CN209476456U - A kind of vanadium titano-magnetite iron ore concentrate ore dressing upgrading system - Google Patents
A kind of vanadium titano-magnetite iron ore concentrate ore dressing upgrading system Download PDFInfo
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- CN209476456U CN209476456U CN201822001760.0U CN201822001760U CN209476456U CN 209476456 U CN209476456 U CN 209476456U CN 201822001760 U CN201822001760 U CN 201822001760U CN 209476456 U CN209476456 U CN 209476456U
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Abstract
The utility model relates to a kind of vanadium titano-magnetite iron ore concentrate ore dressing upgrading systems, belong to technical field of beneficiation.Including tower grinding machine (1), grading plant (4), magnetic separator (2), concentrator (3) and disc vacuum filter (5);The import of tower grinding machine (1) is connect with the coarse fodder mouth of grading plant (4), the outlet of tower grinding machine (1) is connect with the import of grading plant (4), the fines mouth of grading plant (4) is connect with the import of magnetic separator (2), the concentrate outlet of magnetic separator (2) is connect with concentrator (3) import, the discharge port of concentrator (3) is connect with the import of disc vacuum filter (5), and the filtrate port of disc vacuum filter (5) is connect with concentrator (3) feed inlet.Iron ore concentrate content of the existing iron ore concentrate after three sections are ground the technique of magnetic is increased to 60.5% by original 55% by this system, improves the rate of recovery of iron ore concentrate.Iron ore concentrate stay in grade obtained simultaneously, and realize low cost and environmental protection and energy saving.
Description
Technical field
The utility model relates to a kind of vanadium titano-magnetite iron ore concentrate ore dressing upgrading systems, belong to technical field of beneficiation.
Background technique
Vanadium titano-magnetite is not only the important sources of iron, and the vanadium of association, titanium, chromium, cobalt, nickel, platinum family and scandium etc. are a variety of
Component has very high comprehensive utilization value.Main component is iron TFe20%~45%, TiO in vanadium titano-magnetite23%~
16%, V2O50.15%~0.5%.And Sichuan containing Yanbian, Baima Iron Mine reserves are up to 49.4 hundred million tons.Calculate stock number
Association vanadium V2O512610000 tons, titanium TiO24.74 hundred million tons.Due to the magnetic iron ore and titanium mineral crystal stock in v-ti magnetite ore, particle
It is coarse, and distribution of particles unevenness and difficult fine grinding.So that ore grindability coefficient is about the 1/2 of magnetite quartzite, belong to easily choosing, hardly possible
Grind the ore low with mineral purity.Cause existing other kinds of grinding machine in actual work, understands low yield, energy consumption and cost
It is higher, it is not able to satisfy actual production to the needs of low energy consumption and low cost.
And the prior art mainly uses the technique of more complex three sections mill magnetic of technique, by raw ore by it is rough and torn and in break after,
By the closed circuit screening of straight line shaker, the ore of partition size qualification enters the preceding storehouse of roll mill, it is underproof continue back at thin broken after
It is passed through the closed circuit screening circulation of straight line shaker again, the ore in the preceding storehouse of roll mill then passes through high pressure roller mill and branches to storehouse after roll mill, and
Ore after roll mill in storehouse enters one section of ball mill after throwing tail magnetic separation again multistage screening and is ground, after cyclone is concentrated
It is spare into pump pond.It pumps the ore pulp in pond and enters two sections of ball millings after a stages of magnetic separation, level-one cyclone classification, then through second level eddy flow
Device is classified, the classification of three swirler device enters the progress roughing of two stages of magnetic separation and selected, then through two sections of level-one cyclone classifications, two section two
Grade cyclone classification is selected into the progress of three stages of magnetic separation, and the TFe content in obtained final concentrate still can only achieve 55% left side
The right side causes the rate of recovery of TFe 90% hereinafter, prior art is difficult further to improve TFe's after energy consumption and cost consideration
Content.
Utility model content
Technical problem to be solved in the utility model is that prior art vanadium titano-magnetite granularity is big, the product iron after magnetic separation
TFe content is low in concentrate, and the iron ore concentrate rate of recovery is low.
The technical scheme adopted by the utility model to solve the technical problem is as follows: a kind of vanadium titano-magnetite iron ore concentrate ore dressing mentions
Matter system, including tower grinding machine, grading plant, magnetic separator, concentrator and disc vacuum filter, tower grinding machine by grading plant with
Magnetic separator connection;The import of tower grinding machine and the coarse fodder of grading plant are exported and are connected, the outlet of tower grinding machine and the import of grading plant
Connection, the fine material outlet of grading plant and the import of magnetic separator connect, and the concentrate outlet of magnetic separator is connect with concentrator import, dense
The import of the bottom end discharge port and disc vacuum filter of close machine connects, and the filtrate port and concentrator of disc vacuum filter are fed
Mouth connection.
Further, grading plant described in above-mentioned apparatus is hydrocyclone.
Wherein, the field strength of magnetic separator described in above-mentioned apparatus is 900~1000Gs.
Wherein, the inner barrel of tower grinding machine described in above-mentioned apparatus is provided with spiral agitator, is provided on cylinder lateral wall
Maintenance door, and the width of maintenance door is greater than the width of spiral agitator, the upper end of maintenance door is higher than spiral agitator upper flanges
Connecting pin, lower end are located at the lower part of spiral agitator.
Further, the height of maintenance door is 0.9~1.3 times of spiral agitator length in above-mentioned apparatus.
Further, spiral agitator described in above-mentioned apparatus includes main shaft and is arranged on main shaft lateral wall in the shape of a spiral
The blade of arrangement, and the spacing between adjacent blades is sequentially reduced from the bottom to top.
Further, spacing of the spacing in above-mentioned apparatus between the adjacent blades of lowest part between topmost adjacent blades
1.5~3 times.
The beneficial effects of the utility model are: this system returns vanadium titano-magnetite by the closed loop of tower grinding machine and grading plant
Road, so that the larger vanadium titano-magnetite of granularity passes through grading plant repeatedly and enters the grinding of tower grinding machine, so that finally obtained vanadium titanium magnetic
The granularity of iron ore is smaller, so that the problem of overcoming v-ti magnetite ore difficulty fine grinding.Simultaneously again by v-ti magnetite obtained above
Full Iron grade in iron ore concentrate is effectively increased to 60.5% by original 55.0% using magnetic separator by mine, and can be incited somebody to action in actual production
The rate of recovery of TFe is increased to 97% or more in iron ore concentrate, overcome existing multi-stage magnetic separation be not able to satisfy and meanwhile upgrade and
The needs of the rate of recovery.Finally since the granule size of the vanadium titano-magnetite come out through magnetic separator substantially reduces, and it is final to guarantee
The water content of product iron ore concentrate is 10% hereinafter, this system guarantees the water content of product by concentrator and disc vacuum filter
Meet technique requirement.
Detailed description of the invention
Fig. 1 is a kind of flow diagram of the utility model;
Fig. 2 is the utility model tower grinding machine broken section structural schematic diagram.
In the figure, it is marked as 1 is tower grinding machine, 11 be cylinder, and 12 be maintenance door, and 13 be spiral agitator, and 131 be main shaft, 132
It is blade, 14 be output shaft, and 2 be magnetic separator, and 3 be concentrator, and 4 be grading plant, and 5 be disc vacuum filter.
Specific embodiment
The present invention will be further described with reference to the accompanying drawing.
As depicted in figs. 1 and 2, a kind of vanadium titano-magnetite iron ore concentrate ore dressing upgrading system of the utility model, including tower mill
Machine 1, grading plant 4, magnetic separator 2, concentrator 3 and disc vacuum filter 5, tower grinding machine 1 pass through grading plant 4 and magnetic separator 2
Connection;The import of tower grinding machine 1 and the coarse fodder of grading plant 4 are exported and are connected, and the outlet of tower grinding machine 1 and the import of grading plant 4 connect
It connecing, the fine material outlet of grading plant 4 is connect with the import of magnetic separator 2, and the concentrate outlet of magnetic separator 2 is connect with 3 import of concentrator,
The bottom end discharge port of concentrator 3 is connect with the import of disc vacuum filter 5, the filtrate port of disc vacuum filter 5 with it is dense
The connection of 3 feed inlet of machine.It will be appreciated to those of skill in the art that tower grinding machine 1 and magnetic separator 2 are connected by grading plant 4
Get up, so that the iron ore concentrate come in through upper section process is first screened through grading plant 4, simultaneously because the import and classification of tower grinding machine 1
The coarse fodder of device 4 exports connection, the biggish iron ore concentrate particle of granularity can be entered tower grinding machine 1 and ground, so that tower grinding machine 1 and classification
Device 4 formed a closed loop ground repeatedly so that the biggish ore of granularity is directly entered tower grinding machine 1, make its finally meet-
The requirement of 325 mesh.And the fine material outlet of grading plant 4 is connect with the import of magnetic separator 2 so that qualified iron ore concentrate then directly into
Enter magnetic separator 2 and carry out magnetic separation, the process of this sizing screening can reduce the energy consumption of tower grinding machine 1, reduce it is total consume energy so that reduce at
This.And the outlet of magnetic separator 2 is connect with the import of concentrator 3, so that the ore after magnetic separation is directly entered the concentration of concentrator 3,
Concentration higher ore in bottom directly enters disc vacuum filter 5 from outlet at bottom and is filtered except water process, and upper end is clear
Liquid then passes through overflow port and flows out spare, and filter cake made from disc vacuum filter 5 is final products, and the water content of filter cake is
9.5% or so, meet process requirements, while to increase rate of recovery this system of iron ore concentrate also by the filter of disc vacuum filter 5
Liquid mouth is connect with the import of concentrator 3, so that the iron ore concentrate in filtrate can again flow into concentrator 3 and carry out concentration.It is practical
The TFe in former iron ore concentrate can be increased to 60.5% by original 55.0% by this system in production, meet its final product and contain
Water is lower than 10% purpose.
Preferably, grading plant 4 described in above-mentioned apparatus is hydrocyclone.Skilled artisans appreciate that
It is, since the smaller iron ore concentrate granularity come out after the grinding of tower grinding machine 1 again of the ore grain size of front-end-of-line out is in 325 mesh
Left and right, conventional screening plant cannot achieve the purpose of screening, therefore the present apparatus is that further preferred grading plant 4 revolves for waterpower
Device is flowed, convenient for collecting and sieving iron ore concentrate.
Preferably, the field strength of magnetic separator 2 described in above-mentioned apparatus is 900~1000Gs.Those skilled in the art can manage
The inventor of solution, the present apparatus show that the field strength of preferred magnetic separator 2 is 900~1000Gs by test of many times, due to entering
The ore grain size of magnetic separator 2 is smaller to reach -325 mesh, and the preferably field strength of magnetic separator 2 is 900~1000Gs, so that it may so that more
Iron ore concentrate is deposited on 2 roller of magnetic separator, improves the rate of recovery of iron ore concentrate.
Preferably, the cylinder 11 of tower grinding machine described in above-mentioned apparatus 1 is internally provided with spiral agitator 13,11 side wall of cylinder
On be provided with maintenance door 12, and the width of maintenance door 12 is greater than the width of spiral agitator 13, and the upper end of maintenance door 12 is higher than spiral shell
13 upper flanges connecting pin of blender is revolved, lower end is located at the lower part of spiral agitator 13.Skilled artisans appreciate that
Be, existing tower grinding machine 1 maintenance when, generally require all to unload upper driving device, by spiral agitator 13 entirely from
Top extraction, this structure cause garter coil blender 13 time-consuming and laborious.This system is just allowing for this problem, preferably exists
Maintenance door 12 for dismounting spiral agitator 13 is set on 1 cylinder of tower grinding machine, 11 side wall.Since 13 upper end of spiral agitator is straight
The output shaft 14 for connecting flange and the transmission device of tower grinding machine 1 is connected and fixed, and is the fastener of junction easy to disassemble.This dress
The upper end for setting preferred maintenance door 12 is higher than spiral agitator 13 and 1 output shaft of tower grinding machine, 14 flanged ends, simultaneously because spiral
Blender 13 has certain length, for convenient for it is extracted out from maintenance door 12, therefore the width of the preferred maintenance door 12 of the present apparatus
Greater than the width of spiral agitator 13, while the lower end of maintenance door 12 is located at the lower part of spiral agitator 13.
Preferably, the height of maintenance door 12 is 0.9~1.3 times of 13 length of spiral agitator in above-mentioned apparatus.This field
Technical staff is convenient for medium ball, it is understood that since there are gaps between spiral agitator 13 Ying Yuta grinding machine, 1 inner wall
Movement.Therefore the height of the preferred maintenance door 12 of the present apparatus is 0.9~1.3 times of 13 length of spiral agitator.When maintenance door 12
When height is 1.3 times of 13 length of spiral agitator, the height of maintenance door 12 should be greater than spiral agitator 13 and output shaft 14
It junction, can be directly by the horizontal taking-up of spiral agitator 13 to the length of 13 lower end of spiral agitator.When maintenance door 12
When height is 0.9 times of 13 length of spiral agitator, 13 tiltable of spiral agitator is taken out out of barrel 11.
Preferably, spiral agitator 13 described in above-mentioned apparatus includes main shaft 131 and is arranged on 131 lateral wall of main shaft
The blade 132 arranged in the shape of a spiral, and the spacing between adjacent blades 132 is sequentially reduced from the bottom to top.Those skilled in the art
, it is understood that the present apparatus can directly drive 13 turns of spiral agitator by the actuator and linkage on 1 top of tower grinding machine
It is dynamic, and spiral agitator 13 includes main shaft 131 and blade 132, blade 132 is arranged in the shape of a spiral on 131 lateral wall of main shaft, from
And iron ore concentrate is ground in tower grinding machine 1, and the spacing between the preferred adjacent blades 132 of the present apparatus successively subtracts from the bottom to top
Small, so that in the unit time, iron ore concentrate reduces along the displacement that 131 axis direction of main shaft is run, namely be increased iron ore concentrate with
The time of contact of medium ball, so that the granularity in 1 exit of tower grinding machine meets needs.Since blade 132 is on 131 lateral wall of main shaft
Helically line is arranged, therefore the spacing between the adjacent blades 132 of present apparatus record is the adjacent two parts of blade 132 along main shaft 131
Axial distance.Simultaneously because bottom is arranged in the import of tower grinding machine 1 and the spacing between bottom adjacent blades 132 is larger, can
Effectively avoid spiral agitator 13 stuck.
Preferably, the spacing in above-mentioned apparatus between the adjacent blades 132 of lowest part is between topmost adjacent blades 132
1.5~3 times of spacing.It will be appreciated to those of skill in the art that the adjacent blades of the further preferred lowest part of the present apparatus
1.5~3 times of spacing of the spacing between topmost adjacent blades 132 between 132, the iron essence so that main shaft 131 rotates a circle
Mine reduces along the axial displacement of main shaft 131, and then increases the time of contact of iron ore concentrate and medium ball, that is to say and increases grinding
Time greatly reduces the granule size of upper end outlet iron ore concentrate.
Claims (7)
1. a kind of vanadium titano-magnetite iron ore concentrate ore dressing upgrading system, it is characterised in that: including tower grinding machine (1), grading plant (4),
Magnetic separator (2), concentrator (3) and disc vacuum filter (5), tower grinding machine (1) are connected by grading plant (4) and magnetic separator (2)
It connects;The import of tower grinding machine (1) and the coarse fodder of grading plant (4) are exported and are connected, outlet and grading plant (4) of tower grinding machine (1)
Import connection, the fine material outlet of grading plant (4) connect with the import of magnetic separator (2), the concentrate of magnetic separator (2) export with it is dense
Machine (3) import connection, the bottom end discharge port of concentrator (3) are connect with the import of disc vacuum filter (5), disk vacuum filter
The filtrate port of machine (5) is connect with concentrator (3) feed inlet.
2. a kind of vanadium titano-magnetite iron ore concentrate ore dressing upgrading system according to claim 1, it is characterised in that: the classification
Device (4) is hydrocyclone.
3. a kind of vanadium titano-magnetite iron ore concentrate ore dressing upgrading system according to claim 1, it is characterised in that: the magnetic separation
The field strength of machine (2) is 900~1000Gs.
4. special according to claim 1 to a kind of vanadium titano-magnetite iron ore concentrate ore dressing upgrading system described in 3 any claims
Sign is: the cylinder (11) of the tower grinding machine (1) is internally provided with spiral agitator (13), is provided with inspection on cylinder (11) side wall
It repairs door (12), and the width of maintenance door (12) is greater than the width of spiral agitator (13), the upper end of maintenance door (12) is higher than spiral
Blender (13) upper flanges connecting pin, lower end are located at the lower part of spiral agitator (13).
5. a kind of vanadium titano-magnetite iron ore concentrate ore dressing upgrading system according to claim 4, it is characterised in that: maintenance door
(12) height is 0.9~1.3 times of spiral agitator (13) length.
6. a kind of vanadium titano-magnetite iron ore concentrate ore dressing upgrading system according to claim 4, it is characterised in that: the spiral
Blender (13) includes the blade (132) arranged in the shape of a spiral of main shaft (131) and setting on main shaft (131) lateral wall, and
Spacing between adjacent blades (132) is sequentially reduced from the bottom to top.
7. a kind of vanadium titano-magnetite iron ore concentrate ore dressing upgrading system according to claim 6, it is characterised in that: lowest part
1.5~3 times of spacing of the spacing between topmost adjacent blades (132) between adjacent blades (132).
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CN114235647A (en) * | 2021-12-17 | 2022-03-25 | 西藏华泰龙矿业开发有限公司 | Mining whirl elutriation system in laboratory |
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CN114235647A (en) * | 2021-12-17 | 2022-03-25 | 西藏华泰龙矿业开发有限公司 | Mining whirl elutriation system in laboratory |
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