CN105948110B - Method for improving sulfate process titanium dioxide cleanliness - Google Patents

Method for improving sulfate process titanium dioxide cleanliness Download PDF

Info

Publication number
CN105948110B
CN105948110B CN201610557303.2A CN201610557303A CN105948110B CN 105948110 B CN105948110 B CN 105948110B CN 201610557303 A CN201610557303 A CN 201610557303A CN 105948110 B CN105948110 B CN 105948110B
Authority
CN
China
Prior art keywords
titanium dioxide
finished product
cleanliness
cleannes
eye mesh
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.)
Active
Application number
CN201610557303.2A
Other languages
Chinese (zh)
Other versions
CN105948110A (en
Inventor
王海波
王斌
罗志强
杜剑桥
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 CN201610557303.2A priority Critical patent/CN105948110B/en
Publication of CN105948110A publication Critical patent/CN105948110A/en
Application granted granted Critical
Publication of CN105948110B publication Critical patent/CN105948110B/en
Active 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
    • C01G23/08Drying; Calcining ; After treatment of titanium oxide

Abstract

The invention belongs to a production process of sulfate process titanium dioxide, and particularly relates to a method for improving sulfate process titanium dioxide cleanliness. The method includes the following steps of screening a material obtained after roasting ends through a 150-200-mesh screen, making the on-screen material directly enter a plain flour process to be post-processed to obtain a titanium dioxide finished product, conducting strengthened smashing process, 325-mesh screen passing and under-screen material post-processing on the under-screen material to obtain the titanium dioxide finished product. A better separation method is put forward for TiO2 fine hard particles which influence the sulfate process titanium dioxide cleanliness, and the cleanliness of the titanium dioxide finished product can be improved through subsequent grinding and smashing.

Description

A kind of method for improving sulfuric acid method titanium pigment cleannes
Technical field
The invention belongs to sulfuric acid method titanium pigment production technology, and in particular to a kind of side of raising sulfuric acid method titanium pigment cleannes Method.
Background technology
Cleannes-and according to dispersed method configuration slurry is surveyed, a small amount of slurry for mixing then is taken with toolsetting, it is placed on and scrapes The deeper one end of plate fineness gauge groove, with the quick scraping blade of scraper plate after, the rapid dispersiveness that reads is the granule number between 0~6.5, each Sample is read twice, and grain number is the arithmetic mean of instantaneous value of two times result, and reading is smaller, and cleannes are better.
In sulfuric acid method titanium pigment production industry, metatitanic acid obtains titanium white first product by rotary kiln calcining, is limited to domestic water Solution technical merit, the broad particle distribution of metatitanic acid, at the same time at present country's rotary kiln calcination process controlled level it is limited and Not good etc. enough reason of crystal formation conversion agent dispersing uniformity, by inevitably producing some tiny compared with hard aggregation in calcination process Particle, these titanium white first product particles can not effectively be broken and disperse in normal in powder operation, into operation below, finally Reduce the cleannes of product.
Wang Bin et al. researchs show:Coarse grained presence is the main cause for influenceing cleannes, and by Experimental comparison point Analysis is obtained, and the coarse granule in domestic titanium dioxide is mainly made up of Ca, Al, Si etc., and maximum particle diameter is up to 210 μm, and external quality Preferable titanium dioxide coarse granule main component is TiO2, 30 μm are less than particle diameter more.Wang Bin et al. has found can be by inorganic surfaces Slurry after treatment intercepts screening (500 mesh sieve), can be effectively improved the cleannes of product, and then improve dividing for final titanium white product Dissipate property.
But the above method mainly improves the coarse granule being made up of Ca, Al, Si etc. causes the cleannes of titanium white product poor The reason for.If thick and stiff particle main component is TiO2, the particle is mainly shown as 2 μm or so in finished product, if by inorganic table Slurry after the treatment of face is intercepted and carries out 500 mesh sieves point, because the screen size of 500 mesh sieves is 25 μm, can not screen out 2 μm of left sides Right coarse granule.
The content of the invention
Inevitably produce some tiny compared with grit, some of them particle during existing method for producing gtitanium dioxide with sulphuric acid Main component is TiO2, at 2 μm or so, these particles can not effectively be broken and disperse particle diameter in middle powder operation, if by Slurry after inorganic surface treatment is intercepted and sieved, and sieve aperture is larger can not to be obtained granularity and meet desired titanium dioxide, sieve aperture compared with Small slurry cannot be sieved again, so as to influence the cleannes of final titanium dioxide.For the coarse granule of this influence titanium dioxide cleannes Predominantly TiO2Situation, the invention provides it is a kind of improve sulfuric acid method titanium pigment cleannes method.
The method is comprised the following steps:The material being calcined after terminating is sieved with 150~200 eye mesh screens, oversize is direct Powder operation, post processing obtain finished product titanium dioxide in.
Further, in the above method, screenings is ground into sand milling discharging-material size by strengthening pulverizing process, then Cross 325 eye mesh screens, screenings post processing and obtain finished product titanium dioxide.
Preferably, in the above method, described reinforcing pulverizing process is sanded using Raymond mill+two-stage, roll mill+wet ball mill + repeatedly be sanded in any one mode.
Preferably, in the above method, described screen area is sufficiently large.
Preferably, in the above method, the setting angle of the screen cloth is 4~10 degree.
Further, in the above method, the setting angle of described screen cloth is 5 degree.
The inventive method controls rational screening aperture, sulfate process titanium dioxide is fallen into kiln product coarse granule and thin grit is carried out Separate, thick soft particle is sent to middle powder operation, and thin grit is sent to reinforcing pulverizing process, is so sent to the titanium white of postprocessing working procedures Slurry will be in the range of suitable particle size, so as to finally improve the cleannes of titanium white product.
Specific embodiment
Inevitably produce some tiny compared with grit, some of them particle during existing method for producing gtitanium dioxide with sulphuric acid Main component is TiO2, at 2 μm or so, these particles can not effectively be broken and disperse particle diameter in middle powder operation, if by Slurry after inorganic surface treatment is intercepted and sieved, and sieve aperture is larger can not to be obtained granularity and meet desired titanium dioxide, sieve aperture compared with Small slurry cannot be sieved again, so as to influence the cleannes of final titanium dioxide.
Coarse granule for this influence titanium dioxide cleannes is mainly TiO2Situation, inventor by research find, The vibratory sieve of 150~200 eye mesh screens is installed after roasting terminates, by screening, during larger softer particle is directly entered on sieve Powder operation, post processing obtain finished product titanium dioxide;Relatively thin harder particle carries out reinforcing pulverizing process and grinds sand milling under sieve After stock discharge granularity, finished product is obtained after 325 mesh sieves, screenings post processing.
Inventor has found, sieve number is too big when then mesh opening size is too small, and the relatively thin harder particle of granularity has part On sieve, powder operation, post processing necessarily affect the cleannes of product during such as directly oversize is entered;When sieve number too it is small then When mesh opening size is too big, the larger softer particle of granularity has part under sieve, such as enters reinforcing pulverizing process, will necessarily increase The burden that reinforcementization is crushed.So, need to be by the Task-size Controlling of vibratory sieve in 150~200 mesh.
Sieved by the vibratory sieve of this mesh number, general 99.9% is sized on sieve, and this partial material particle is larger Softer, carrying out conventional middle powder operation, post processing can just prepare the preferable titanium dioxide of cleannes;General 0.1% is sized sieve Under, this partial material particle relatively it is thin it is harder (herein be carefully compared with oversize, but for relative finished product, its granularity compared with Slightly), if do not carried out specially treated, directly carrying out conventional middle powder operation, post processing will influence the cleannes of titanium dioxide, institute So that inventor has found that the partial material should be made to be crushed to sand milling stock discharge granularity by the way of crushing is strengthened, after 325 mesh Screen cloth, screenings post processing can also prepare the preferable titanium dioxide of cleannes.
Technique and equipment that reinforcing pulverizing process described in the inventive method does not determine, as long as can be thin grit under sieve Grind sand milling stock discharge granularity requirements, such as can recommend using " Raymond mill+two-stage sand milling " or " roll mill+ Wet ball mill+be sanded repeatedly " technique meets sand milling slurry granularity requirements until slurry granularity.
The mesh oversize of the inventive method 150~200, the post processing of screenings can respectively be post-processed and remixed, or mixing Post-processed again afterwards.
Further, in order to efficiently separate, the sieving area of vibratory sieve should be sufficiently large.
Further, in order to prevent titanium white first product from buildup and being kept for certain residence time in vibratory sieve, vibratory sieve is installed Angle be set to 4~10 degree.Preferably 10 degree.
In actual production technique, screenings can use titanium white storage tank, and titanium dioxide storage tank and corresponding pipeline answer wear-resisting and corrosion resistant Erosion, tank capacity 20m3, the nominal diameter of titanium white first product feed pipe and discharge nozzle is selected as 20cm in case line clogging, feed pipe peace Mounted in the top of tank body, discharge nozzle is arranged on bottom, and the bottom of tank body should be designed as cone, so that blowing is not accumulated Material phenomenon.
Embodiment 1
Taking the oversize 100g of 200 mesh shaking screens carries out middle powder operation, post-processes to obtain finished product titanium dioxide;Screenings 100g titaniums In vain fall kiln first product, at a high speed crush 30s after, according to 300g/L be beaten, 0.6mm zirconiums pearl be sanded 40min (2000rpm, zirconium oxide bead with For 1/1), after 325 mesh sieves, then inorganic coating is surface-treated titanium white first product mass ratio, adds 5 ‰ organosilicons to be had Vapour powder after machine treatment, then measures its cleannes.
Comparative example 1
Directly take sulfate process titanium dioxide to fall kiln first product 100g, after crushing 30s at a high speed, be beaten according to 300g/L, 0.6mm zirconium pearl sand (2000rpm, for 1/1), after 325 mesh sieves, then inorganic coating carries out table to mill 40min for zirconium oxide bead and titanium white first product mass ratio Face is processed, and adds 5 ‰ organosilicons to carry out vapour powder after organic process, then measures its cleannes.
Comparative example 2
Taking the oversize 100g of 100 mesh shaking screens carries out middle powder operation, post-processes to obtain finished product titanium dioxide;Screenings 100g titaniums In vain fall kiln first product, at a high speed crush 30s after, according to 300g/L be beaten, 0.6mm zirconiums pearl be sanded 40min (2000rpm, zirconium oxide bead with For 1/1), after 325 mesh sieves, then inorganic coating is surface-treated titanium white first product mass ratio, adds 5 ‰ organosilicons to be had Vapour powder after machine treatment, then measures its cleannes.
Table 1
From above-described embodiment 1, comparative example 1,2, in addition to screen number difference, other specification all same;By so Treatment after titanium dioxide cleannes be shown in Table 1, from table 1, be calcined in separating sulfuric acid legal system titanium dioxide using the inventive method After material, the cleannes of titanium white product are significantly improved, and 200 mesh sieves with respect to product after 100 mesh sieves cleannes Improve.

Claims (5)

1. it is a kind of improve sulfuric acid method titanium pigment cleannes method, it is characterised in that:Comprise the following steps:After roasting is terminated Material is sieved with 150~200 eye mesh screens, and oversize is directly entered middle powder operation, post processing and obtains finished product titanium dioxide;By screenings Sand milling discharging-material size is ground by strengthening pulverizing process, finished product titanium white is obtained after 325 eye mesh screens, screenings post processing Powder.
2. method according to claim 1, it is characterised in that:Described reinforcing pulverizing process uses Raymond mill+two-stage sand Mill, roll mill+wet ball mill+repeatedly be sanded in any one mode.
3. method according to claim 1, it is characterised in that:150~200 described mesh sieve web areas are sufficiently large.
4. method according to claim 1, it is characterised in that:The setting angle of 150~200 eye mesh screen is 4~10 Degree.
5. method according to claim 4, it is characterised in that:The setting angle of 150~200 described eye mesh screens is 5 degree.
CN201610557303.2A 2016-07-15 2016-07-15 Method for improving sulfate process titanium dioxide cleanliness Active CN105948110B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610557303.2A CN105948110B (en) 2016-07-15 2016-07-15 Method for improving sulfate process titanium dioxide cleanliness

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610557303.2A CN105948110B (en) 2016-07-15 2016-07-15 Method for improving sulfate process titanium dioxide cleanliness

Publications (2)

Publication Number Publication Date
CN105948110A CN105948110A (en) 2016-09-21
CN105948110B true CN105948110B (en) 2017-05-24

Family

ID=56899958

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610557303.2A Active CN105948110B (en) 2016-07-15 2016-07-15 Method for improving sulfate process titanium dioxide cleanliness

Country Status (1)

Country Link
CN (1) CN105948110B (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109233344A (en) * 2018-11-26 2019-01-18 攀钢集团攀枝花钢铁研究院有限公司 The breaking method of sulfate process titanium dioxide first product
CN112024109A (en) * 2020-08-25 2020-12-04 攀钢集团重庆钒钛科技有限公司 Titanium dioxide particle size distribution control method
CN114106591B (en) * 2021-12-01 2023-08-29 龙佰集团股份有限公司 Preparation method of special titanium white for high-grade automotive finishing paint

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101186332A (en) * 2007-12-19 2008-05-28 龚家竹 Modified method for producing titanium dioxide
CN101823763A (en) * 2009-03-03 2010-09-08 安徽安纳达钛业股份有限公司 Production method of special titanium white

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012184158A (en) * 2011-02-16 2012-09-27 Sumitomo Chemical Co Ltd Low valence titanium oxide powder and zinc oxide-based sintered body

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101186332A (en) * 2007-12-19 2008-05-28 龚家竹 Modified method for producing titanium dioxide
CN101823763A (en) * 2009-03-03 2010-09-08 安徽安纳达钛业股份有限公司 Production method of special titanium white

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
影响钛白产品清洁度的原因分析;王斌等;《钛钢钒钛》;20141231;第35卷(第6期);第18-21页 *
降低钛白粉成品筛余物的研究;陈文娟等;《化学工程师》;20090131;第160卷(第1期);第45-46页 *

Also Published As

Publication number Publication date
CN105948110A (en) 2016-09-21

Similar Documents

Publication Publication Date Title
TWI485004B (en) Preparation method for stainless steel slags and steelworks slags for recovery of metal
TWI582055B (en) Ultra fine milk of lime composition
CN105948110B (en) Method for improving sulfate process titanium dioxide cleanliness
CN101912811B (en) Method for preparing nepheline syenite powder
CN105102132B (en) The method and apparatus for being used to prepare and separating the material including compound more material systems
CN104619648B (en) Based on TiO2Scrub particle, and prepare and use as be based on TiO2Scrub particle method
CN106395839B (en) A kind of technique preparing electrophoretic paint calcined kaolin with gangue
CN105013591A (en) Method for rapidly removing solid impurities in zirconia microspheres
CN108187878B (en) One-section semi-closed-circuit ore grinding and grading process
WO2016071197A1 (en) Method for producing gravels separated into fractions of different grain sizes
CN109233344A (en) The breaking method of sulfate process titanium dioxide first product
CN105921212B (en) The method for reducing titania slurry viscosity
CN109055634B (en) Separate the method and separation system of reactive powder and inert powder in slag micro powder
JP2011005350A (en) Talc dressing method
CN208526782U (en) Wheat grain powder production system
EP2407244B1 (en) Method for comminution of material by a tube mill
JP5493937B2 (en) Classification method of metal fine powder
JP2010155745A (en) Method and system for producing crushed sand for concrete
CN104107764A (en) Method for improving flatness and glossiness of titanium dioxide film
US6036999A (en) Method of preparing grinding media consisting essentially of sintered TiO2 particles
CN113773805A (en) Dry-wet combined production process for superhard material grinding material
CN205462695U (en) Mill of low -intensity reduced iron selects system
DE102014013526A1 (en) Dry grinding and dispersion of titanium dioxide clinker
CN100448545C (en) High-iron gibbsite material grinding process
JP7364128B2 (en) Method for crushing ore and manufacturing method for pellets

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