Pty Ltd | Method for the treatment of acidic leach liquors |
CN103421922A (en) * | 2012-05-25 | 2013-12-04 | 李宾 | Method for producing ferronickel by processing laterite nickel ore in Sulawesi, Indonesia through RKEF technology |
CN103451451A (en) * | 2013-09-27 | 2013-12-18 | 北京科技大学 | Ferro-nickel alloy production technology with laterite nickel ore processed through oxygen enrichment hot air shaft furnace |
CN103602813A (en) * | 2013-11-29 | 2014-02-26 | 四川省冶金设计研究院 | Elevated short-process energy-saving novel RKEF (Rotary Kiln Electric Furnace) ferro-nickel alloy production process and equipment |
CN203559103U (en) * | 2013-11-29 | 2014-04-23 | 四川省冶金设计研究院 | Novel elevated short-process and energy-saving nickel ferroalloy production device based on RKEF (rotary kiln-electric arc furnace) technology |
CN104195279A (en) * | 2014-09-03 | 2014-12-10 | 中南大学 | Process for preparing ferric-nickel from laterite-nickel ore |
CN105483366A (en) * | 2016-01-20 | 2016-04-13 | 连云港宝翔铸造有限公司 | Method for producing ferro-nickel through low-grade high-iron lateritic nickel ores |
CN205837748U (en) * | 2016-06-08 | 2016-12-28 | 中冶南方工程技术有限公司 | Lateritic nickel ore raw material storage and lateritic nickel ore stock preparation system |
-
2016
- 2016-06-08 CN CN201610402785.4A patent/CN106088694B/en active Active
Patent Citations (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2002008477A1 (en) * | 2000-07-21 | 2002-01-31 | Nichromet Extraction Inc. | Method for recovering nickel and cobalt from laterite ores |
CN101575654A (en) * | 2009-02-05 | 2009-11-11 | 丁家伟 | Process and device for preparing iron alloy containing nickel and nickel-chromium |
CN102010985A (en) * | 2010-12-27 | 2011-04-13 | 山东泰山钢铁集团有限公司 | Method for smelting ferronickel by laterite-nickel ore added by circular sintering machine-submerged arc furnace |
CN202181335U (en) * | 2011-07-11 | 2012-04-04 | 攀枝花泓兵钒镍有限责任公司 | Transfer device for joining rotary kiln and ore smelting furnace in production of ferronickel with lateritic nickel ore |
WO2013026093A1 (en) * | 2011-08-22 | 2013-02-28 | Newamu Ip Holdings Pty Ltd | Method for the treatment of acidic leach liquors |
CN102312081A (en) * | 2011-09-23 | 2012-01-11 | 王凯 | Method of preparing nickel alloy from nickel laterite ores with vehicle rapid reducing furnace |
CN103421922A (en) * | 2012-05-25 | 2013-12-04 | 李宾 | Method for producing ferronickel by processing laterite nickel ore in Sulawesi, Indonesia through RKEF technology |
CN102912209A (en) * | 2012-10-19 | 2013-02-06 | 四川金广技术开发有限公司 | Process for producing bead ferronickel by rotary hearth furnace through coal-based reduction of red soil nickel oxide ores |
CN103451451A (en) * | 2013-09-27 | 2013-12-18 | 北京科技大学 | Ferro-nickel alloy production technology with laterite nickel ore processed through oxygen enrichment hot air shaft furnace |
CN103602813A (en) * | 2013-11-29 | 2014-02-26 | 四川省冶金设计研究院 | Elevated short-process energy-saving novel RKEF (Rotary Kiln Electric Furnace) ferro-nickel alloy production process and equipment |
CN203559103U (en) * | 2013-11-29 | 2014-04-23 | 四川省冶金设计研究院 | Novel elevated short-process and energy-saving nickel ferroalloy production device based on RKEF (rotary kiln-electric arc furnace) technology |
CN104195279A (en) * | 2014-09-03 | 2014-12-10 | 中南大学 | Process for preparing ferric-nickel from laterite-nickel ore |
CN105483366A (en) * | 2016-01-20 | 2016-04-13 | 连云港宝翔铸造有限公司 | Method for producing ferro-nickel through low-grade high-iron lateritic nickel ores |
CN205837748U (en) * | 2016-06-08 | 2016-12-28 | 中冶南方工程技术有限公司 | Lateritic nickel ore raw material storage and lateritic nickel ore stock preparation system |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106676261A (en) * | 2017-01-23 | 2017-05-17 | 宝钢德盛不锈钢有限公司 | Efficient uniform mixing process for laterite nickel ore |
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