CN208357011U - The system for recycling particulate antimony oxide ore - Google Patents

The system for recycling particulate antimony oxide ore Download PDF

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CN208357011U
CN208357011U CN201820418101.4U CN201820418101U CN208357011U CN 208357011 U CN208357011 U CN 208357011U CN 201820418101 U CN201820418101 U CN 201820418101U CN 208357011 U CN208357011 U CN 208357011U
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ore pulp
entrance
antimony
ore
outlet
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于传兵
王传龙
刘志国
宋磊
郭素红
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China ENFI Engineering Corp
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China ENFI Engineering Corp
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Abstract

The utility model discloses a kind of systems for recycling particulate antimony oxide ore, which includes: mixing arrangement, have antimony oxide ore entrance, water inlet and mixed ore pulp outlet;Ball-milling device has mixed ore pulp entrance and particulate antimony oxide ore slurry outlet;Gravity concentration apparatus has particulate antimony oxide ore ore pulp entrance, heavy mineral slurry outlet and gravity tailings outlet;Size mixing device, slurry outlet after there is heavy mineral ore pulp entrance and size mixing;Device is activated, there is ore pulp entrance after sizing mixing, activator entrance and activation slurry outlet;Flotation unit has activation ore pulp entrance, collecting agent entrance, foaming agent entrance, the outlet of antimony rough concentrate and flotation tailing outlet;Separation unit has antimony rough concentrate entrance, antimony concentrate outlet and tailing outlet.The antimony concentrate that grade is greater than 24% can be obtained using the system, the rate of recovery of particulate antimony oxide ore is greater than 40%, compared with the rate of recovery of the prior art no more than 10%, has significant economic benefit.

Description

The system for recycling particulate antimony oxide ore
Technical field
The utility model belongs to antimony oxide ore process field, specifically, the utility model relates to recycle particulate antimony oxide The system of mine.
Background technique
Domestic and international researcher has carried out the flotation recovery of particulate antimony bloom, stibiconite and cervantite a large amount of for many years Research, never finds effective beneficiation method.Traditional particulate antimony oxide ore (antimony bloom, stibiconite and cervantite) ore dressing one As using shaking table recycle, the rate of recovery is very low, causes the serious waste of resource.And particulate antimony bloom, stibiconite and cervantite are hard because of it Spend small, grind easily to cross and crush, meet the easy argillization of water, in addition it is about the same with the zero point of quartz, i.e., both flotation behavior and Its is similar, and antimony bloom, stibiconite and cervantite mineral can be hydrolyzed into micro water-wetted surface compound HSbO in water2Or HSbO3, it is caused to be difficult directly to recycle by method for floating.
Therefore, the technology of existing processing antimony oxide ore is further improved.
Utility model content
The utility model is intended to solve at least some of the technical problems in related technologies.For this purpose, this reality It is to propose a kind of system for recycling particulate antimony oxide ore with a novel purpose.Grade can be obtained using the system to be greater than The rate of recovery of 24% antimony concentrate, particulate antimony oxide ore is greater than 40%, compared with the rate of recovery of the prior art no more than 10%, tool There is significant economic benefit.
In the one aspect of the utility model, the utility model proposes a kind of system for recycling particulate antimony oxide ore, roots According to the embodiments of the present invention, which includes:
Mixing arrangement, the mixing arrangement have antimony oxide ore entrance, water inlet and mixed ore pulp outlet;
Ball-milling device, the ball-milling device have mixed ore pulp entrance and particulate antimony oxide ore slurry outlet, the mixing Ore pulp entrance is connected with mixed ore pulp outlet;
Gravity concentration apparatus, the gravity concentration apparatus have particulate antimony oxide ore ore pulp entrance, heavy mineral slurry outlet and gravity treatment tail Mine outlet, the particulate antimony oxide ore ore pulp entrance are connected with the particulate antimony oxide ore slurry outlet;
Size mixing device, slurry outlet after the size mixing device has heavy mineral ore pulp entrance and sizes mixing, the heavy mineral mine Slurry entrance is connected with the heavy mineral slurry outlet;
Device is activated, the activation device is described with ore pulp entrance, activator entrance and activation slurry outlet after sizing mixing Ore pulp entrance is connected with slurry outlet after described size mixing after sizing mixing;
Flotation unit, the flotation unit have activation ore pulp entrance, collecting agent entrance, foaming agent entrance, antimony rough concentrate Outlet and flotation tailing outlet, the activation ore pulp entrance are connected with the activation slurry outlet;
Separation unit, the separation unit have antimony rough concentrate entrance, antimony concentrate outlet and tailing outlet, the antimony coarse-fine Mine entrance is connected with antimony rough concentrate outlet.
According to the utility model embodiment recycling particulate antimony oxide ore system, because antimony oxide ore mineral specific gravity compared with Greatly, the specific gravity of the impurity such as quartz, calcite and thin mud is smaller in mineral, and strengthens in gravitational field in high power, heavy mineral The gravity difference of small impurity is reinforced with specific gravity, and heavy suite can replace light impurity particle to occupy position in sorting bed Set and remain, light impurity particle is then used as tailing to be discharged, as a result, can by gravity treatment realize antimony oxide ore mineral and quartz, The initial gross separation of the impurity such as calcite and thin mud is obtained containing antimony oxide ore mineral, iron mineral, titanium mineral and part coarse granule stone The heavy mineral ore pulp of English and calcite etc..During antimony oxide ore and water contact, the metal sun of antimony oxide ore mineral surfaces Ion oligodynamical is hydrolyzed to metal cation hydroxo complex, which can be adsorbed in antimony oxide by hydrogen bond connection again The hydroxylating metal oxide surface of mine mineral so that active metal cationic occur in mineral surfaces, and produces after collecting agent hydrolysis Raw RCOO- can be acted on the active metal cationic of mineral surfaces, i.e., chemisorption occurs in antimony oxide ore mineral surfaces, dredge Aqua R is outside, to keep antimony oxide ore mineral hydrophobic easily floating, achievees the purpose that flotation antimony rough concentrate.Antimony rough concentrate is through further The antimony concentrate that grade is greater than 22% can be obtained in sorting.Entire technique may make the rate of recovery of antimony to be greater than 50%, not with the prior art The rate of recovery to 10% is compared, and has significant economic benefit.
In addition, can also be had according to the system of the recycling particulate antimony oxide ore of the utility model above-described embodiment following attached The technical characteristic added:
In some embodiments of the utility model, the gravity concentration apparatus is centrifugal ore separator.Be conducive to improve as a result, thin The reselection efficiency of grain antimony oxide ore ore pulp.
In some embodiments of the utility model, the sorting unit includes the roughing device being sequentially connected, scans dress It sets and selecting device.Be conducive to improve the grade of gained antimony concentrate as a result,.
The additional aspect and advantage of the utility model will be set forth in part in the description, partially will be from following description In become obvious, or recognized by the practice of the utility model.
Detailed description of the invention
The above-mentioned and/or additional aspect and advantage of the utility model from the description of the embodiment in conjunction with the following figures will Become obvious and be readily appreciated that, in which:
Fig. 1 is the system structure diagram according to the recycling particulate antimony oxide ore of the utility model one embodiment;
Fig. 2 is to implement recycling particulate according to the system using recycling particulate antimony oxide ore of the utility model one embodiment The method flow schematic diagram of antimony oxide ore.
Specific embodiment
The embodiments of the present invention are described below in detail, examples of the embodiments are shown in the accompanying drawings, wherein from beginning Same or similar element or element with the same or similar functions are indicated to same or similar label eventually.Below by ginseng The embodiment for examining attached drawing description is exemplary, it is intended to for explaining the utility model, and should not be understood as to the utility model Limitation.
In the present invention unless specifically defined or limited otherwise, term " installation ", " connected ", " connection ", " Gu It is fixed " etc. terms shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection, or integral;It can be Mechanical connection, is also possible to be electrically connected;It can be directly connected, two can also be can be indirectly connected through an intermediary The interaction relationship of connection or two elements inside element, unless otherwise restricted clearly.For the common skill of this field For art personnel, the concrete meaning of above-mentioned term in the present invention can be understood as the case may be.
In the one aspect of the utility model, the utility model proposes a kind of system for recycling particulate antimony oxide ore, roots According to the embodiments of the present invention, with reference to Fig. 1, the system include: mixing arrangement 100, ball-milling device 200, gravity concentration apparatus 300, Size mixing device 400, activation device 500, flotation unit 600 and separation unit 700.
Embodiment according to the present utility model, mixing arrangement 100 have antimony oxide ore entrance 101, water inlet 102 and mixing Slurry outlet 103, and be suitable for mixing antimony oxide ore and water, to obtain mixed ore pulp.According to the present utility model one A embodiment, antimony oxide ore may include at least one of antimony bloom, stibiconite and cervantite.It is according to the present utility model another A embodiment, the mass concentration of mixed ore pulp can be 20-70wt%.Inventors have found that if the mass concentration of mixed ore pulp Excessively high, the mobility of ore pulp is deteriorated, and be easy to cause subsequent ball milling machine " swollen tripe ", seriously affects the normal operation of grinding attachment;Such as The mass concentration of fruit mixed ore pulp is too low, and grinding efficiency is deteriorated, the decline of ball mill processing capacity.
Embodiment according to the present utility model, ball-milling device 200 have mixed ore pulp entrance 201 and particulate antimony oxide ore mine Slurry outlet 202, mixed ore pulp entrance 201 are connected with mixed ore pulp outlet 103, and are suitable for mixed ore pulp carrying out ball milling, so as to Obtain particulate antimony oxide ore ore pulp.One embodiment according to the present utility model, partial size is not more than in particulate antimony oxide ore ore pulp The accounting of 0.074mm can be 50-90%.Be conducive to as a result, by ore pulp antimony oxide ore mineral and quartz, calcite etc. it is miscellaneous Matter is levigate, facilitates subsequent reselection and sorting.It should be noted that ball-milling device can be ball mill.
Embodiment according to the present utility model, gravity concentration apparatus 300 have particulate antimony oxide ore ore pulp entrance 301, heavy mineral Slurry outlet 302 and tailing outlet 303, particulate antimony oxide ore ore pulp entrance 301 and 202 phase of particulate antimony oxide ore slurry outlet Even, and it is suitable for particulate antimony oxide ore ore pulp carrying out gravity treatment, to obtain heavy mineral ore pulp and tailing.Inventors have found that because of oxygen The specific gravity of antimony sulfide ore mineral is larger, and stibiconite specific gravity is 5.2, and cervantite specific gravity is 6.5, and antimony bloom specific gravity is 5.7, and quartz, side The specific gravity of the impurity such as Xie Shi and thin mud is smaller, and quartzy specific gravity is 2.5, and calcite specific gravity is that 2.7, thin mud ratio weighs about 2.4.And in height Times strengthen in gravitational field, the gravity difference of heavy mineral and the small tailing of specific gravity will be reinforced, and heavy suite can take It plants oneself and remains in sorting bed for light mineral particle, light mineral particle is then used as tailing to be discharged, and can lead to as a result, The initial gross separation that the tailings such as antimony oxide ore mineral and quartz, calcite and thin mud are realized in gravity treatment is crossed, is obtained containing antimony oxide ore mine Object, iron mineral, titanium mineral and part coarse granule quartz and calcite heavy mineral ore pulp.It should be noted that gravity concentration apparatus can Think centrifugal ore separator.
Embodiment according to the present utility model, ore pulp goes out after size mixing device 400 has heavy mineral ore pulp entrance 401 and sizes mixing Mouth 402, heavy mineral ore pulp entrance 401 is connected with heavy mineral slurry outlet 302, and is suitable for sizing mixing heavy mineral ore pulp, with Just ore pulp after being sized mixing.Specifically, sizing mixing for heavy mineral ore pulp can be realized by way of centrifugal dehydration.It is practical new according to this One embodiment of type, the mass concentration of ore pulp can be 15-40wt% after sizing mixing.Inventors have found that if ore pulp after sizing mixing Mass concentration it is excessively high, the grade of the resulting antimony rough concentrate of flotation is lower;If the mass concentration of ore pulp is too low after sizing mixing, need More flotation devices and floating agent are wanted, and the flotation operation rate of recovery reduces.
Embodiment according to the present utility model, activation device 500 is with ore pulp entrance 501, activator entrance 502 after sizing mixing With activation slurry outlet 503, after sizing mixing ore pulp entrance 501 with size mixing after slurry outlet 402 be connected, and suitable for ore pulp after sizing mixing It is mixed with activator and carries out priming reaction, to obtain activation ore pulp.Specifically, activator is added to size mixing after in ore pulp, Stir 2-6min so that activator with size mixing after ore pulp react abundant.
One embodiment according to the present utility model, the mass ratio of ore pulp and activator can be 100000 after sizing mixing: (10-100).Inventors have found that the dosage of i.e. activator is insufficient, then if the mass ratio of ore pulp and activator is excessively high after sizing mixing Cannot fully active oxidation antimony mineral, cause the rate of recovery of antimony mineral too low;If the quality of ore pulp and activator after sizing mixing Than too low, i.e. the dosage of activator is excessive, or a large amount of gangue is caused to be activated, and on the one hand influences the grade of rough concentrate, another Aspect causes activator level excessive, and reagent cost increases.
Further embodiment according to the present utility model, activator can be in plumbi nitras, copper sulphate, vulcanized sodium At least one.Inventors have found that when activator is plumbi nitras, Pb2+Activator can be adsorbed with electrostatic interaction and chemical bond In antimony mineral surface, increase the surface-active point of antimony mineral, enhances absorption of the collecting agent to antimony mineral, improve the flotation of antimony mineral The rate of recovery.Cu when activator is copper sulphate, in copper sulphate2+It can precipitate or be complexed the CN that inhibiting effect is played in ore pulp-、SO3 2- Then plasma generates activation film in mineral surfaces again.When activator is vulcanized sodium, vulcanized sodium can make oxide ore Surface Creation One layer of sulfide film, the floatability of this sulfide film is close with sulphide ore, and the flotability of mineral thus can be improved.With it He compares activator, and the activation effect of plumbi nitras is best, the rate of recovery highest of antimony oxide ore.
Another embodiment according to the present utility model, the pH value for activating ore pulp can be 6.0-10.0.Inventors have found that If the pH value for activating ore pulp is too low, it is necessary to add a large amount of acidic materials, one side beneficiation reagent increased costs, another aspect Equipment can be caused to corrode;If the pH value for activating ore pulp is excessively high, the floatability of antimony mineral is substantially reduced, and influences returning for antimony mineral Yield.
Embodiment according to the present utility model, flotation unit 600 have activation ore pulp entrance 601, collecting agent entrance 602, Foaming agent entrance 603, antimony rough concentrate outlet 604 and flotation tailing outlet 605, activation ore pulp entrance 601 and activation slurry outlet 503 are connected, and are suitable for activate ore pulp and mix progress flotation with collecting agent and foaming agent, to obtain antimony rough concentrate and flotation tail Mine.Specifically, collecting agent and foaming agent are added in activation ore pulp, 2-6min is stirred, flotation 3-10min obtains antimony rough concentrate. Inventors have found that because antimony oxide ore with water during contacting, the metal cation oligodynamical of antimony oxide ore mineral surfaces, It is hydrolyzed to metal cation hydroxo complex, which can be adsorbed in the hydroxylating of antimony oxide ore mineral by hydrogen bond connection again Metal oxide surface under the action of activator, produces so that active metal cationic occur in mineral surfaces after collecting agent hydrolysis Raw RCOO- can be acted on preferentially with the active metal cationic of mineral surfaces, i.e., preferentially in antimony oxide ore mineral surfaces Absorption is learned, hydrophobing agent R is outside, the hydrophobicity enhancing of antimony oxide ore mineral, then under the action of foaming agent, so that antimony oxide ore mine Object is hydrophobic easily floating, and then achievees the purpose that flotation antimony rough concentrate.
The additive amount of one embodiment according to the present utility model, ore pulp after being sized mixing based on 100000g, collecting agent can be 10~100g, foaming agent additive amount can be 1~10g.Inventors have found that if ore pulp and collecting agent after sizing mixing, foaming agent Mixing mass ratio is excessively high, i.e., collecting agent, the dosage of foaming agent are less than normal, and the floatability of antimony mineral is deteriorated, and causes the antimony concentrate rate of recovery It is substantially reduced.If the mixing mass ratio of ore pulp and collecting agent, foaming agent is too low after sizing mixing, i.e. the dosage of collecting agent, foaming agent Bigger than normal, the floatability of part gangue is preferable, causes the reduction of antimony concentrate grade, beneficiation reagent increased costs.
Further embodiment according to the present utility model, collecting agent can be in RCOONa, butyl xanthate, diethyldithiocarbamates At least one of.Inventors have found that compared with RCOONa collecting agent and traditional collecting agent butyl xanthate, diethyldithiocarbamate etc., to fine fraction Strong with the collecting power of micro-size fraction antimony oxide ore, the rate of recovery of antimony mineral is high.
Another embodiment according to the present utility model, foaming agent can be for selected from terpenic oil, carboxylic acid, methyl-isobutyl first At least one of alcohol.Inventors have found that terpenic oil is easy to get compared with other collecting agents, dosage is few, and price is minimum, at This is also minimum.
There is antimony rough concentrate entrance 701, antimony concentrate to export 702 and for embodiment according to the present utility model, separation unit 700 Tailing outlet 703, antimony rough concentrate entrance 701 are connected with antimony rough concentrate outlet 604, and are suitable for sorting antimony rough concentrate, with Just antimony concentrate and tailing are obtained.One embodiment according to the present utility model, sorting unit may include the roughing being sequentially connected Device scans device and selecting device.Inventors have found that first separation operation that ore pulp enters after sizing mixing is roughing.It sweeps Choosing refer to rougher tailings cannot function as true tailings it is discarded when, the next step operation processing of entrance, in order to improve returning for metal Yield, it is sometimes desirable to can just obtain true tailings by repeatedly scanning.It is selected to refer in ore dressing process, to improve rougher concentration Useful component content, make up to the requirement of industrial quality, the sorting operation being further enriched with to rough concentrate.Antimony is coarse-fine Mine through further roughing, scan with it is selected after can be obtained grade be greater than 22% antimony concentrate.
According to the utility model embodiment recycling particulate antimony oxide ore system, because antimony oxide ore mineral specific gravity compared with Greatly, the specific gravity of the impurity such as quartz, calcite and thin mud is smaller in mineral, and strengthens in gravitational field in high power, heavy mineral The gravity difference of small impurity is reinforced with specific gravity, and heavy suite can replace light impurity particle to occupy position in sorting bed Set and remain, light impurity particle is then used as tailing to be discharged, as a result, can by gravity treatment realize antimony oxide ore mineral and quartz, The initial gross separation of the impurity such as calcite and thin mud is obtained containing antimony oxide ore mineral, iron mineral, titanium mineral and part coarse granule stone The heavy mineral ore pulp of English and calcite etc..During antimony oxide ore and water contact, the metal sun of antimony oxide ore mineral surfaces Ion oligodynamical is hydrolyzed to metal cation hydroxo complex, which can be adsorbed in antimony oxide by hydrogen bond connection again The hydroxylating metal oxide surface of mine mineral so that active metal cationic occur in mineral surfaces, and produces after collecting agent hydrolysis Raw RCOO- can be acted on the active metal cationic of mineral surfaces, i.e., chemisorption occurs in antimony oxide ore mineral surfaces, dredge Aqua R is outside, to keep antimony oxide ore mineral hydrophobic easily floating, achievees the purpose that flotation antimony rough concentrate.Antimony rough concentrate is through further The antimony concentrate that grade is greater than 22% can be obtained in sorting.Entire technique may make the rate of recovery of antimony to be greater than 50%, not with the prior art The rate of recovery to 10% is compared, and has significant economic benefit.
In order to facilitate understanding, recycling particulate antimony oxide ore is implemented to the system using above-mentioned recycling particulate antimony oxide ore below Method be described in detail, embodiment according to the present utility model, with reference to Fig. 2, this method comprises:
S100: antimony oxide ore and water are mixed
In the step, antimony oxide ore and water are mixed, to obtain mixed ore pulp.One according to the present utility model Embodiment, antimony oxide ore may include at least one of antimony bloom, stibiconite and cervantite.It is according to the present utility model another Embodiment, the mass concentration of mixed ore pulp can be 20-70wt%.Inventors have found that if the mass concentration mistake of mixed ore pulp The mobility of height, ore pulp is deteriorated, and be easy to cause subsequent ball milling machine " swollen tripe ", seriously affects the normal operation of grinding attachment;If The mass concentration of mixed ore pulp is too low, and grinding efficiency is deteriorated, the decline of ball mill processing capacity.
S200: mixed ore pulp is subjected to ball milling
In the step, mixed ore pulp is subjected to ball milling, to obtain particulate antimony oxide ore ore pulp.It is according to the present utility model One embodiment, accounting of the partial size no more than 0.074mm can be 50-90% in particulate antimony oxide ore ore pulp.Be conducive to as a result, By in ore pulp antimony oxide ore mineral and the impurity such as quartz, calcite it is levigate, facilitate subsequent reselection and sorting.
S300: particulate antimony oxide ore ore pulp is subjected to gravity treatment
In the step, particulate antimony oxide ore ore pulp is subjected to gravity treatment, to obtain heavy mineral ore pulp and tailing.Invention human hair Existing, because the specific gravity of antimony oxide ore is larger, stibiconite specific gravity is 5.2, and cervantite specific gravity is 6.5, and antimony bloom specific gravity is 5.7, in mineral The specific gravity of the impurity such as quartz, calcite and thin mud is smaller, and quartzy specific gravity is 2.5, and calcite specific gravity is that 2.7, thin mud ratio weighs about 2.4.And strengthen in gravitational field in high power, the gravity difference of heavy mineral and the small tailing of specific gravity will be reinforced, heavy mineral Particle can replace light mineral particle to plant oneself and remain in sorting bed, and light mineral particle is then used as tailing to arrange Out, the initial gross separation that can realize the tailings such as antimony oxide ore mineral and quartz, calcite and thin mud by gravity treatment as a result, is contained There is the heavy mineral ore pulp of antimony oxide ore mineral, iron mineral, titanium mineral and part coarse granule quartz and calcite.
S400: heavy mineral ore pulp is sized mixing
In the step, heavy mineral ore pulp is sized mixing, so as to ore pulp after being sized mixing.Specifically, can be de- by being centrifuged The mode of water realizes sizing mixing for heavy mineral ore pulp.One embodiment according to the present utility model, the mass concentration of ore pulp after sizing mixing It can be 15-40wt%.Inventors have found that if the mass concentration of ore pulp is excessively high after sizing mixing, the resulting antimony rough concentrate of flotation Grade is lower;If the mass concentration of ore pulp is too low after sizing mixing, more flotation devices and floating agent are needed, and flotation is made The industry rate of recovery reduces.
S500: ore pulp is mixed with activator after sizing mixing carries out priming reaction
Ore pulp is mixed with activator in the step, after sizing mixing carries out priming reaction, to obtain activation ore pulp.Specifically , activator is added to after sizing mixing in ore pulp, stir 2-6min so that activator with size mixing after ore pulp react abundant.
One embodiment according to the present utility model, the mass ratio of ore pulp and activator can be 100000 after sizing mixing: (10-100).Inventors have found that the dosage of i.e. activator is insufficient, then if the mass ratio of ore pulp and activator is excessively high after sizing mixing Cannot fully active oxidation antimony mineral, cause the rate of recovery of antimony mineral too low;If the quality of ore pulp and activator after sizing mixing Than too low, i.e. the dosage of activator is excessive, or a large amount of gangue is caused to be activated, and on the one hand influences the grade of rough concentrate, another Aspect causes activator level excessive, and reagent cost increases.
Further embodiment according to the present utility model, activator can be in plumbi nitras, copper sulphate, vulcanized sodium At least one.Inventors have found that when activator is plumbi nitras, Pb2+Activator can be adsorbed with electrostatic interaction and chemical bond In antimony mineral surface, increase the surface-active point of antimony mineral, enhances absorption of the collecting agent to antimony mineral, improve the flotation of antimony mineral The rate of recovery.Cu when activator is copper sulphate, in copper sulphate2+It can precipitate or be complexed the CN that inhibiting effect is played in ore pulp-、SO3 2- Then plasma generates activation film in mineral surfaces again.When activator is vulcanized sodium, vulcanized sodium can make oxide ore Surface Creation One layer of sulfide film, the floatability of this sulfide film is close with sulphide ore, and the flotability of mineral can be improved as a result,.With Other activators compare, and the activation effect of plumbi nitras is best, the rate of recovery highest of antimony oxide ore.
Another embodiment according to the present utility model, the pH value for activating ore pulp can be 6.0-10.0.Inventors have found that If the pH value for activating ore pulp is too low, it is necessary to add a large amount of acidic materials, one side beneficiation reagent increased costs, another aspect Equipment can be caused to corrode;If the pH value for activating ore pulp is excessively high, the floatability of antimony mineral is substantially reduced, and influences returning for antimony mineral Yield.
S600: activation ore pulp is mixed with collecting agent and foaming agent and carries out flotation
In the step, activation ore pulp is mixed with collecting agent and foaming agent and carries out flotation, to obtain antimony rough concentrate and to float Select tailing.Specifically, collecting agent and foaming agent are added in activation ore pulp, 2-6min is stirred, it is coarse-fine that flotation 3-10min obtains antimony Mine.Inventors have found that the metal cation of antimony oxide ore mineral surfaces is micro molten because antimony oxide ore with water during contacting Solution, is hydrolyzed to metal cation hydroxo complex, which can be adsorbed in the hydroxyl of antimony oxide ore mineral by hydrogen bond connection again Base metal oxide surface, so that there is active metal cationic in mineral surfaces, under the action of activator, collecting agent hydrolysis The RCOO- generated afterwards can be acted on preferentially with the active metal cationic of mineral surfaces, i.e., preferentially send out in antimony oxide ore mineral surfaces Biochemical absorption, hydrophobing agent R is outside, the hydrophobicity enhancing of antimony oxide ore mineral, then under the action of foaming agent, so that antimony oxide Mine mineral are hydrophobic easily floating, and then achieve the purpose that flotation antimony rough concentrate.
The additive amount of one embodiment according to the present utility model, ore pulp after being sized mixing based on 100000g, collecting agent can be 10~100g, foaming agent additive amount can be 1~10g.Inventors have found that if ore pulp and collecting agent after sizing mixing, foaming agent Mixing mass ratio is excessively high, i.e., collecting agent, the dosage of foaming agent are less than normal, and the floatability of antimony mineral is deteriorated, and causes the antimony concentrate rate of recovery It is substantially reduced.If the mixing mass ratio of ore pulp and collecting agent, foaming agent is too low after sizing mixing, i.e. the dosage of collecting agent, foaming agent Bigger than normal, the floatability of part gangue is preferable, causes the reduction of antimony concentrate grade, beneficiation reagent increased costs.
Further embodiment according to the present utility model, collecting agent can be in RCOONa, butyl xanthate, diethyldithiocarbamates At least one of.Inventors have found that compared with RCOONa collecting agent and traditional collecting agent butyl xanthate, diethyldithiocarbamate etc., to fine fraction Strong with the collecting power of micro-size fraction antimony oxide ore, the rate of recovery of antimony mineral is high.
Another embodiment according to the present utility model, foaming agent can be for selected from terpenic oil, carboxylic acid, methyl-isobutyl first At least one of alcohol.Inventors have found that terpenic oil is easy to get compared with other collecting agents, dosage is few, and price is minimum, at This is also minimum.
S700: antimony rough concentrate is sorted
In the step, antimony rough concentrate is sorted, to obtain antimony concentrate and tailing.One according to the present utility model Embodiment, sorting may include roughing, scan with it is selected.A specific embodiment according to the present utility model, sorting can wrap Include that one roughing is secondary to be scanned and recleaning.Inventors have found that first separation operation that ore pulp enters after sizing mixing is thick Choosing.Scan refer to rougher tailings cannot function as true tailings it is discarded when, the next step operation processing of entrance, in order to improve metal The rate of recovery, it is sometimes desirable to by repeatedly scanning and can just obtain true tailings.It is selected to refer in ore dressing process, to improve roughing The useful component content of concentrate, makes up to the requirement of industrial quality, the sorting operation being further enriched with to rough concentrate.Antimony Rough concentrate through further roughing, scan with it is selected after can be obtained grade be greater than 22% antimony concentrate.
Implement recycling particulate oxidation according to the system using above-mentioned recycling particulate antimony oxide ore of the utility model embodiment The method of antimony ore, because the specific gravity of antimony oxide ore mineral is larger, the specific gravity of the impurity such as quartz, calcite and thin mud is smaller in mineral, And strengthen in gravitational field in high power, the gravity difference of heavy mineral and the small impurity of specific gravity is reinforced, heavy suite energy Enough light impurity particle is replaced to plant oneself and remain in sorting bed, light impurity particle is then used as tailing to be discharged, as a result, The initial gross separation that the impurity such as antimony oxide ore mineral and quartz, calcite and thin mud can be realized by gravity treatment, obtains containing antimony oxide Mine mineral, iron mineral, titanium mineral and part coarse granule quartz and calcite etc. heavy mineral ore pulp.It is contacted in antimony oxide ore with water During, the metal cation oligodynamical of antimony oxide ore mineral surfaces is hydrolyzed to metal cation hydroxo complex, the network The hydroxylating metal oxide surface that object can be adsorbed in antimony oxide ore mineral by hydrogen bond connection again is closed, so that mineral surfaces occur Active metal cationic, and the RCOO- generated after collecting agent hydrolysis can be acted on the active metal cationic of mineral surfaces, that is, be existed Chemisorption occurs for antimony oxide ore mineral surfaces, and hydrophobing agent R is outside, to keep antimony oxide ore mineral hydrophobic easily floating, reaches flotation The purpose of antimony rough concentrate.The antimony concentrate that grade is greater than 22% can be obtained through further sorting in antimony rough concentrate.Entire technique may make The rate of recovery of antimony is greater than 50%, compared with the rate of recovery of the prior art less than 10%, has significant economic benefit.
Below with reference to specific embodiment, the utility model is described, it should be noted that these embodiments are only Descriptive, without limiting the utility model in any way.
Embodiment 1
A kind of antimony oxide ore of the 1.10wt% containing Sb, antimony mineral mainly include cervantite, antimony bloom and stibiconite.By the oxygen Antimony sulfide ore is mixed with water, is obtained mass concentration and is the mixed ore pulp of 65wt%, and be passed to ball mill ball milling, obtains partial size not Particulate antimony oxide ore ore pulp greater than 0.074mm accounting 50-90%, then using centrifugal ore separator to particulate antimony oxide ore ore pulp Gravity treatment is carried out, heavy mineral ore pulp and tailing are obtained, heavy mineral ore pulp is subjected to centrifugal dehydration, obtaining mass concentration is 33wt%'s Ore pulp after sizing mixing, ore pulp after sizing mixing in mass ratio: plumbi nitras is added in plumbi nitras=100000:20, stirs 2-6min, obtains pH value For 8.5 activation ore pulp, it is then based on ore pulp after 100000g sizes mixing and 30g RCOONa and 3g terpenic oil is added, stir 2-6min, Flotation 3-10min obtains antimony rough concentrate.The antimony rough concentrate obtains grade with recleaning and is through one roughing, secondary scan 22.02% antimony concentrate, antimony recovery 50.05%, compared with the rate of recovery of existing re-selection procedure 9%, the rate of recovery is improved 41.05%.
Embodiment 2
A kind of antimony oxide ore of the 3.30wt% containing Sb, antimony mineral are mainly cervantite, and gangue mineral is mainly quartz, side Solve stone and a small amount of clay mine.The antimony oxide ore is mixed with water, mass concentration is obtained and is the mixed ore pulp of 66wt%, and sent To ball mill ball milling, the particulate antimony oxide ore ore pulp that partial size is not more than 0.074mm accounting 50-90% is obtained, then using centrifugation Ore separators carries out gravity treatment to particulate antimony oxide ore ore pulp, obtains heavy mineral ore pulp and tailing, and it is de- that heavy mineral ore pulp is carried out centrifugation Water, obtaining mass concentration is ore pulp after the sizing mixing of 34wt%, and ore pulp after sizing mixing in mass ratio: plumbi nitras=100000:20 is added Plumbi nitras stirs 2-6min, obtains the activation ore pulp that pH value is 7.8, is then based on ore pulp after 100000g sizes mixing and 40g is added RCOONa and 2g terpenic oil, stirs 2-6min, and flotation 3-10min obtains antimony rough concentrate.The antimony rough concentrate is through one roughing, secondary It scans and obtains the antimony concentrate that grade is 28.10%, antimony recovery 51.50%, with existing re-selection procedure 10% with recleaning The rate of recovery compare, the rate of recovery improves 40.50%.
In the description of this specification, reference term " one embodiment ", " some embodiments ", " example ", " specifically show The description of example " or " some examples " etc. means specific features, structure, material or spy described in conjunction with this embodiment or example Point is contained at least one embodiment or example of the utility model.In the present specification, to the schematic table of above-mentioned term It states and is necessarily directed to identical embodiment or example.Moreover, particular features, structures, materials, or characteristics described can be with It can be combined in any suitable manner in any one or more of the embodiments or examples.In addition, without conflicting with each other, this field Technical staff can by the feature of different embodiments or examples described in this specification and different embodiments or examples into Row combination and combination.
Although the embodiments of the present invention have been shown and described above, it is to be understood that above-described embodiment is Illustratively, it should not be understood as limiting the present invention, those skilled in the art are in the scope of the utility model Inside it can make changes, modifications, alterations, and variations to the above described embodiments.

Claims (3)

1. a kind of system for recycling particulate antimony oxide ore characterized by comprising
Mixing arrangement, the mixing arrangement have antimony oxide ore entrance, water inlet and mixed ore pulp outlet;
Ball-milling device, the ball-milling device have mixed ore pulp entrance and particulate antimony oxide ore slurry outlet, the mixed ore pulp Entrance is connected with mixed ore pulp outlet;
There is particulate antimony oxide ore ore pulp entrance, heavy mineral slurry outlet and gravity tailings to go out for gravity concentration apparatus, the gravity concentration apparatus Mouthful, the particulate antimony oxide ore ore pulp entrance is connected with the particulate antimony oxide ore slurry outlet;
Size mixing device, slurry outlet after the size mixing device has heavy mineral ore pulp entrance and sizes mixing, the heavy mineral ore pulp enter Mouth is connected with the heavy mineral slurry outlet;
Device is activated, the activation device is described to size mixing with ore pulp entrance, activator entrance and activation slurry outlet after sizing mixing Ore pulp entrance is connected with slurry outlet after described size mixing afterwards;
Flotation unit, the flotation unit have activation ore pulp entrance, collecting agent entrance, foaming agent entrance, the outlet of antimony rough concentrate It is exported with flotation tailing, the activation ore pulp entrance is connected with the activation slurry outlet;
There is antimony rough concentrate entrance, antimony concentrate outlet and tailing outlet, the antimony rough concentrate to enter for separation unit, the separation unit Mouth is connected with antimony rough concentrate outlet.
2. system according to claim 1, which is characterized in that the gravity concentration apparatus is centrifugal ore separator.
3. system according to claim 1 or 2, which is characterized in that the separation unit includes the roughing dress being sequentially connected It sets, scan device and selecting device.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108499722A (en) * 2018-03-27 2018-09-07 中国恩菲工程技术有限公司 The system for recycling particulate antimony oxide ore

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108499722A (en) * 2018-03-27 2018-09-07 中国恩菲工程技术有限公司 The system for recycling particulate antimony oxide ore

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