CN105460973B - The method that white carbon/composite titania material is prepared using potassium feldspar - Google Patents

The method that white carbon/composite titania material is prepared using potassium feldspar Download PDF

Info

Publication number
CN105460973B
CN105460973B CN201510851578.2A CN201510851578A CN105460973B CN 105460973 B CN105460973 B CN 105460973B CN 201510851578 A CN201510851578 A CN 201510851578A CN 105460973 B CN105460973 B CN 105460973B
Authority
CN
China
Prior art keywords
white carbon
ammonium
potassium feldspar
gas
temperature
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.)
Expired - Fee Related
Application number
CN201510851578.2A
Other languages
Chinese (zh)
Other versions
CN105460973A (en
Inventor
肖建军
许道立
刘改正
张国峰
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.)
LUOYANG LVREN ENVIRONMENTAL PROTECTION EQUIPMENT Co Ltd
Original Assignee
LUOYANG LVREN ENVIRONMENTAL PROTECTION EQUIPMENT 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 LUOYANG LVREN ENVIRONMENTAL PROTECTION EQUIPMENT Co Ltd filed Critical LUOYANG LVREN ENVIRONMENTAL PROTECTION EQUIPMENT Co Ltd
Priority to CN201510851578.2A priority Critical patent/CN105460973B/en
Publication of CN105460973A publication Critical patent/CN105460973A/en
Application granted granted Critical
Publication of CN105460973B publication Critical patent/CN105460973B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G23/00Compounds of titanium
    • C01G23/04Oxides; Hydroxides
    • C01G23/047Titanium dioxide
    • C01G23/053Producing by wet processes, e.g. hydrolysing titanium salts
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B33/00Silicon; Compounds thereof
    • C01B33/113Silicon oxides; Hydrates thereof
    • C01B33/12Silica; Hydrates thereof, e.g. lepidoic silicic acid
    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05CNITROGENOUS FERTILISERS
    • C05C3/00Fertilisers containing other salts of ammonia or ammonia itself, e.g. gas liquor

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geology (AREA)
  • Fertilizers (AREA)
  • Inorganic Compounds Of Heavy Metals (AREA)

Abstract

The method that potassium feldspar prepares white carbon/composite titania material is the present invention relates to the use of, is that raw material prepares SiF using potassium feldspar, ammonium fluoride, the concentrated sulfuric acid4Gas, recycles ammoniacal liquor to the SiF4Gas is absorbed, while to adding titanium tetrachloride in the ammoniacal liquor so that titanium tetrachloride and SiF4Gas can synchronously be hydrolyzed, and the product after hydrolysis is aged, filtering, washing, carry out high-temperature calcination so as to white carbon/composite titania material is obtained after drying.While potassium feldspar resource is made full use of, the white carbon/composite titania material of acquisition is respectively provided with excellent photocatalysis performance, and preparation process is simple to the present invention under ultraviolet light and visible ray, and raw material availability is high.

Description

The method that white carbon/composite titania material is prepared using potassium feldspar
Technical field
The present invention relates to a kind of preparation method of composite titania material, specifically, relate to using potassium feldspar system The method of standby white carbon/composite titania material.
Background technology
Titanium dioxide because its have stability it is high, with photo-catalysis function, it is cheap the features such as, be widely used in photocatalysis row Industry, but actually preparing photocatalysis TiO2When, because of its extremely easy reunion, it is difficult to reclaim and also exist TiO2Photochemical catalyst is certainly The not high defect of right light utilization efficiency, constrains TiO2The catalytic efficiency of photochemical catalyst.Current result of the above problems is usual It is by the TiO2Photocatalyst on suitable carrier material, to improve the photocatalysis rate of titanium dioxide, preparation technology Cumbersome, raw material availability is low.
Precipitated silica is a kind of amorphous silica powder body material with waterglass as main material production, with than The features such as surface area is big, porosity is high, aperture is small, chemical stability is good is a kind of with performance advantage and cost advantage TiO2Carrier material;On the other hand, the potash feldspar ore reserves of China extremely enrich, potassium feldspar contain abundant potassium, aluminium, silicon etc. into Point, therefore, it can by preparing white carbon to potassium feldspar comprehensive exploitation, and silicon tetrachloride etc. is synchronously added in preparation process Raw material is directly obtained white carbon/composite titania material by reaction.
The content of the invention
The technical solution adopted in the present invention is:The method that white carbon/composite titania material is prepared using potassium feldspar, Specifically include following steps:
Step one, potassium feldspar, ammonium fluoride, the concentrated sulfuric acid be added in reactor successively, it is at 200 DEG C~300 DEG C and spontaneous Reacted under pressure, generated gas and solid residue, its reaction principle is:
NH4F =HF↑ + NH3↑,
2K[AlSi3O8] + 24HF + 4H2SO4 = K2SO4 + Al2(SO4)3 + 6SiF4+ 16H2O,
Wherein, potassium feldspar, ammonium fluoride, the mass ratio of the concentrated sulfuric acid are 1:3~3.5:3.5~4;The concentrated sulfuric acid is by mass fraction 98% concentrated sulfuric acid is calculated;
Step 2, in the case where temperature is 5 DEG C~10 DEG C and condition of negative pressure, be passed through in the ammoniacal liquor for mass fraction being 20%~30% The gas, while to adding titanium tetrachloride in the ammoniacal liquor, and the gas and the titanium tetrachloride are made by magnetic agitation There is hydrolysis generation turbid solution simultaneously, the turbid solution is aged, filtering, washing, obtain compound after drying, its reaction Principle is mainly:
TiCl4+ 2H2O=TiO2↓+4HCl,
3SiF4 + 2H2O = 2H2SiF6 + SiO2↓,
H2SiF6 +6NH4OH = 6NH4F + SiO2↓ + 4H2O,
NH4OH + HCl = NH4Cl + H2O ;
Step 3, by the compound temperature be 500 DEG C~1100 DEG C at carry out the h of high-temperature calcination 6~8, be cooled to room White carbon/composite titania material is obtained after temperature.
Based on above-mentioned, the step one be additionally included in temperature for used under the conditions of 90 DEG C~110 DEG C mass fraction for 8%~ 10% sulfuric acid solution leaches the solid residue, and leaching liquid is obtained, to addition ammoniacal liquor regulation pH=8~10 in the leaching liquid, By obtaining ammonium-potassium sulfate filtrate and aluminum hydroxide precipitation after filtering, then by the ammonium-potassium sulfate filtrate by being concentrated in vacuo to Saturation, separates out ammonium-potassium sulfate crystal;Finally by slurry-spraying pelletizing, it is drying to obtain binary compound fertilizer ammonium-potassium sulfate.
Based on above-mentioned, the turbid solution in the step 2 is aged, obtain after filtering and contain ammonium fluoride, the filter of ammonium chloride Liquid, the filtrate obtains ammonium fluoride and can be heated as the ammonium chloride crystals particle of nitrogenous fertilizer, the ammonium fluoride through evaporative crystallization Decomposing generation hydrogen fluoride and ammonia can recycle.
Based on above-mentioned, the step 3 also includes:The compound is passed through in spraying reaction tower in atomization temperature first To carry out 10~35s of atomization under the conditions of 70 DEG C~95 DEG C, atomizing particle size is 5~100 microns, atomized after recovered drying Grain, then carries out the h of high-temperature calcination 6~8 again by the atomizing particle under the conditions of temperature is for 500 DEG C~1100 DEG C, is cooled to room White carbon/composite titania material is obtained after temperature.
The present invention has prominent substantive distinguishing features progressive with significant compared with the prior art, specifically,
Ammonium fluoride, potassium feldspar decomposition are produced SiF by the present invention first4Gas, recycles ammoniacal liquor to the SiF4Gas is carried out Hydrolysis is absorbed, titanium tetrachloride is added in hydrolytic process, the product after hydrolysis is aged, filtering, washing, carry out high temperature after drying and forge Burn so as to white carbon/composite titania material is obtained.
Preparation process process is simple of the present invention, reaction condition enter water-filling gently, to equipment than relatively low to titanium tetrachloride In solution preocess, SiF is contained because being passed through4Gas, not only play a part of reactant, the effect of stirring is also acted, with same When in the presence of magnetic agitation so that the composite of preparation is more uniform, it is to avoid the agglomeration of titanium dioxide, improves Its photocatalysis efficiency.Further, in the preparation process intermediate product can be carried by recycling generation byproduct The utilization rate of potassium feldspar high.
Specific embodiment
Below by specific embodiment, technical scheme is described in further detail.
Embodiment 1
The present embodiment provides a kind of method that utilization potassium feldspar prepares white carbon/composite titania material, specific steps Including:
Step one, potassium feldspar, ammonium fluoride, the concentrated sulfuric acid be added in converter reactor successively, in 200 DEG C and self-generated pressure Under reacted, generate gas and solid residue, its reaction principle is:
NH4F =2HF↑ + NH3↑,
2K[AlSi3O8] + 24HF + 4H2SO4 = K2SO4 + Al2(SO4)3 + 6SiF4+ 16H2O,
Wherein, potassium feldspar, ammonium fluoride, the mass ratio of the concentrated sulfuric acid are 1:3.5:4;The concentrated sulfuric acid for mass fraction be 98% it is dense Sulfuric acid;
Step 2, in the case where temperature is 10 DEG C and condition of negative pressure, in absorption column of gas to mass fraction be 25% ammoniacal liquor in The gas of step one generation is passed through, while to adding titanium tetrachloride in the ammoniacal liquor, and the gas is made by magnetic agitation There is hydrolysis generation turbid solution simultaneously in body and the titanium tetrachloride, the turbid solution is aged, filtering, washing, after drying Compound is obtained, its reaction principle is mainly:
TiCl4+ 2H2O=TiO2↓+4HCl,
3SiF4 + 2H2O = 2H2SiF6 + SiO2↓,
H2SiF6 +6NH4OH = 6NH4F + SiO2↓ + 4H2O,
NH4OH + HCl = NH4Cl + H2O ;
Step 3, the compound is positioned in calcining furnace be 1100 DEG C in temperature at carry out the h of high-temperature calcination 6, cool down White carbon/composite titania material is obtained after to room temperature.
Embodiment 2
The present embodiment provides a kind of method that utilization potassium feldspar prepares white carbon/composite titania material, specific steps Roughly the same with embodiment 1, difference is:
Step one, potassium feldspar, ammonium fluoride, the concentrated sulfuric acid be added in converter reactor successively, in 250 DEG C and self-generated pressure Under reacted, generate gas and solid residue, its reaction principle is:
NH4F =2HF↑ + NH3↑,
2K[AlSi3O8] + 24HF + 4H2SO4 = K2SO4 + Al2(SO4)3 + 6SiF4+ 16H2O,
Wherein, potassium feldspar, ammonium fluoride, the mass ratio of the concentrated sulfuric acid are 1:3.5:4;The concentrated sulfuric acid for mass fraction be 98% it is dense Sulfuric acid.At the solid residue is 110 DEG C in temperature, after being leached through the sulfuric acid solution that mass fraction is 10%, in leaching liquid It is 10 to add ammoniacal liquor to adjust the pH of the leaching liquid, ammonium-potassium sulfate filtrate and aluminum hydroxide precipitation is obtained after filtering, then by institute Ammonium-potassium sulfate filtrate is stated by being concentrated in vacuo to saturation, ammonium-potassium sulfate crystal is separated out;And by slurry-spraying pelletizing, be drying to obtain two Component composite fertilizer ammonium-potassium sulfate;
Step 2, in the case where temperature is 5 DEG C and condition of negative pressure, in absorption column of gas to mass fraction be 20% ammoniacal liquor in The gas of step one generation is passed through, while to adding titanium tetrachloride in the ammoniacal liquor, and the gas is made by magnetic agitation There is hydrolysis generation turbid solution simultaneously in body and the titanium tetrachloride, the turbid solution is aged, filtering, washing, after drying Obtain compound.Turbid solution filtrate after filtering is obtained ammonium fluoride and can be as the ammonium chloride of nitrogenous fertilizer through evaporative crystallization Crystalline particle, the ammonium fluoride is thermally decomposed to generate hydrogen fluoride and ammonia and can be recycled.
Embodiment 3
The present embodiment provides a kind of method that utilization potassium feldspar prepares white carbon/composite titania material, specific steps Roughly the same with embodiment 1, difference is:
Step 3, the compound is passed through in spraying reaction tower and carries out atomization 35s, it is 95 DEG C, mist to control atomization temperature It is 5~100 microns to change particle diameter, and then be positioned over the atomizing particle in calcining furnace by atomized particle after recovered drying High-temperature calcination 6h is carried out at being 1000 DEG C in temperature, is obtained with white carbon/composite titania material.
Finally it should be noted that:The above embodiments are merely illustrative of the technical solutions of the present invention rather than its limitations;To the greatest extent Pipe has been described in detail with reference to preferred embodiment to the present invention, and those of ordinary skill in the art should be understood:Still Specific embodiment of the invention can be modified or equivalent is carried out to some technical characteristics;Without deviating from this hair The spirit of bright technical scheme, it all should cover in the middle of claimed technical scheme scope of the invention.

Claims (3)

1. the method that white carbon/composite titania material is prepared using potassium feldspar, specifically includes following steps:
Step one, potassium feldspar, ammonium fluoride, the concentrated sulfuric acid be added in reactor successively, in 200 DEG C~300 DEG C and self-generated pressure Under reacted, generate gas and solid residue, wherein, potassium feldspar, ammonium fluoride, the concentrated sulfuric acid mass ratio be 1:3~3.5:3.5 ~4;
Step 2, in the case where temperature is 5 DEG C~10 DEG C and condition of negative pressure, be passed through in the ammoniacal liquor for mass fraction being 20%~30% described The gas of step one generation, while to adding titanium tetrachloride in the ammoniacal liquor, and by magnetic agitation make the gas and There is hydrolysis generation turbid solution in the titanium tetrachloride, the turbid solution is aged, filtering, washing, obtain after drying simultaneously Compound;
Step 3, first by the compound be passed through in spraying reaction tower be 70 DEG C~95 DEG C in atomization temperature under the conditions of carry out mist Change 10~35s, atomizing particle size is 5~100 microns, and then atomized particle after recovered drying exists the atomizing particle Temperature is obtained white carbon/titanium dioxide to carry out the h of high-temperature calcination 6~8 again under the conditions of 500 DEG C~1100 DEG C after being cooled to room temperature Composite.
2. the method that utilization potassium feldspar according to claim 1 prepares white carbon/composite titania material, its feature exists In it also includes:Mass fraction is used to leach institute for 8%~10% sulfuric acid solution under the conditions of being 90 DEG C~110 DEG C in temperature Solid residue is stated, leaching liquid is obtained, to ammoniacal liquor regulation pH=8~10 are added in the leaching liquid, by obtaining ammonium sulfate after filtering Potassium filtrate and aluminum hydroxide precipitation, then make ammonium-potassium sulfate crystal by the ammonium-potassium sulfate filtrate by being concentrated in vacuo to saturation Separate out;Finally by slurry-spraying pelletizing, it is drying to obtain binary compound fertilizer ammonium-potassium sulfate.
3. the method that utilization potassium feldspar according to claim 1 prepares white carbon/composite titania material, its feature exists In the turbid solution in the step 2 is aged, obtain after filtering and contain ammonium fluoride, the filtrate of ammonium chloride, the filtrate warp Evaporative crystallization obtains ammonium fluoride and the ammonium chloride crystals particle as nitrogenous fertilizer, and the ammonium fluoride is thermally decomposed to generate hydrogen fluoride and ammonia Gas so that the ammonium fluoride is recycled.
CN201510851578.2A 2015-11-30 2015-11-30 The method that white carbon/composite titania material is prepared using potassium feldspar Expired - Fee Related CN105460973B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510851578.2A CN105460973B (en) 2015-11-30 2015-11-30 The method that white carbon/composite titania material is prepared using potassium feldspar

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510851578.2A CN105460973B (en) 2015-11-30 2015-11-30 The method that white carbon/composite titania material is prepared using potassium feldspar

Publications (2)

Publication Number Publication Date
CN105460973A CN105460973A (en) 2016-04-06
CN105460973B true CN105460973B (en) 2017-06-09

Family

ID=55599200

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510851578.2A Expired - Fee Related CN105460973B (en) 2015-11-30 2015-11-30 The method that white carbon/composite titania material is prepared using potassium feldspar

Country Status (1)

Country Link
CN (1) CN105460973B (en)

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102039117B (en) * 2009-10-15 2012-08-08 中国矿业大学(北京) Method for preparing loaded nano TiO2 composite material by using precipitated white carbon black as carrier
CN103172074B (en) * 2013-01-17 2014-11-26 洛阳氟钾科技有限公司 Process for decomposing potassium feldspar by adopting low-temperature semidry method for comprehensive utilization
CN103539130A (en) * 2013-10-31 2014-01-29 洛阳氟钾科技有限公司 Technological method for preparing white carbon black from potassium feldspar

Also Published As

Publication number Publication date
CN105460973A (en) 2016-04-06

Similar Documents

Publication Publication Date Title
CN102828037B (en) Method of preparing low-silicon low-phosphorus potassium metavanadate solution from vanadium slag
CN105110344B (en) Method and apparatus for preparing fumed silica from coal gangue
CN104925817B (en) The preparation method of nanometer grade silica
CN101941704A (en) New method for preparing silicon dioxide by utilizing rice hull ash
CN105645358A (en) Method for preparing hydrogen fluoride from fluosilicic acid
CN101417815B (en) Method for preparing titanium white by spray hydrolysis
CN108163812B (en) Preparation method of hydrogen fluoride and preparation method of hydrofluoric acid
CN103539130A (en) Technological method for preparing white carbon black from potassium feldspar
CN103121699B (en) A kind of method that potassium fluosilicate prepares potassium fluoride
CN110040763A (en) It is a kind of using high chlorine secondary zinc oxide as the technique of raw material coproduction low sulfuric chlorohydrin zinc and common salt
CN103613127B (en) The recoverying and utilizing method of low boilers in titanium tetrachloride production
CN102701260B (en) Spray pyrolysis method for aid-containing rare earth chloride solution
CN105460973B (en) The method that white carbon/composite titania material is prepared using potassium feldspar
CN108455647A (en) A kind of method of phosphoric acid by-product ardealite and fluosilicic acid production calcirm-fluoride by-product white carbon and ammonium sulfate
CN105174281A (en) Method for synthesizing microporous molecular sieve by-product fluoride by means of fluosilicic acid
CN112897466A (en) Method for producing anhydrous hydrogen fluoride by using fluosilicic acid in phosphoric acid
CN104843777B (en) Method for preparing rutile titanium dioxide from titanium slag
CN105752994A (en) Method for preparing white carbon black from graphite tailings
CN101077786B (en) Method for preparing aluminum fluoride
CN106006557A (en) Method for producing hydrogen chloride from chlorosilane raffinate
CN104003429B (en) A kind of method utilizing Bayer-process seed-separating mother liquor to prepare boehmite
CN1156398C (en) Methodf or preparing anhydrous magnesium chloride
CN111017937A (en) Method for preparing potassium fluoride and co-producing ultrafine white carbon black
CN107827135A (en) A kind of preparation method of high-purity superfine alumina powder
CN111847384B (en) Preparation method of anhydrous hydrogen fluoride

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20170609

Termination date: 20171130

CF01 Termination of patent right due to non-payment of annual fee