CN109292809A - The application of the method for purification, gypsum and gypsum of titanium gypsum - Google Patents

The application of the method for purification, gypsum and gypsum of titanium gypsum Download PDF

Info

Publication number
CN109292809A
CN109292809A CN201811166947.4A CN201811166947A CN109292809A CN 109292809 A CN109292809 A CN 109292809A CN 201811166947 A CN201811166947 A CN 201811166947A CN 109292809 A CN109292809 A CN 109292809A
Authority
CN
China
Prior art keywords
gypsum
flotation
purification
titanium
titanium gypsum
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201811166947.4A
Other languages
Chinese (zh)
Inventor
曾冠武
黎建明
郝建璋
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Pangang Group Panzhihua Iron and Steel Research Institute Co Ltd
Original Assignee
Pangang Group Panzhihua Iron and Steel Research Institute Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Pangang Group Panzhihua Iron and Steel Research Institute Co Ltd filed Critical Pangang Group Panzhihua Iron and Steel Research Institute Co Ltd
Priority to CN201811166947.4A priority Critical patent/CN109292809A/en
Publication of CN109292809A publication Critical patent/CN109292809A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01FCOMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
    • C01F11/00Compounds of calcium, strontium, or barium
    • C01F11/46Sulfates
    • C01F11/468Purification of calcium sulfates
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D1/00Flotation
    • B03D1/001Flotation agents
    • B03D1/002Inorganic compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D1/00Flotation
    • B03D1/001Flotation agents
    • B03D1/004Organic compounds
    • B03D1/012Organic compounds containing sulfur
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D1/00Flotation
    • B03D1/001Flotation agents
    • B03D1/004Organic compounds
    • B03D1/016Macromolecular compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D1/00Flotation
    • B03D1/001Flotation agents
    • B03D1/018Mixtures of inorganic and organic compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D2201/00Specified effects produced by the flotation agents
    • B03D2201/005Dispersants
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D2201/00Specified effects produced by the flotation agents
    • B03D2201/007Modifying reagents for adjusting pH or conductivity
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D2201/00Specified effects produced by the flotation agents
    • B03D2201/02Collectors
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D2201/00Specified effects produced by the flotation agents
    • B03D2201/04Frothers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D2201/00Specified effects produced by the flotation agents
    • B03D2201/06Depressants
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2006/00Physical properties of inorganic compounds
    • C01P2006/80Compositional purity

Abstract

The present invention provides the applications of a kind of method of purification of titanium gypsum, gypsum and gypsum, are related to the technical field of industrial chemicals processing.The method of purification of titanium gypsum provided by the invention, including sizing mixing, flotation and separation, wherein, in flotation step, used flotation agent includes capturing agent, optional foaming agent, optional dispersing agent, optional activator, optional inhibitor and optional pH regulator.This method of purification simple process reduces the cost for purification of titanium gypsum, is rich in iron in the by-product obtained after purification, can be used for sintered ironmaking, realize the efficient utilization of titanium gypsum.Gypsum provided by the invention, the purity is high of the dihydrate gypsum contained can substitute the natural gypsum as construction material, to alleviate the problem of titanium gypsum excessively cannot be rehoused and utilize and cause the wasting of resources and environmental pollution completely.

Description

The application of the method for purification, gypsum and gypsum of titanium gypsum
Technical field
The present invention relates to industrial chemicals manufacture fields, more particularly, to a kind of method of purification of titanium gypsum, gypsum and gypsum Application.
Background technique
Titanium dioxide is one of the white pigment that performance is best now, is widely used in coating, plastics, papermaking, chemical fibre, makeup The industries such as product, production method is based on sulfuric acid process.However by-product titanium will be generated using sulfuric acid process 1 ton of titanium dioxide of every production 5~6 tons of gypsum, China generates about 8,000,000 tons of titanium gypsum every year.If these titanium gypsums cannot be disposed and be utilized well, not only It will cause the wasting of resources, and can cause seriously to pollute to ecological environment.
The main component of titanium gypsum is dihydrate gypsum, and impurity is mainly iron, magnesium, aluminium and titanium.The content of iron is most in impurity Height, mainly with Fe2O3Form exist.Since the content of gypsum in titanium gypsum is low, color is partially red or partially yellow, using effect and Application range is severely impacted.Currently, titanium gypsum is only used for construction material such as cement retarder, mixing cementing material, road floor Material etc., using extremely limiting to.
To realize making full use of for titanium gypsum, need to purify titanium gypsum, removal influences the main miscellaneous of its color Matter Fe2O3.Currently, the method for purification of titanium gypsum mainly has recrystallization method, the precipitation method and organic extraction.Using three of the above side Though method can effectively realize the purification to titanium gypsum, have the defects that certain.Recrystallization method technique is cumbersome, and energy consumption is high; Precipitation method filtration difficulty, it is inconvenient;Organic extraction is at high cost.
In view of this, the present invention is specifically proposed.
Summary of the invention
The first purpose of this invention is to provide a kind of method of purification of titanium gypsum, and simple process, production cost is low, can To overcome the above problem or at least be partially solved the above problem.
Second object of the present invention is to provide a kind of gypsum, which purifies to obtain by titanium gypsum, to alleviate titanium The problem of gypsum excessively cannot be rehoused and utilize and cause the wasting of resources and environmental pollution.
Third object of the present invention is to provide a kind of application of gypsum in construction material, and the gypsum purified can To replace the natural gypsum completely.
In order to solve the above-mentioned technical problem, the following technical scheme is adopted:
According to the first aspect of the invention, the present invention provides a kind of methods of purification of titanium gypsum, including size mixing, flotation and Separation;
Wherein, in the flotation step, used flotation agent includes capturing agent, optional foaming agent, optional dispersion Agent, optional activator, optional inhibitor and optional pH regulator.
As further technical solution, in the step of sizing mixing, by titanium gypsum and water to be processed according to mass ratio be 1:3 ~20 are uniformly mixed;
Preferably, in the step of sizing mixing, titanium gypsum to be processed is mixed according to mass ratio for 1:5~10 with water It is even;
Preferably, the water further includes the water that separating step obtains.
As further technical solution, in the flotation step, flotation agent is added into the ore pulp sized mixing, mixing is equal It is even, it carries out flotation and obtains concentrate foam and tailing ore pulp.
As further technical solution, the capturing agent includes neopelex, lauryl sodium sulfate, oleic acid At least one of sodium and sodium salicylate;
Preferably, the mass ratio of the additional amount of the capturing agent and titanium gypsum be 0.3~2:1000, preferably 0.5~ 1.2:1000;
Preferably, the foaming agent includes at least one of terpinol, camphorated oil, pinke needle oil and butyl ether oil;
Preferably, the mass ratio of the additional amount of the foaming agent and titanium gypsum be 0.3~2:1000, preferably 0.5~ 1.2:1000;
Preferably, the dispersing agent includes in ethyl alcohol, waterglass, calcium stearate, calgon, cellulose and glycerol It is at least one;
Preferably, the mass ratio of the additional amount of the dispersing agent and ore pulp is 1~10:1000;
Preferably, the activator includes at least one of sulfuric acid, sulfurous acid, oxalic acid and sodium carbonate;
Preferably, the mass ratio of the additional amount of the activator and titanium gypsum be 0.3~2:1000, preferably 0.5~ 1.2:1000;
Preferably, the inhibitor includes at least one of vulcanized sodium, lime, dextrin and starch;
Preferably, the mass ratio of the additional amount of the inhibitor and titanium gypsum be 0.3~2:1000, preferably 0.5~ 1.2:1000;
Preferably, the pH regulator includes at least one of sulfuric acid, hydrochloric acid, sodium hydroxide and calcium hydroxide;
Preferably, the pH of ore pulp is adjusted to 6~8 using pH regulator.
As further technical solution, the flotation is a flotation or multiple flotation.
It is described to be uniformly mixed to be uniformly mixed by churned mechanically mode as further technical solution.
As further technical solution, in the separating step, the concentrate foam and tailing ore pulp that respectively obtain flotation It is separated by solid-liquid separation, obtains gypsum and rich iron charge;
Preferably, described be separated by solid-liquid separation includes at least one of sedimentation, filtering and centrifugation;
It preferably, further include drying steps after the solid-liquid separation step.
As further technical solution, the isolated water returns to step cycle use of sizing mixing.
According to the second aspect of the invention, the present invention provides a kind of gypsum that the method for purification using titanium gypsum obtains.
According to the third aspect of the invention we, the application the present invention provides a kind of gypsum in construction material.
Compared with prior art, the present invention include it is following the utility model has the advantages that
The method of purification of titanium gypsum provided by the invention, by the way that successively titanium gypsum is sized mixing, flotation and lock out operation Purification gypsum is obtained, simple process reduces the cost for purification of titanium gypsum, is rich in iron in the by-product obtained after purification, can use In sintered ironmaking, the efficient utilization of titanium gypsum is realized.Gypsum provided by the invention, the purity is high of the dihydrate gypsum contained, can The substitution natural gypsum completely excessively cannot be rehoused and be utilized and cause the wasting of resources to alleviate titanium gypsum as construction material And the problem of environmental pollution.
Detailed description of the invention
It, below will be to specific in order to illustrate more clearly of the specific embodiment of the invention or technical solution in the prior art Embodiment or attached drawing needed to be used in the description of the prior art be briefly described, it should be apparent that, it is described below Attached drawing is some embodiments of the present invention, for those of ordinary skill in the art, before not making the creative labor It puts, is also possible to obtain other drawings based on these drawings.
Fig. 1 is the method for purification flow chart of titanium gypsum provided in an embodiment of the present invention.
Specific embodiment
Embodiment of the present invention is described in detail below in conjunction with embodiments and examples, but this field skill Art personnel will be understood that following embodiments and embodiment are merely to illustrate the present invention, and are not construed as limiting model of the invention It encloses.Based on the embodiments of the present invention, obtained by those of ordinary skill in the art without making creative efforts Every other embodiment, shall fall within the protection scope of the present invention.The person that is not specified actual conditions, according to normal conditions or manufacturer builds The condition of view carries out.Reagents or instruments used without specified manufacturer is the conventional production that can be obtained by commercially available purchase Product.
In a first aspect, the present invention provides a kind of methods of purification of titanium gypsum, including size mixing, flotation and separation, wherein floating Select in step, used flotation agent include capturing agent, optional foaming agent, optional dispersing agent, optional activator, optionally Inhibitor and optional pH regulator.
Titanium gypsum is the Main By product of sulfuric acid legal system titanium dioxide, and main component is dihydrate gypsum, and impurity is mainly Iron, magnesium, aluminium and titanium.The content highest of iron in impurity, mainly with Fe2O3Form exist.Due to the content of gypsum in titanium gypsum Low, color is partially red or partially yellow, and using effect and application range are severely impacted.Currently, titanium gypsum is only used for construction material Such as cement retarder, mixing cementing material, road layer material.It realizes making full use of for titanium gypsum, needs to carry out titanium gypsum Purification, removal influence the major impurity Fe of its color2O3
Floatation is suitable for by floatingly selecting mineral from ore pulp using the physics of mineral surfaces and the difference of chemical property The thin dip dyeing ore of particle is sorted, is had a wide range of applications in mining processing industry.Flotation agent is common reagent in floatation process, It can be used for adjusting the chemical property of flotation material and flotation medium, to expand the floatability difference of flotation storeroom, improve flotation Efficiency.Flotation agent includes capturing agent, foaming agent, dispersing agent, activator, inhibitor and pH regulator.
Capturing agent by the polar group that can have an effect with mineral particle surface and hydrophobic effect non-polar group group At.Due to the surface of most of mineral grains be it is hydrophilic, carry out flotation when need to be improved its floatability.Capturing agent is added to mine After in slurry, it can be adsorbed on the surface of mineral grain, polar group forms hydrophobic outwardly towards mineral particle surface, non-polar group Film makes mineral grain have floatability, realizes the flotation of mineral.
Foaming agent is the surface active molecules with hydrophilic radical and hydrophobic grouping, orientable to be adsorbed on gas-liquid interface, is dropped The surface tension of low solution makes the air being filled be easy to disperse into bubble, and generates stable foam.Foaming agent has with capturing agent Synergy is adsorbed in mineral particle surface jointly, and mineral is promoted to float.
Dispersing agent is mainly used for that thin ore particle is prevented to assemble, and biggish ore particle is dispersed into fine grained, and is allowed in monomer Dispersity.
Activator can enhance mineral with the binding ability of capturing agent, and indissoluble mineral is made to be activated and be floated.
Inhibitor can improve mineral hydrophily or mineral is prevented to act on capturing agent, be suppressed its floatability.
PH regulator is by adjusting mash acid alkalinity, control mineral surfaces characteristic, ore pulp chemical composition and various medicaments Action condition, improve flotation effect.
It should be noted that above-mentioned " optionally " refer to above-mentioned foaming agent, dispersing agent, activator, inhibitor and pH tune Whole dose can add, and can not also add.When only using capturing agent, the floatability of gypsum can be improved, realize the floating of gypsum Choosing;Further, after adding foaming agent, dispersing agent, activator, inhibitor and pH regulator, capturing agent and stone can be reinforced The combination of cream improves the floatability of gypsum, improves flotation effect.It, can according to the actual situation or process requirements in practical application It is added.
The present invention extracts the gypsum in titanium gypsum, and Fe using floatation2O3Equal impurity stay in ore pulp, to realize to titanium stone The purification of cream.According to the present invention, titanium gypsum is uniformly mixed with water according to certain volume ratio first, is tuned into ore pulp, then to Flotation agent is added in ore pulp, is uniformly mixed, and is carried out flotation and is obtained concentrate foam and tailing ore pulp, the concentrate for finally obtaining flotation Foam and tailing ore pulp are separated by solid-liquid separation, and purification gypsum and rich iron charge are obtained.
Present invention process is simple, reduces the cost for purification of titanium gypsum, is rich in iron in the by-product obtained after purification, can use In sintered ironmaking, the efficient utilization of titanium gypsum is realized.
As further technical solution, in step of sizing mixing, by titanium gypsum and water to be processed according to mass ratio be 1:3~20 It is uniformly mixed.
In the present invention, titanium gypsum and the typical but non-limiting volume ratio of water are as follows: 1:3,1:5,1:7,1:9,1:11,1: 13,1:15,1:17,1:19 or 1:20.
In the present invention, titanium gypsum and water are subjected to the ore pulp for being mixed to get suitable flotation, the ratio of titanium gypsum and water The effect of flotation is influenced, when the ratio of titanium gypsum and water is smaller, the concentration of ore pulp is diluter, needs to add more flotation agent The flotation effect of rationality can be reached, production capacity is low;When the large percentage of titanium gypsum and water, ore pulp is excessively sticky, is unfavorable for Mineral grain dispersion, influences separating effect.
Preferably, in step of sizing mixing, titanium gypsum to be processed is uniformly mixed with water according to mass ratio for 1:5~10.
By the further adjustment and optimization to titanium gypsum and water volume ratio, so that the ore pulp being prepared more is suitable for Floating operation, refining effect are more preferable.
Preferably, water further includes the water that separating step obtains.
In the present invention, titanium gypsum dissolved dilution is prepared to the ore pulp of flotation due to going back in flotation step using water Flotation agent is added, so the water water that also optional separating step obtains.
As further technical solution, in flotation step, flotation agent is added into the ore pulp sized mixing, is uniformly mixed, It carries out flotation and obtains concentrate foam and tailing ore pulp.
In the present invention, the surface that can be adsorbed on bubble after flotation agent is in conjunction with gypsum, is separated in the form of foam Come.Concentrate foam and foam-like tailing are obtained after flotation.
As further technical solution, capturing agent include neopelex, lauryl sodium sulfate, enuatrol and At least one of sodium salicylate.
It is understood that the present invention is not particularly limited the concrete type of the capturing agent, including but not limited to ten At least one of dialkyl benzene sulfonic acids sodium, lauryl sodium sulfate, enuatrol and sodium salicylate or those skilled in the art The well known other kinds of capturing agent with above-mentioned substance with similarity.
Preferably, the mass ratio of the additional amount of capturing agent and titanium gypsum be 0.3~2:1000, preferably 0.5~1.2: 1000.It is typical but non-limiting, such as the mass ratio of capturing agent and titanium gypsum can be 0.3:1000,0.5:1000,0.7: 1000,0.9:1000,1.1:1000,1.3:1000,1.5:1000,1.7:1000,1.9:1000 or 2:1000.
By the further adjustment and optimization to capturing agent and titanium gypsum mass ratio, the flotation effect of titanium gypsum is improved.
Preferably, foaming agent includes at least one of terpinol, camphorated oil, pinke needle oil and butyl ether oil.
It is understood that the present invention is not particularly limited the concrete type of the foaming agent, it is including but not limited to loose At least one of oleyl alcohol, camphorated oil, pinke needle oil and butyl ether oil well known to those skilled in the art have with above-mentioned substance The other kinds of foaming agent of similarity.
Preferably, the mass ratio of the additional amount of foaming agent and titanium gypsum be 0.3~2:1000, preferably 0.5~1.2: 1000.It is typical but non-limiting, such as the mass ratio of foaming agent and titanium gypsum can be 0.3:1000,0.5:1000,0.7: 1000,0.9:1000,1.1:1000,1.3:1000,1.5:1000,1.7:1000,1.9:1000 or 2:1000.
By the further adjustment and optimization to foaming agent and titanium gypsum mass ratio, the flotation effect of titanium gypsum is improved.
Preferably, dispersing agent include in ethyl alcohol, waterglass, calcium stearate, calgon, cellulose and glycerol at least It is a kind of.
It is understood that the present invention is not particularly limited the concrete type of the dispersing agent, including but not limited to second At least one of alcohol, waterglass, calcium stearate, calgon, cellulose and glycerol or those skilled in the art are known With above-mentioned substance have similarity other kinds of dispersing agent.
Preferably, the mass ratio of the additional amount of dispersing agent and ore pulp is 1~10:1000.It is typical but non-limiting, such as The mass ratio of dispersing agent and ore pulp can be 1:1000,2:1000,3:1000,4:1000,5:1000,6:1000,7:1000,8: 1000,9:1000 or 10:1000.
By the further adjustment and optimization to dispersing agent and ore pulp mass ratio, the flotation effect of titanium gypsum is improved.
Preferably, activator includes at least one of sulfuric acid, sulfurous acid, oxalic acid and sodium carbonate.
It is understood that the present invention is not particularly limited the concrete type of the activator, including but not limited to sulphur At least one of acid, sulfurous acid, oxalic acid and sodium carbonate or it is well known to those skilled in the art have with above-mentioned substance it is similar The other kinds of activator of property.
Preferably, the mass ratio of the additional amount of activator and titanium gypsum be 0.3~2:1000, preferably 0.5~1.2: 1000.It is typical but non-limiting, such as the mass ratio of activator and titanium gypsum can be 0.3:1000,0.5:1000,0.7: 1000,0.9:1000,1.1:1000,1.3:1000,1.5:1000,1.7:1000,1.9:1000 or 2:1000.
By the further adjustment and optimization to activator and titanium gypsum mass ratio, the flotation effect of titanium gypsum is improved.
Preferably, inhibitor includes at least one of vulcanized sodium, lime, dextrin and starch.
It is understood that the present invention is not particularly limited the concrete type of the inhibitor, including but not limited to sulphur Changing at least one of sodium, lime, dextrin and starch or well known to those skilled in the art and above-mentioned substance has similarity The other kinds of inhibitor of matter.
Preferably, the mass ratio of the additional amount of inhibitor and titanium gypsum be 0.3~2:1000, preferably 0.5~1.2: 1000.It is typical but non-limiting, such as the mass ratio of inhibitor and titanium gypsum can be 0.3:1000,0.5:1000,0.7: 1000,0.9:1000,1.1:1000,1.3:1000,1.5:1000,1.7:1000,1.9:1000 or 2:1000.
By the further adjustment and optimization to inhibitor and titanium gypsum mass ratio, the flotation effect of titanium gypsum is improved.
Preferably, pH regulator includes at least one of sulfuric acid, hydrochloric acid, sodium hydroxide and calcium hydroxide.
It is understood that the present invention is not particularly limited the concrete type of the pH regulator, including but not limited to At least one of sulfuric acid, hydrochloric acid, sodium hydroxide and calcium hydroxide or well known to those skilled in the art and above-mentioned substance have There is the other kinds of pH regulator of similarity.
Preferably, the pH of ore pulp is adjusted to 6~8 using pH regulator.At this ph, capturing agent can be more preferable with gypsum Ground combines, and is conducive to flotation.
It should be noted that the present invention is to above-mentioned capturing agent, foaming agent, dispersing agent, activator, inhibitor and pH regulator Source there is no special limitation, using each raw material well-known to those skilled in the art, can such as use its commercially available quotient Product can also voluntarily be prepared using preparation method well known to those skilled in the art.
As further technical solution, flotation is a flotation or multiple flotation.
In the present invention, flotation step can carry out repeatedly.First in flotation early period by the way that a small amount of flotation agent pair is added Ore pulp carries out flotation, obtains the gypsum of high-purity, then in the flotation later period, by continuing to add flotation agent for remaining a small amount of stone Cream flotation is clean, to obtain the rich iron charge of higher amount.
As further technical solution, being uniformly mixed as by churned mechanically mode in size mixing step and flotation step It is uniformly mixed.In step of sizing mixing, titanium gypsum will be sufficiently mixed uniformly with water, otherwise will affect next flotation effect;? In floatation process, ore pulp will be sufficiently mixed uniformly with flotation agent, avoid gypsum flotation insufficient.
As further technical solution, in separating step, the concentrate foam and tailing ore pulp for respectively obtaining flotation are carried out It is separated by solid-liquid separation, obtains gypsum and rich iron charge.
In the present invention, the concentrate foam containing dihydrate gypsum and the tail containing metal impurities have been obtained after flotation Mine ore pulp, the two contain a large amount of liquid, need to remove these liquid.
Preferably, be separated by solid-liquid separation includes at least one of sedimentation, filtering and centrifugation.Separation of solid and liquid generallys use physics point From.
It preferably, further include drying steps after solid-liquid separation step.After concentrate foam and tailing ore pulp are separated by solid-liquid separation Most moisture can be removed, but still has a small amount of moisture residue, will be obtained after these extra moisture dryings removals Purify gypsum and rich iron charge.
Excessive limitation is not done for dry concrete operation method and operating condition such as temperature etc., those skilled in the art can To carry out selective regulation according to the actual situation.
As further technical solution, isolated water returns to step cycle use of sizing mixing.
In the present invention, by water that concentrate foam and tailing solid-liquid separation on ore pulp obtain containing being added in floatation process Flotation agent can return to step cycle use of sizing mixing, it is possible to reduce the dosage of water and flotation agent in titanium gypsum purification process reduces titanium The cost for purification of gypsum.
It is preferably carried out in mode in one kind, as shown in Figure 1, first mixing titanium gypsum according to certain volume ratio with water Uniformly, it is tuned into ore pulp, flotation agent is then added into ore pulp, is uniformly mixed, flotation is carried out and obtains concentrate foam and tailing ore pulp, Finally concentrate foam and tailing ore pulp that flotation obtains are filtered, obtain purification gypsum and rich iron charge.
According to the second aspect of the invention, the present invention provides a kind of gypsum that the method for purification using titanium gypsum obtains. The gypsum is obtained using cheap titanium gypsum as feedstock purification, excessively cannot be rehoused and be utilized and draw to alleviate titanium gypsum The problem of playing the wasting of resources and environmental pollution.
According to the third aspect of the invention we, the application the present invention provides a kind of gypsum in construction material.The present invention mentions The gypsum of confession, the purity is high of the dihydrate gypsum contained can substitute the natural gypsum as construction material completely.
The present invention is further illustrated below by specific embodiment and comparative example, it should be understood, however, that, these implementations Example, which is only used for being described in more detail, to be used, and but should not be understood as present invention is limited in any form.
Titanium gypsum used in the embodiment of the present invention is provided by certain southwestern titanium powder plant, and main chemical compositions are as shown in table 1, with SO3Meter is secondly water gypsum content is about 75%.Its content of vanadium is higher than 2%, has higher utility value, while also iron content, titanium etc. Using ingredient.However sulfur content it is higher inhibit its return on a large scale factory utilization.
1 calcium method tailings in vanadium extraction main component of table
Embodiment 1
A kind of method of purification of titanium gypsum is present embodiments provided, as shown in Figure 1, comprising the following steps:
Above-mentioned titanium gypsum 50g is weighed first to be placed in XFD-1.5 type single-channel type flotation cell, and 1.5L water is added, stirs evenly; Then 10mL alcohol is added, air agitation 2min adds 0.1g enuatrol, continues to stir 1min, flotation to non-foam generates; Gypsum and rich iron charge finally are obtained to obtained concentrate foam and tailing slurry filtration, drying respectively.
Embodiment 2
Present embodiments provide a kind of method of purification of titanium gypsum, comprising the following steps:
Above-mentioned titanium gypsum 75g is weighed first to be placed in XFD-1.5 type single-channel type flotation cell, and 1.5L water is added, stirs evenly; Then 5mL waterglass is added, air agitation 2min adds 0.1g lauryl sodium sulfate, continues to stir 1min, flotation to nothing Foam generates;The finally centrifugation of concentrate foam and tailing ore pulp, the drying to obtaining respectively, obtains gypsum and rich iron charge.
Embodiment 3
Present embodiments provide a kind of method of purification of titanium gypsum, comprising the following steps:
Above-mentioned titanium gypsum 150g is weighed first to be placed in XFD-1.5 type single-channel type flotation cell, 1.5L water is added, and stirring is equal It is even;Then 0.2mL butyl ether oil is added, air agitation 2min adds 0.1g lauryl sodium sulfate, continues to stir 1min, float Choosing to non-foam generates;The finally centrifugation of concentrate foam and tailing ore pulp, the drying to obtaining respectively, obtains gypsum and rich iron charge.
Embodiment 4
Present embodiments provide a kind of method of purification of titanium gypsum, comprising the following steps:
Above-mentioned titanium gypsum 300g is weighed first to be placed in XFD-1.5 type single-channel type flotation cell, 1.5L water is added, and stirring is equal It is even;Then 0.2g sodium carbonate is added, air agitation 2min adds 0.1g lauryl sodium sulfate, continues to stir 1min, flotation It is generated to non-foam;Gypsum and rich iron charge finally are obtained to obtained concentrate foam and tailing settling ore pulp, drying respectively.
Embodiment 5
A kind of method of purification of titanium gypsum is present embodiments provided, as shown in Figure 1, comprising the following steps:
Above-mentioned titanium gypsum 350g is weighed first to be placed in XFD-1.5 type single-channel type flotation cell, 1.5L water is added, and stirring is equal It is even;Then hydrochloric acid and sodium hydroxide is added, the pH of solution is adjusted to 6~8, add, 5mL waterglass, 0.2mL butyl ether oil, 0.2g carbon Sour sodium and 0.2g starch, air agitation 2min add 0.1g lauryl sodium sulfate, continue to stir 1min, flotation is to still Foam generates;Gypsum and rich iron charge finally are obtained to obtained concentrate foam and tailing slurry filtration, drying respectively.
Embodiment 6
A kind of method of purification of titanium gypsum is present embodiments provided, as shown in Figure 1, comprising the following steps:
Above-mentioned titanium gypsum 100g is weighed first to be placed in XFD-1.5 type single-channel type flotation cell, 1.5L water is added, and stirring is equal It is even;Then 5mL waterglass is added, air agitation 2min adds 0.1g neopelex, continues to stir 1min, float Choosing to non-foam generates;Gypsum and rich iron charge finally are obtained to obtained concentrate foam and tailing slurry filtration, drying respectively.
Embodiment 7
Present embodiments provide a kind of method of purification of titanium gypsum, comprising the following steps:
Above-mentioned titanium gypsum 100g is weighed first to be placed in XFD-1.5 type single-channel type flotation cell, and 1.5L water, air agitation is added Then 0.1g neopelex is added in 2min, continue to stir 1min, flotation to non-foam generates;Finally respectively to The centrifugation of concentrate foam and tailing ore pulp, the drying arrived, obtain gypsum and rich iron charge.
Embodiment 8
Present embodiments provide a kind of method of purification of titanium gypsum, comprising the following steps:
Above-mentioned titanium gypsum 200g is weighed first to be placed in XFD-1.5 type single-channel type flotation cell, 1.5L water is added, and stirring is equal It is even, 0.05g neopelex is then added, continues to stir 1min, flotation to non-foam generates, respectively to obtained essence Mine foam and tailing slurry filtration, drying obtain a flotation gypsum, then 0.05g detergent alkylate sulphur is added into flotation cell Sour sodium, flotation to bubble-free generate, and filter respectively, are dried to obtain secondary flotation gypsum and rich iron tailings.
Comparative example 1
This comparative example provides a kind of method of purification of titanium gypsum, comprising the following steps:
Above-mentioned titanium gypsum 400g is weighed first to be placed in XFD-1.5 type single-channel type flotation cell, 1.5L water is added, and stirring is equal It is even;Then 5mL waterglass is added, air agitation 2min adds 0.1g lauryl sodium sulfate, continues to stir 1min, flotation It is generated to non-foam;Gypsum and rich iron charge finally are obtained to obtained concentrate foam and tailing slurry filtration, drying respectively.
Comparative example 2
This comparative example provides a kind of method of purification of titanium gypsum, comprising the following steps:
Above-mentioned titanium gypsum 100g is weighed first to be placed in XFD-1.5 type single-channel type flotation cell, 1.5L water is added, and stirring is equal It is even;Then 5mL waterglass is added, air agitation 2min adds 0.01g lauryl sodium sulfate, continues to stir 1min, flotation It is generated to non-foam;Gypsum and rich iron charge finally are obtained to obtained concentrate foam and tailing slurry filtration, drying respectively.
Iron in the purity of embodiment 1-8 and comparative example the 1-2 gypsum purified, yield and rich iron charge is contained respectively Amount, yield are detected, and the results are shown in Table 2.
The content of iron, yield in the purity of 2 gypsum of table, yield and rich iron charge
Embodiment Gypsum purity Gypsum yield Iron charge iron content Iron yield
Embodiment 1 95.3% 83.1% 21.4% 84.6%
Embodiment 2 91.2% 86.3% 20.9% 85.7%
Embodiment 3 85.6% 92.8% 19.4% 83.8%
Embodiment 4 82.5% 94.7% 18.7% 82.4%
Embodiment 5 81.6% 95.1% 18.1% 81.3%
Embodiment 6 88.3% 89.7% 20.4% 86.9%
Embodiment 7 85.1% 92.5% 28.2% 70.1%
Embodiment 8 is primary 93.1% - - -
Embodiment 8 two times 86.5% 93.1%* 27.6% 75.2%
Comparative example 1 80.9% 95.8% 17.5% 80.5%
Comparative example 2 93.6% 32.8% 8.9% 92.5%
*: indicating the accumulative yield of flotation twice
Embodiment 2 and the difference of comparative example 1 be, the titanium gypsum of comparative example 1 and the ratio of water are greater than the titanium stone of embodiment 2 The ratio of cream and water.From table 2 it can be seen that the purity that embodiment 2 purifies obtained gypsum is substantially better than the gypsum of comparative example 1 Purity.When titanium gypsum is mixed with water, the additive amount of water cannot be too small, should control in a certain range.
Embodiment 6 is identical as the additional amount of 7 capturing agent of embodiment, but dispersing agent waterglass is not added in embodiment 7.From Table 2 is as can be seen that the purity that embodiment 6 purifies obtained gypsum is substantially better than the purity of the gypsum of embodiment 7.Illustrate dispersing agent Addition be more conducive to the purification of titanium gypsum.
Embodiment 6 and the difference of comparative example 2 are that the additional amount of capturing agent is significantly less than catching for embodiment 6 in comparative example 2 Obtain the additional amount of agent.From table 2 it can be seen that embodiment 6 purifies the gypsum receipts that obtained gypsum yield is substantially better than comparative example 2 Rate.The additional amount of capturing agent cannot be too small, should control in a certain range.
Titanium gypsum in embodiment 8 have passed through purification by floatation twice, from table 2 it can be seen that mentioning after second of flotation The purity of pure obtained gypsum is significantly improved.
Finally, it should be noted that the above embodiments are only used to illustrate the technical solution of the present invention., rather than its limitations;To the greatest extent Pipe present invention has been described in detail with reference to the aforementioned embodiments, those skilled in the art should understand that: its according to So be possible to modify the technical solutions described in the foregoing embodiments, or to some or all of the technical features into Row equivalent replacement;And these are modified or replaceed, various embodiments of the present invention technology that it does not separate the essence of the corresponding technical solution The range of scheme.

Claims (10)

1. a kind of method of purification of titanium gypsum, which is characterized in that including sizing mixing, flotation and separation;
Wherein, in the flotation step, used flotation agent includes capturing agent, optional foaming agent, optional dispersing agent, appoints The activator of choosing, optional inhibitor and optional pH regulator.
2. the method for purification of titanium gypsum according to claim 1, which is characterized in that, will be to be processed in the step of sizing mixing Titanium gypsum and water according to mass ratio be that 1:3~20 are uniformly mixed;
Preferably, in the step of sizing mixing, titanium gypsum to be processed is uniformly mixed with water according to mass ratio for 1:5~10;
Preferably, the water further includes the water that separating step obtains.
3. the method for purification of titanium gypsum according to claim 1, which is characterized in that in the flotation step, to sizing mixing To ore pulp in add flotation agent, be uniformly mixed, carry out flotation obtain concentrate foam and tailing ore pulp.
4. the method for purification of titanium gypsum according to claim 1-3, which is characterized in that the capturing agent includes ten At least one of dialkyl benzene sulfonic acids sodium, lauryl sodium sulfate, enuatrol and sodium salicylate;
Preferably, the mass ratio of the additional amount of the capturing agent and titanium gypsum be 0.3~2:1000, preferably 0.5~1.2: 1000;
Preferably, the foaming agent includes at least one of terpinol, camphorated oil, pinke needle oil and butyl ether oil;
Preferably, the mass ratio of the additional amount of the foaming agent and titanium gypsum be 0.3~2:1000, preferably 0.5~1.2: 1000;
Preferably, the dispersing agent include in ethyl alcohol, waterglass, calcium stearate, calgon, cellulose and glycerol at least It is a kind of;
Preferably, the mass ratio of the additional amount of the dispersing agent and ore pulp is 1~10:1000;
Preferably, the activator includes at least one of sulfuric acid, sulfurous acid, oxalic acid and sodium carbonate;
Preferably, the mass ratio of the additional amount of the activator and titanium gypsum be 0.3~2:1000, preferably 0.5~1.2: 1000;
Preferably, the inhibitor includes at least one of vulcanized sodium, lime, dextrin and starch;
Preferably, the mass ratio of the additional amount of the inhibitor and titanium gypsum be 0.3~2:1000, preferably 0.5~1.2: 1000;
Preferably, the pH regulator includes at least one of sulfuric acid, hydrochloric acid, sodium hydroxide and calcium hydroxide;
Preferably, the pH of ore pulp is adjusted to 6~8 using pH regulator.
5. the method for purification of titanium gypsum according to claim 1, which is characterized in that the flotation is a flotation or more Secondary flotation.
6. the method for purification of titanium gypsum according to claim 2 or 3, which is characterized in that described to be uniformly mixed to pass through machine The mode of tool stirring is uniformly mixed.
7. the method for purification of titanium gypsum according to claim 1, which is characterized in that in the separating step, will float respectively It selects obtained concentrate foam and tailing ore pulp to be separated by solid-liquid separation, obtains gypsum and rich iron charge;
Preferably, described be separated by solid-liquid separation includes at least one of sedimentation, filtering and centrifugation;
It preferably, further include drying steps after the solid-liquid separation step.
8. the method for purification of titanium gypsum according to claim 1, which is characterized in that the isolated water return is sized mixing Step cycle uses.
9. the gypsum obtained using the method for purification of the described in any item titanium gypsums of claim 1-8.
10. gypsum or gypsum as claimed in claim 9 that the method for purification of the described in any item titanium gypsums of claim 1-8 obtains Application in construction material.
CN201811166947.4A 2018-09-30 2018-09-30 The application of the method for purification, gypsum and gypsum of titanium gypsum Pending CN109292809A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201811166947.4A CN109292809A (en) 2018-09-30 2018-09-30 The application of the method for purification, gypsum and gypsum of titanium gypsum

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201811166947.4A CN109292809A (en) 2018-09-30 2018-09-30 The application of the method for purification, gypsum and gypsum of titanium gypsum

Publications (1)

Publication Number Publication Date
CN109292809A true CN109292809A (en) 2019-02-01

Family

ID=65161686

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201811166947.4A Pending CN109292809A (en) 2018-09-30 2018-09-30 The application of the method for purification, gypsum and gypsum of titanium gypsum

Country Status (1)

Country Link
CN (1) CN109292809A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110028258A (en) * 2019-05-16 2019-07-19 西南科技大学 A kind of method that iron Sulphur ressource is utilized respectively in titanium gypsum
CN111014230A (en) * 2019-11-15 2020-04-17 鞍钢集团矿业有限公司 Low-temperature oxidation method of dry-method and semi-dry-method desulfurized ash
CN112266007A (en) * 2020-11-04 2021-01-26 湖南振亚新材料科技有限公司 Preparation method of high-purity high-whiteness calcium sulfate
CN112279288A (en) * 2020-11-04 2021-01-29 湖南振亚新材料科技有限公司 Continuous preparation method of modified calcium sulfate
CN115180646A (en) * 2022-08-22 2022-10-14 清华大学 Method for purifying calcium sulfate dihydrate from by-product gypsum

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104261453A (en) * 2008-07-31 2015-01-07 吉野石膏株式会社 Process For Continuous Modification Of Dihydrate Gypsum And Modified Dihydrate Gypsum Obtained By The Process
CN106179771A (en) * 2016-07-18 2016-12-07 攀钢集团攀枝花钢铁研究院有限公司 The recoverying and utilizing method of calcium method tailings in vanadium extraction
CN106629806A (en) * 2016-11-18 2017-05-10 江苏仁欣环保科技有限公司 Method for producing dihydrate gypsum from waste liquid in laterite nickel ore wet process

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104261453A (en) * 2008-07-31 2015-01-07 吉野石膏株式会社 Process For Continuous Modification Of Dihydrate Gypsum And Modified Dihydrate Gypsum Obtained By The Process
CN106179771A (en) * 2016-07-18 2016-12-07 攀钢集团攀枝花钢铁研究院有限公司 The recoverying and utilizing method of calcium method tailings in vanadium extraction
CN106629806A (en) * 2016-11-18 2017-05-10 江苏仁欣环保科技有限公司 Method for producing dihydrate gypsum from waste liquid in laterite nickel ore wet process

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110028258A (en) * 2019-05-16 2019-07-19 西南科技大学 A kind of method that iron Sulphur ressource is utilized respectively in titanium gypsum
CN111014230A (en) * 2019-11-15 2020-04-17 鞍钢集团矿业有限公司 Low-temperature oxidation method of dry-method and semi-dry-method desulfurized ash
CN112266007A (en) * 2020-11-04 2021-01-26 湖南振亚新材料科技有限公司 Preparation method of high-purity high-whiteness calcium sulfate
CN112279288A (en) * 2020-11-04 2021-01-29 湖南振亚新材料科技有限公司 Continuous preparation method of modified calcium sulfate
CN115180646A (en) * 2022-08-22 2022-10-14 清华大学 Method for purifying calcium sulfate dihydrate from by-product gypsum

Similar Documents

Publication Publication Date Title
CN109292809A (en) The application of the method for purification, gypsum and gypsum of titanium gypsum
CN1322934C (en) Collophanite direct flotation and reverse flotation technique
CN105689149B (en) A kind of bi-anti-symmetric matrix method of suitable silicon calcium quality ore
CN102744152A (en) Reverse/direct flotation technology of collophanite
CN101679077A (en) Surface-reacted calcium carbonate in combination with hydrophobic adsorbent for water treatment
CN104801427B (en) A kind of high magnesium low-grade phosphorus ore coarse grain direct reverse flotation technique
CN114887757B (en) Mineral separation method of lepidolite
CN102671771B (en) Method for floating and separating zinc silicate and kutnahorite
CN109569891A (en) One kind is for compound flotation collector of magnesite Counterfloatating desiliconization and preparation method thereof
CN101722110A (en) Collector for scheelite concentration and use thereof
CN107899753A (en) A kind of anion combined capturing and collecting agent of free-floride FLOTATION SEPARATION quartz and feldspar and preparation method and application
CN105307774B (en) Method for separating calcium carbonate and gypsum
CN106076607B (en) A kind of two step desliming reverse floatation process handling high alumina-silica collophane
CN101531384A (en) Technique for preparing electronic grade magnesium hydrate and ammonium sulphate by cycle serum featuring in flue gas desulfurization by method of magnesium oxidization
CN109999990B (en) Production process of acid-grade fluorite fine powder
CN111701728A (en) Selective flotation separation method for fluorite and calcium-containing gangue
CN106944246A (en) The method of copper-cobalt ore flotation agent and copper-cobalt ore
CN105597943B (en) A kind of depressing agent and preparation method and applications
CN212596353U (en) System for purifying phosphogypsum based on flotation column and gravity separation column with filler
CN209989272U (en) System for preparing magnesium oxide from low-grade magnesite
CN106732324B (en) It is a kind of for the filter aid of fine filtration of sodium aluminate solution and its production and application method
CN104922943A (en) Collophanite direct flotation fine-grade tailing settlement concentration method
CN112371346B (en) Dolomite inhibitor and application method thereof
CN103706488A (en) Reverse flotation technology of phosphate ore in alkaline medium
CN109351481B (en) Phosphorite calcining-digesting-reverse flotation separation process

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication

Application publication date: 20190201

RJ01 Rejection of invention patent application after publication