CN109013057A - A method of separating feldspar and quartz from granite - Google Patents

A method of separating feldspar and quartz from granite Download PDF

Info

Publication number
CN109013057A
CN109013057A CN201810987774.6A CN201810987774A CN109013057A CN 109013057 A CN109013057 A CN 109013057A CN 201810987774 A CN201810987774 A CN 201810987774A CN 109013057 A CN109013057 A CN 109013057A
Authority
CN
China
Prior art keywords
less
granite
feldspar
equal
quartz
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.)
Granted
Application number
CN201810987774.6A
Other languages
Chinese (zh)
Other versions
CN109013057B (en
Inventor
陈小平
李贵国
王玉臣
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.)
Inner Mongolia Huachen Renewable Resources Technology Co Ltd
Original Assignee
Inner Mongolia Huachen Renewable Resources Technology 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 Inner Mongolia Huachen Renewable Resources Technology Co Ltd filed Critical Inner Mongolia Huachen Renewable Resources Technology Co Ltd
Priority to CN201810987774.6A priority Critical patent/CN109013057B/en
Publication of CN109013057A publication Critical patent/CN109013057A/en
Application granted granted Critical
Publication of CN109013057B publication Critical patent/CN109013057B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • 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
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C1/00Magnetic separation
    • B03C1/02Magnetic separation acting directly on the substance being separated
    • B03C1/30Combinations with other devices, not otherwise provided for
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B07SEPARATING SOLIDS FROM SOLIDS; SORTING
    • B07CPOSTAL SORTING; SORTING INDIVIDUAL ARTICLES, OR BULK MATERIAL FIT TO BE SORTED PIECE-MEAL, e.g. BY PICKING
    • B07C5/00Sorting according to a characteristic or feature of the articles or material being sorted, e.g. by control effected by devices which detect or measure such characteristic or feature; Sorting by manually actuated devices, e.g. switches
    • B07C5/34Sorting according to other particular properties
    • B07C5/342Sorting according to other particular properties according to optical properties, e.g. colour
    • B07C5/3425Sorting according to other particular properties according to optical properties, e.g. colour of granular material, e.g. ore particles, grain

Abstract

The method of the present invention relates to a kind of from granite separating feldspar and quartz, belong to separation ore-sorting technical field, this method includes muck, ore grinding, sub-sieve, photoelectricity color sorting, six processes of powder processed and magnetic separation, using physical technique by granite andesine, quartz, magnetisable material is completely separated, period is without any exhaust gas, the substance that waste water etc. pollutes environment generates, floatation process in the prior art is effectively prevented to endanger environment bring, and utilize the feldspar after this method sorting purification, quartz is entirely capable of replacing natural feldspar, application of the quartz in ceramic industry, sufficient raw in this method, suitable for large-scale industrial production.

Description

A method of separating feldspar and quartz from granite
Technical field
The invention belongs to separation ore-sorting technical fields, and in particular to a kind of separating feldspar from granite and quartz Method.
Background technique
Potassium albite, since fusing point is low, chemical stability is good between 1100-1300 DEG C, with quartz and silicate congruent melting When have a fluxing action, reaction forms low-melting-point glass substance, can reduce the firing temperature of ceramic, promote the burning of ceramic Knot, feldspar plays non-plastic raw material in blank before sintering, improves the hydrophobicity of blank, shortens the drying time of green body, subtracts The dry of few green body shrinks and deforms.In ceramic glaze, after feldspar glass melt is cooling after melting, the glass of glaze is formd Substance increases the transparency of glaze, improves the glossiness and service performance of glaze paint.But Production of Ceramics to be used in nature High-quality feldspar raw material goods and materials it is deficient, quality deteriorates increasingly, considers from ceramic industry long term growth, it is necessary to find feldspar raw material generation Articles.
Different types of granite is all the Minerals And Rocks based on feldspar, quartz, and domestic number is with thousand granites Material processing enterprise is in exploitation process, quarry stone after all generating a large amount of waste material and exploitation, these tailings and quarry stone In the presence of, cause serious pollution to environment, although the chemical component of these granite waste materials be mainly potassium, it is albite, quartz, black Color mica, but due to K in granite waste material2O、Na2O grade is low, and harmful components Fe2O3、TiO2It is higher, therefore cannot be replaced Ceramic glaze is directly used in, in blank for feldspar, and a small amount of preferable granite mine of quality can only also add part and make pottery for low side Among porcelain billet material, prevent a large amount of granite waste material causes the wasting of resources from rationally utilizing and handling.Currently, domestic existing Having granite separating feldspar, quartzy purification technique is mainly floatation process, still, there is a large amount of harmful chemicals in floatation process With the presence of harmful substance, environment is caused great harm, and from the point of view of separation results, the grade of K, Na improve also with regard to 1-2 Percentage point, be not achieved completely sorting purification effect, therefore, be badly in need of one kind can improve K, Na grade and Slave granite in separating feldspar and quartz method.
Summary of the invention
In view of this, the method for the purpose of the present invention is to provide a kind of from granite separating feldspar and quartz.
In order to achieve the above objectives, the invention provides the following technical scheme:
1, a kind of method of separating feldspar from granite and quartz, described method includes following steps:
(1) muck;
(2) ore grinding: will through step (1), treated that granite is put into sand pelletizer processed carries out ore grinding, obtain grain Diameter is less than or equal to the granite block of 8mm;
(3) sub-sieve: the granite block by partial size in step (2) less than or equal to 8mm is put into screen-dividing machine, is obtained respectively Partial size is less than 0.38mm, partial size is more than or equal to 0.38mm and is less than 0.83mm, partial size more than or equal to 0.83mm less than 2.36mm and grain Diameter is more than or equal to 2.36mm and is less than tetra- kinds of granite blocks of 8mm;
(4) partial size obtained in step (3) photoelectricity color sorting: is more than or equal to 0.38mm is less than 0.83mm, partial size is greater than etc. It is less than 2.36mm in 0.83mm and partial size is more than or equal to 2.36mm and is respectively put into photoelectricity color sorting less than tri- kinds of granite blocks of 8mm Photoelectricity color sorting is carried out in machine, finally obtains feldspar and quartz respectively;
(5) powder processed;The feldspar obtained in step (4) and quartz are pulverized respectively, obtain feldspar powder and silica flour;
(6) magnetic separation: the feldspar powder and silica flour that obtain in step (5) are respectively put into magnetic separator and carry out magnetic separation, institute is made State Fe in feldspar powder and silica flour2O3Content, which is respectively less than, is equal to 0.03-0.1wt%.
Further, in step (1), the muck is specially that granite is broken into partial size less than or equal to 400mm's Material block.
Further, in step (2), the sand pelletizer processed is drum-type sand pelletizer, and the drum-type sand is granulated The barrel diameter of machine is 2500mm, barrel lenght 4000mm, main engine power 75kW, revolving speed 25-30r/min.
Further, the cylinder inboard wall of the drum-type sand pelletizer posts corundum liner plate.
Further, the hardness of the corundum liner plate is greater than 9 grades.
Further, in step (4), when the photoelectricity color sorting, used photoelectric colour sorter has can be in 7000- 10000 points of CCD camera lenses for being scanned capture, frequency review one's lessons by oneself compound solenoid valve less than or equal to 1600Hz's;The photoelectricity color sorting The resolution accuracy of machine is heterochromatic less than 200 mesh, conveyor belt speed 2.4-2.75m/s, and color background is set as blue when selecting feldspar Red, color background is set as red when choosing is quartzy.
Further, in step (6), the magnetic separation divides three phases to complete, first magnetic force be 5000-6000 Gauss forever Magnetic separation is carried out in magnetomechanical, is then carried out magnetic separation in the case where magnetic force is the plate magnetic separator of 8000-11000 Gauss, is finally in magnetic force Magnetic separation is carried out under the pulsating high gradient magnetic separator with vertical ring of 13000-14000 Gauss.
The beneficial effects of the present invention are: the side of the present invention provides a kind of from granite separating feldspar and quartz Method, this method all use physical technique to be completely separated granite andesine, quartz, magnetisable material, effectively prevent Floatation process endangers environment bring in the prior art.During the separation process, by adjusting the technological parameter in each stage, make most The feldspar and quartz isolated eventually reach top grade grade, and then can replace natural top grade feldspar and quartz.Wherein, in ore grinding When, it limits using barrel diameter as 2500mm, barrel lenght 4000mm, main engine power 75kW, revolving speed 25-30r/min Drum-type sand pelletizer, it is ensured that it is final to obtain separation thoroughly with the granite block of torispherical state, and powder Body is few, improves identification and resolution ratio for subsequent photoelectricity color sorting, because diameter is excessive when barrel diameter is more than or less than 2500m The separation of granite block be not thorough, the too small granite block of diameter mutually forms Frotteurism, it is serious to cross powder, and work as Cylinder is too long or too short, can generate overground behavior, causes that powder is more, the separation of granite block is not thorough, and low output is asked Topic.In sub-sieve, granite block is subjected to stacking by particle size interval, it is ensured that the effect of subsequent photoelectricity color sorting, in addition, It can be further improved the effect of photoelectricity color sorting using photoelectric colour sorter specific in the present invention, guarantee the feldspar being finally recovered out With the purity of quartz.Finally, magnetic separation divides three phases to complete, the first stage is to remove the machinery iron of production process abrasion as mesh , second stage is for the purpose of selecting mica ferromagnetism, weak magnetic substance, and the phase III is to select the faint magnetism of ultra-fine mica For the purpose of substance, such sublevel stages of magnetic separation can guarantee Fe in the feldspar being finally recovered out and quartz2O3Content, which is respectively less than, to be equal to 0.03-0.1wt% guarantees the quality degree of purity of product.This method is generated without the substance of the pollution environment such as any exhaust gas, waste water, And be entirely capable of replacing the application of natural feldspar, quartz in ceramic industry using feldspar, the quartz after this method sorting purification, it should Sufficient raw in method is suitable for large-scale industrial production.
Detailed description of the invention
In order to keep the purpose of the present invention, technical scheme and beneficial effects clearer, the present invention provides following attached drawing and carries out Illustrate:
Fig. 1 is the domestic granite shape appearance figure in Wulanchabu League of Inner Mongolia city;
Fig. 2 is the domestic granite in Wulanchabu League of Inner Mongolia city through 1200 DEG C of calcined shape appearance figures;
Fig. 3 is the shape appearance figure of the feldspar obtained after the processing of photoelectricity color sorting in embodiment 1;
Fig. 4 is the shape appearance figure of the quartz obtained after the processing of photoelectricity color sorting in embodiment 1;
Fig. 5 is the shape appearance figure of the feldspar obtained after magnetic separation is handled in embodiment 1;
Fig. 6 is the shape appearance figure of the quartz obtained after magnetic separation is handled in embodiment 1;
Fig. 7 is the shape appearance figure of the black mica obtained after magnetic separation is handled in embodiment 1;
Fig. 8 be in embodiment 1 feldspar that is obtained after magnetic separation is handled again through 1200 DEG C of calcined shape appearance figures;
Fig. 9 is quartzy again through 1200 DEG C of calcined shape appearance figures for what is obtained after magnetic separation is handled in embodiment 1.
Specific embodiment
Below by a preferred embodiment of the present invention will be described in detail.
Embodiment 1
It is (as shown in Figure 1) for separation object with the domestic granite in Inner Mongol Wulanchabu, it is separated from the granite Feldspar and quartz, by the granite it is separately sampled send the excellent rich ceramic test center of Wuhan University of Technology, Foshan, Tangshan ceramics detect Center, Shenyang Long Ji magnetoelectricity limited liability company laboratory, Changsha letter are detected along mining industry Co., Ltd etc., and comprehensive analysis is as follows, By mass percentage, contain Al in the granite2O3: 14.6%-17.86%, SiO2: 73.08%-78.02%, Fe2O3: 0.90%-1.47%, CaO:0.78%-1.22%, MgO:0.05%-0.10%, K2O:4.72%-5.24%, Na2O: 3.45%-3.55%, TiO2: 0.02%-1.22%.The granite is milled after 1200 DEG C of calcinings (as shown in Figure 2), whiteness For 4.9-11.3.Huang gang rock andesine and quartz are separated with the following method:
(1) granite muck: is broken into the material block that partial size is less than or equal to 400mm;
(2) ore grinding: will through step (1), treated that granite is put into that barrel diameter is 2500mm, barrel lenght is 4000mm, main engine power 75kW, revolving speed 30r/min, cylinder inboard wall post the drum-type system that hardness is greater than 9 grades of corundum liner plates Ore grinding is carried out in sand pelletizer, obtains the granite block that partial size is less than or equal to 8mm;
(3) sub-sieve: the granite block by partial size in step (2) less than or equal to 8mm is put into screen-dividing machine, is obtained respectively Partial size is less than 0.38mm, partial size is more than or equal to 0.38mm and is less than 0.83mm, partial size more than or equal to 0.83mm less than 2.36mm and grain Diameter is more than or equal to 2.36mm and is less than tetra- kinds of granite blocks of 8mm;
(4) partial size obtained in step (3) photoelectricity color sorting: is more than or equal to 0.38mm is less than 0.83mm, partial size is greater than etc. It is less than 2.36mm in 0.83mm and partial size is more than or equal to 2.36mm and is respectively put into photoelectricity color sorting less than tri- kinds of granite blocks of 8mm Photoelectricity color sorting is carried out in machine, is finally obtained respectively feldspar (as shown in Figure 3) and quartzy (as shown in Figure 4);Used photoelectric color The CCD camera lens of capture can be scanned in 7000-10000 point by selecting machine to have, and frequency is compound less than or equal to reviewing one's lessons by oneself for 1600Hz The resolution accuracy of solenoid valve, the photoelectric colour sorter is heterochromatic less than 200 mesh, and conveyor belt speed is equal to 2.75m/s, face when selecting feldspar Color background is set as blue red, and color background is set as red when choosing is quartzy;
(5) powder processed;The feldspar obtained in step (4) and quartz are pulverized respectively, obtain feldspar powder and silica flour;
(6) magnetic separation: by the feldspar powder and silica flour that are obtained in step (5) first respectively in the permanent magnetism that magnetic force is 6000 Gausses Magnetic separation is carried out in machine, is then carried out magnetic separation in the case where magnetic force is the plate magnetic separator of 10000 Gausses respectively, is finally in magnetic force respectively Magnetic separation is carried out under the pulsating high gradient magnetic separator with vertical ring of 14000 Gausses, finally obtains feldspar (as shown in Figure 5), quartz (such as Fig. 6 It is shown) and black mica (as shown in Figure 7).
The feldspar obtained after magnetic separation, quartz are detected respectively, testing result is as follows:
By mass percentage, contain in the feldspar after magnetic separation: Al2O3: 18.70%, SiO2: 65.88%, Fe2O3: 0.07%, CaO:0.70%, MgO:0.06%, K2O:9.60%, Na2O:4.40%, TiO2: 0.01%.Fe in the feldspar2O3Contain Amount is within the scope of 0.03-0.1wt%, and testing its whiteness through 1200 DEG C of calcinings after cake processed is 68-70, calcined product See Fig. 8.
By mass percentage, contain in the quartz after magnetic separation: Al2O3: 0.90%, SiO2: 98%, Fe2O3: 0.03%, CaO:0.26%, MgO:0.07%, K2O:0.25%, Na2O:0.25%, TiO2: 0.06%.Fe in the quartz2O3Contain Amount is within the scope of 0.03-0.1wt%, and testing its whiteness through 1200 DEG C of calcinings after cake processed is 95, and calcined product is shown in Fig. 9.
Therefore, the feldspar and quartz isolated from granite by method in the present invention can replace natural top grade feldspar and Quartz.
In the present invention, when ore grinding, the revolution of drum-type sand pelletizer can also be 25-30r/ other than for 30r/min Any value in min;When photoelectricity color sorting, photoelectric colour sorter conveyor belt speed is in addition to that can also be 2.4-2.75m/ for 2.75m/s Any value in s;When magnetic separation, the magnetic force of first stage permanent magnetic motor, can also be in 5000-6000 Gauss in addition to for 6000 Gausses Any value, the magnetic force of second stage permanent magnetic motor is in addition to that can also be any in 8000-11000 Gauss for 10000 Gausses Value, the magnetic force of phase III permanent magnetic motor can also be any value in 13000-14000 Gauss, equal energy in addition to being 14000 Gausses Realize the effect in the present invention.
Finally, it is stated that preferred embodiment above is only used to illustrate the technical scheme of the present invention and not to limit it, although logical It crosses above preferred embodiment the present invention is described in detail, however, those skilled in the art should understand that, can be Various changes are made to it in form and in details, without departing from claims of the present invention limited range.

Claims (7)

1. a kind of method of separating feldspar from granite and quartz, which is characterized in that described method includes following steps:
(1) muck;
(2) ore grinding: will through step (1), treated that granite is put into sand pelletizer processed carries out ore grinding, it is small to obtain partial size In the granite block for being equal to 8mm;
(3) sub-sieve: the granite block by partial size in step (2) less than or equal to 8mm is put into screen-dividing machine, obtains partial size respectively It is big less than 2.36mm and partial size more than or equal to 0.83mm less than 0.83mm, partial size to be more than or equal to 0.38mm less than 0.38mm, partial size It is less than tetra- kinds of granite blocks of 8mm in being equal to 2.36mm;
(4) photoelectricity color sorting: the partial size obtained in step (3) is more than or equal to 0.38mm and is more than or equal to less than 0.83mm, partial size 0.83mm is less than 2.36mm and partial size is more than or equal to 2.36mm and is respectively put into photoelectric colour sorter less than tri- kinds of granite blocks of 8mm Middle progress photoelectricity color sorting finally obtains feldspar and quartz respectively;
(5) powder processed;The feldspar obtained in step (4) and quartz are pulverized respectively, obtain feldspar powder and silica flour;
(6) magnetic separation: the feldspar powder and silica flour that obtain in step (5) are respectively put into magnetic separator and carry out magnetic separation, the length is made Fe in mountain flour and silica flour2O3Content, which is respectively less than, is equal to 0.03-0.1wt%.
2. the method according to claim 1, wherein the muck is specially by granite in step (1) It is broken into the material block that partial size is less than or equal to 400mm.
3. the method according to claim 1, wherein the sand pelletizer processed is drum-type sand in step (2) Pelletizer, the barrel diameter of the drum-type sand pelletizer are 2500mm, barrel lenght 4000mm, and main engine power is 75kW, revolving speed 25-30r/min.
4. according to the method described in claim 3, it is characterized in that, the cylinder inboard wall of the drum-type sand pelletizer posts just Beautiful liner plate.
5. according to the method described in claim 4, it is characterized in that, the hardness of the corundum liner plate is greater than 9 grades.
6. the method according to claim 1, wherein in step (4), when the photoelectricity color sorting, used light Electric color selector has and can be scanned the CCD camera lens of capture in 7000-10000 point, and frequency is reviewed one's lessons by oneself less than or equal to 1600Hz's Compound solenoid valve;The resolution accuracy of the photoelectric colour sorter is heterochromatic less than 200 mesh, conveyor belt speed 2.4-2.75m/s, choosing Color background is set as blue red when feldspar, and color background is set as red when choosing is quartzy.
7. first the method according to claim 1, wherein the magnetic separation divides three phases to complete in step (6) Magnetic separation first is carried out in the permanent magnetic motor that magnetic force is 5000-6000 Gauss, then in the flat plate magnet that magnetic force is 8000-11000 Gauss It selects and carries out magnetic separation under machine, finally carry out magnetic separation in the case where magnetic force is the pulsating high gradient magnetic separator with vertical ring of 13000-14000 Gauss.
CN201810987774.6A 2018-08-28 2018-08-28 Method for separating feldspar and quartz from granite stone Active CN109013057B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810987774.6A CN109013057B (en) 2018-08-28 2018-08-28 Method for separating feldspar and quartz from granite stone

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810987774.6A CN109013057B (en) 2018-08-28 2018-08-28 Method for separating feldspar and quartz from granite stone

Publications (2)

Publication Number Publication Date
CN109013057A true CN109013057A (en) 2018-12-18
CN109013057B CN109013057B (en) 2020-05-08

Family

ID=64625673

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810987774.6A Active CN109013057B (en) 2018-08-28 2018-08-28 Method for separating feldspar and quartz from granite stone

Country Status (1)

Country Link
CN (1) CN109013057B (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110606753A (en) * 2019-10-18 2019-12-24 内蒙古华宸再生资源科技有限公司 Method for producing ceramic raw material based on physical purification technology and product
CN110639692A (en) * 2019-09-27 2020-01-03 中国地质科学院郑州矿产综合利用研究所 Method for preparing powder from granite pegmatite by coarse grain separation and dry method
CN112047350A (en) * 2020-09-04 2020-12-08 江西九岭新能源有限公司 Process for extracting high-purity silicon dioxide from granite pegmatite type petalite
CN113042180A (en) * 2021-03-12 2021-06-29 中国地质科学院矿产综合利用研究所 Method for recovering rare earth from heterolite

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2428986A (en) * 2005-08-09 2007-02-14 Racoon Group Ltd A waste recycling system
CN102728478A (en) * 2012-07-07 2012-10-17 蚌埠玻璃工业设计研究院 Beneficiation method for extracting feldspar and quartz from granite
CN103372496A (en) * 2013-06-21 2013-10-30 田辉明 Process method for separating quartz sand, arkosic sand and iron powder from river yellow sand
CN104437830A (en) * 2014-11-05 2015-03-25 中国地质科学院郑州矿产综合利用研究所 Process for removing impurities and improving whiteness of calcite ore
CN105772214A (en) * 2016-05-09 2016-07-20 中国地质科学院郑州矿产综合利用研究所 Mineral separation process for impurity removal and purification of non-metallic ore
CN106000622A (en) * 2016-06-06 2016-10-12 赣州金环磁选设备有限公司 Color-magnetic separation combined sorting method for high-purity quartz sand produced through quartzite
CN107824330A (en) * 2017-09-15 2018-03-23 江苏闽江矿业有限公司 A kind of production method of artificial stone quartz sand

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2428986A (en) * 2005-08-09 2007-02-14 Racoon Group Ltd A waste recycling system
CN102728478A (en) * 2012-07-07 2012-10-17 蚌埠玻璃工业设计研究院 Beneficiation method for extracting feldspar and quartz from granite
CN103372496A (en) * 2013-06-21 2013-10-30 田辉明 Process method for separating quartz sand, arkosic sand and iron powder from river yellow sand
CN104437830A (en) * 2014-11-05 2015-03-25 中国地质科学院郑州矿产综合利用研究所 Process for removing impurities and improving whiteness of calcite ore
CN105772214A (en) * 2016-05-09 2016-07-20 中国地质科学院郑州矿产综合利用研究所 Mineral separation process for impurity removal and purification of non-metallic ore
CN106000622A (en) * 2016-06-06 2016-10-12 赣州金环磁选设备有限公司 Color-magnetic separation combined sorting method for high-purity quartz sand produced through quartzite
CN107824330A (en) * 2017-09-15 2018-03-23 江苏闽江矿业有限公司 A kind of production method of artificial stone quartz sand

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110639692A (en) * 2019-09-27 2020-01-03 中国地质科学院郑州矿产综合利用研究所 Method for preparing powder from granite pegmatite by coarse grain separation and dry method
CN110606753A (en) * 2019-10-18 2019-12-24 内蒙古华宸再生资源科技有限公司 Method for producing ceramic raw material based on physical purification technology and product
CN112047350A (en) * 2020-09-04 2020-12-08 江西九岭新能源有限公司 Process for extracting high-purity silicon dioxide from granite pegmatite type petalite
CN113042180A (en) * 2021-03-12 2021-06-29 中国地质科学院矿产综合利用研究所 Method for recovering rare earth from heterolite
CN113042180B (en) * 2021-03-12 2021-11-16 中国地质科学院矿产综合利用研究所 Method for recovering rare earth from heterolite

Also Published As

Publication number Publication date
CN109013057B (en) 2020-05-08

Similar Documents

Publication Publication Date Title
CN109013057A (en) A method of separating feldspar and quartz from granite
CN106000622B (en) A kind of color of quartzite production glass sand-magnetic separation joint dressing method
CN108940569B (en) Comprehensive utilization method of granite
CN110328047B (en) Method for preparing ceramic raw material from granite stone sawn mud stone powder
CN108504855A (en) A method of producing iron ore concentrate by reducing agent suspending magnetization roasting of siderite
CN102363218B (en) Method for producing copper-powder-containing iron by reducing copper-containing furnace cinders directly
CN105107616A (en) Low-cost high-recovery environment-friendly mineral separation method of low-grade vanadium titano-magnetite
CN104128259A (en) Simple magnetic separation process for Anshan type iron carbonate-containing lean magnetite ore
CN105921258A (en) Method for impurity removal and whitening of potassium feldspar
CN105032602B (en) Highly-efficient preparation method of ultra-white quartz sand utilizing vein quartz minerals
CN109622210A (en) A kind of method of weathering type potash feldspar ore gradation grade purification
CN108393191A (en) A kind of novel magnetic iron ore sorting process
CN105689126B (en) A kind of oolitic hematite ore-dressing technique
CN108580022B (en) Mineral processing technology for producing chemical-grade chromite concentrate
CN110369119B (en) Comprehensive recovery process for iron, carbon and zinc in steel mill dust waste
CN108217666A (en) A kind of processing method of wollastonite
CN110606675B (en) Vanadium-titanium slag superfine powder admixture and preparation method thereof
CN102886308B (en) Method for recycling waste rare-earth polishing powder
CN104446500B (en) Compound ceramic nozzle of a kind of boron nitride/silicon powder and preparation method thereof
CN113087546B (en) Iron-based artistic black glaze and preparation method thereof
CN103962222A (en) Method for recleaning of vanadium-titanium magnetite concentrates through calcination, alkaline leaching, desliming and magnetic separation
CN101993236B (en) Method to prepare full-body tiles by iron tailings
CN104138852A (en) Method for separating miscellaneous stone from talcum mine
CN114671440A (en) Superconducting high-gradient magnetic separation high-silicon solid waste low-carbon green preparation of high-purity SiO2Method (2)
CN101701288B (en) Process for roasting and restoring tailings with weak-intensity magnetism by dragon kiln

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
GR01 Patent grant
GR01 Patent grant