CN107840640A - Utilize the method for granite waste material production ceramics - Google Patents
Utilize the method for granite waste material production ceramics Download PDFInfo
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- CN107840640A CN107840640A CN201710987200.4A CN201710987200A CN107840640A CN 107840640 A CN107840640 A CN 107840640A CN 201710987200 A CN201710987200 A CN 201710987200A CN 107840640 A CN107840640 A CN 107840640A
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- Prior art keywords
- stone
- waste material
- magnetic separation
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- granite waste
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- 239000010438 granite Substances 0.000 title claims abstract description 38
- 239000002699 waste material Substances 0.000 title claims abstract description 30
- 238000000034 method Methods 0.000 title claims abstract description 22
- 239000000919 ceramic Substances 0.000 title claims abstract description 21
- 238000004519 manufacturing process Methods 0.000 title abstract description 7
- 239000004575 stone Substances 0.000 claims abstract description 73
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims abstract description 46
- 238000007885 magnetic separation Methods 0.000 claims abstract description 38
- 239000002002 slurry Substances 0.000 claims abstract description 36
- 239000000843 powder Substances 0.000 claims abstract description 24
- 229910052742 iron Inorganic materials 0.000 claims abstract description 23
- 239000004576 sand Substances 0.000 claims abstract description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 17
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims abstract description 16
- 239000010703 silicon Substances 0.000 claims abstract description 16
- 229910052710 silicon Inorganic materials 0.000 claims abstract description 16
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 claims abstract description 15
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims abstract description 15
- 239000012535 impurity Substances 0.000 claims abstract description 15
- 239000011777 magnesium Substances 0.000 claims abstract description 15
- 229910052749 magnesium Inorganic materials 0.000 claims abstract description 15
- 229910052758 niobium Inorganic materials 0.000 claims abstract description 15
- 239000010955 niobium Substances 0.000 claims abstract description 15
- GUCVJGMIXFAOAE-UHFFFAOYSA-N niobium atom Chemical compound [Nb] GUCVJGMIXFAOAE-UHFFFAOYSA-N 0.000 claims abstract description 15
- 239000010936 titanium Substances 0.000 claims abstract description 15
- 229910052719 titanium Inorganic materials 0.000 claims abstract description 15
- 239000010433 feldspar Substances 0.000 claims abstract description 10
- 229910052626 biotite Inorganic materials 0.000 claims abstract description 9
- 238000000227 grinding Methods 0.000 claims abstract description 9
- 239000000758 substrate Substances 0.000 claims abstract description 9
- 239000008188 pellet Substances 0.000 claims description 26
- 239000006148 magnetic separator Substances 0.000 claims description 25
- 239000007787 solid Substances 0.000 claims description 16
- 239000002245 particle Substances 0.000 claims description 8
- 238000001694 spray drying Methods 0.000 claims description 8
- 229910052738 indium Inorganic materials 0.000 claims description 2
- 238000002156 mixing Methods 0.000 claims description 2
- 235000013339 cereals Nutrition 0.000 abstract description 21
- 239000004927 clay Substances 0.000 abstract description 5
- 235000012054 meals Nutrition 0.000 abstract description 5
- 238000004064 recycling Methods 0.000 abstract description 4
- 229910052782 aluminium Inorganic materials 0.000 abstract description 3
- 239000004411 aluminium Substances 0.000 abstract description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 abstract description 3
- 238000005516 engineering process Methods 0.000 abstract description 3
- 235000013312 flour Nutrition 0.000 abstract description 3
- BITYAPCSNKJESK-UHFFFAOYSA-N potassiosodium Chemical compound [Na].[K] BITYAPCSNKJESK-UHFFFAOYSA-N 0.000 abstract description 3
- 239000000203 mixture Substances 0.000 abstract description 2
- 238000009837 dry grinding Methods 0.000 description 12
- 239000013067 intermediate product Substances 0.000 description 7
- 230000000052 comparative effect Effects 0.000 description 6
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 6
- 239000000463 material Substances 0.000 description 6
- 239000000047 product Substances 0.000 description 5
- 229910052573 porcelain Inorganic materials 0.000 description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 239000011734 sodium Substances 0.000 description 4
- 229910052681 coesite Inorganic materials 0.000 description 3
- 239000000470 constituent Substances 0.000 description 3
- 229910052906 cristobalite Inorganic materials 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 239000000377 silicon dioxide Substances 0.000 description 3
- 229910052682 stishovite Inorganic materials 0.000 description 3
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N titanium dioxide Inorganic materials O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 3
- 229910052905 tridymite Inorganic materials 0.000 description 3
- 239000007795 chemical reaction product Substances 0.000 description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 description 2
- 239000011707 mineral Substances 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- DLHONNLASJQAHX-UHFFFAOYSA-N aluminum;potassium;oxygen(2-);silicon(4+) Chemical compound [O-2].[O-2].[O-2].[O-2].[O-2].[O-2].[O-2].[O-2].[Al+3].[Si+4].[Si+4].[Si+4].[K+] DLHONNLASJQAHX-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 239000004035 construction material Substances 0.000 description 1
- 238000005034 decoration Methods 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 229910052571 earthenware Inorganic materials 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 1
- 239000010453 quartz Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 229910052572 stoneware Inorganic materials 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B33/00—Clay-wares
- C04B33/02—Preparing or treating the raw materials individually or as batches
- C04B33/13—Compounding ingredients
- C04B33/132—Waste materials; Refuse; Residues
- C04B33/1324—Recycled material, e.g. tile dust, stone waste, spent refractory material
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B33/00—Clay-wares
- C04B33/02—Preparing or treating the raw materials individually or as batches
- C04B33/10—Eliminating iron or lime
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B33/00—Clay-wares
- C04B33/02—Preparing or treating the raw materials individually or as batches
- C04B33/13—Compounding ingredients
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2235/00—Aspects relating to ceramic starting mixtures or sintered ceramic products
- C04B2235/02—Composition of constituents of the starting material or of secondary phases of the final product
- C04B2235/30—Constituents and secondary phases not being of a fibrous nature
- C04B2235/34—Non-metal oxides, non-metal mixed oxides, or salts thereof that form the non-metal oxides upon heating, e.g. carbonates, nitrates, (oxy)hydroxides, chlorides
- C04B2235/3418—Silicon oxide, silicic acids or oxide forming salts thereof, e.g. silica sol, fused silica, silica fume, cristobalite, quartz or flint
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2235/00—Aspects relating to ceramic starting mixtures or sintered ceramic products
- C04B2235/02—Composition of constituents of the starting material or of secondary phases of the final product
- C04B2235/30—Constituents and secondary phases not being of a fibrous nature
- C04B2235/34—Non-metal oxides, non-metal mixed oxides, or salts thereof that form the non-metal oxides upon heating, e.g. carbonates, nitrates, (oxy)hydroxides, chlorides
- C04B2235/3427—Silicates other than clay, e.g. water glass
- C04B2235/3463—Alumino-silicates other than clay, e.g. mullite
- C04B2235/3472—Alkali metal alumino-silicates other than clay, e.g. spodumene, alkali feldspars such as albite or orthoclase, micas such as muscovite, zeolites such as natrolite
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2235/00—Aspects relating to ceramic starting mixtures or sintered ceramic products
- C04B2235/02—Composition of constituents of the starting material or of secondary phases of the final product
- C04B2235/30—Constituents and secondary phases not being of a fibrous nature
- C04B2235/34—Non-metal oxides, non-metal mixed oxides, or salts thereof that form the non-metal oxides upon heating, e.g. carbonates, nitrates, (oxy)hydroxides, chlorides
- C04B2235/3427—Silicates other than clay, e.g. water glass
- C04B2235/3463—Alumino-silicates other than clay, e.g. mullite
- C04B2235/3481—Alkaline earth metal alumino-silicates other than clay, e.g. cordierite, beryl, micas such as margarite, plagioclase feldspars such as anorthite, zeolites such as chabazite
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- C04B2235/00—Aspects relating to ceramic starting mixtures or sintered ceramic products
- C04B2235/02—Composition of constituents of the starting material or of secondary phases of the final product
- C04B2235/50—Constituents or additives of the starting mixture chosen for their shape or used because of their shape or their physical appearance
- C04B2235/54—Particle size related information
- C04B2235/5418—Particle size related information expressed by the size of the particles or aggregates thereof
- C04B2235/5427—Particle size related information expressed by the size of the particles or aggregates thereof millimeter or submillimeter sized, i.e. larger than 0,1 mm
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- C04B2235/00—Aspects relating to ceramic starting mixtures or sintered ceramic products
- C04B2235/02—Composition of constituents of the starting material or of secondary phases of the final product
- C04B2235/50—Constituents or additives of the starting mixture chosen for their shape or used because of their shape or their physical appearance
- C04B2235/54—Particle size related information
- C04B2235/5418—Particle size related information expressed by the size of the particles or aggregates thereof
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- C04B2235/00—Aspects relating to ceramic starting mixtures or sintered ceramic products
- C04B2235/60—Aspects relating to the preparation, properties or mechanical treatment of green bodies or pre-forms
- C04B2235/602—Making the green bodies or pre-forms by moulding
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/60—Production of ceramic materials or ceramic elements, e.g. substitution of clay or shale by alternative raw materials, e.g. ashes
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- Dispersion Chemistry (AREA)
- Materials Engineering (AREA)
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- Organic Chemistry (AREA)
- Environmental & Geological Engineering (AREA)
- Processing Of Solid Wastes (AREA)
- Compositions Of Oxide Ceramics (AREA)
Abstract
The present invention discloses a kind of method that ceramics are produced using granite waste material, belongs to granite waste material utilization technology field.It is included granite waste material graded crushing, and then plus water is ground into the stone slurry of specific grain composition;Stone is starched by preliminary magnetic separation to remove more than 95% iron and the metallics such as 70%~90% biotite and magnesium, silicon, titanium, niobium and objectionable impurities in stone slurry;Then dilute again and carry out further magnetic separation;Stone is starched and mixed with feldspar, sand, clay, and is milled to certain fineness, powder is then made;Finally powder is put into grinding tool and is pressed into base substrate, is then fired.It is too high that iron content in obtained potassium sodium aluminium stone flour produced using prior art instant invention overcomes granite waste material, it is not used to production ceramics or even if can be used for production ceramics, but the quality of the ceramic product obtained by it is generally poor, so as to influence granite dead meal recycling popularization and application the problem of.
Description
Technical field
The invention belongs to granite waste material utilization technology field, and in particular to one kind utilizes granite waste material production pottery
The method of porcelain.
Background technology
Granite plates are a kind of high-quality construction materials, be largely used to high-grade, luxurious building, construct building by laying bricks or stones and filling
Decorations.With the development of modern architecture, the demand of granite plates is increased sharply, the exploitation of granite is further driven to, adds
Work.And substantial amounts of dead meal is generated in the process of granite, substantial amounts of silicon, potassium feldspar, sodium length are contained in stone slurry
The nonmetallic minerals such as stone, aluminum oxide, it is upper number raw material of production ceramics.However, generally granite processing factory is to starch the stone
Directly dumped as useless slurry, so do and not only cause pollution to local environment, also result in the serious waste of resource.
Ceramics are the common names using clay as the product of primary raw material such as pottery, stoneware, porcelain, two so-called potteries and porcelain
(Ceramics)There is three kinds of daily, artistic and architectural faience etc..The traditional concept of ceramics refers to all with nothings such as clay, feldspar, quartz
Machine nonmetallic mineral is the artificial industrial products of raw material.It includes the mixture by clay or containing clay through being kneaded, and shaping, forges
Burn and manufactured various products.By most coarse earthenware its scope is belonged to most fine fine pottery and porcelain.
At present, people begin attempt to granite dead meal potassium sodium aluminium stone flour is made by recycling, and for producing
Ceramics.However, the recycling cost of existing granite dead meal is too high, iron content is too high in product potassium sodium aluminium stone flour, can not
For producing ceramics or even if can be used for production ceramics, but the quality of the ceramic product obtained by it is generally poor, from
And influence the popularization and application of granite dead meal recycling.
The content of the invention
The invention provides a kind of method that ceramics are produced using granite waste material, this method can solve existing granite
The problem of iron residual content is too high in gained end-product in waste recovery processing procedure be present.
In order to solve the above-mentioned technical problem, the technical solution adopted in the present invention is:
It comprises the following steps:
A, first granite waste material is dry grinded into a diameter of 40mm~60mm middle stone pellet, then will the middle stone pellet dry grind into
20mm~40mm gravelstone pellet, then the gravelstone pellet is dry grinded into 5mm~15mm sand grains again;
B, water is added to be ground into stone slurry the sand grains, the solid particle grading of the stone slurry is:
A diameter of 1mm~1.5mm:20%~30%;
A diameter of 2mm~3mm:50%~60%;
A diameter of more than 3mm:≤3%;
C, the stone is starched and carries out preliminary magnetic separation in the magnetic separator of the Gauss field strength of 15000 Gauss field strength~16000 to remove
More than 95% iron and the metallics such as 70%~90% biotite and magnesium, silicon, titanium, niobium and objectionable impurities in stone slurry;
D, stone slurry will be obtained by preliminary magnetic separation, and to be diluted to solid content be 20wt%~30wt%, then 50000 Gauss field strength~
Further magnetic separation is carried out in the magnetic separator of 60000 Gauss field strength;
E, by weight, by the stone slurry of 15 parts~25 parts further magnetic separation of process and 30 parts~45 parts feldspars, 25 parts~35 parts
Sand, the mixing of 15 parts~20 parts clays, and be put into and the fineness of gained mud is milled in ball mill is tailed over for 250 mesh sieves 0.8%
In the range of~1.2%;
F, obtained mud is sprayed into the powder that water content is 6.0%~7.0% using spray drying tower;
G, gained powder is put into grinding tool and is pressed into base substrate, be then fired.
In above-mentioned technical proposal, more specifically technical scheme is:The magnetic separator and F-step of the preliminary magnetic separation of E steps enter one
The magnetic separator for walking magnetic separation is wet type electromagnetic magnetic separator.
Due to being had the advantages that using above-mentioned technical proposal, the present invention:
1st, the present invention is matched somebody with somebody by the way that granite waste material first to be crushed to, is ground into the particle pole of particular size, so as to as sufficient as possible
Using the specific high-strength magnetic field of magnetic separator, the magnetic force to iron is improved, removes more than 95% iron, then again by dilution and again
Using magnetic separator, specifically high-strength magnetic field is removed to residual iron, so as to reduce intermediate product --- in granite waste material stone slurry
Iron content, improve end-product ceramics quality.
2nd, the diameter that the present invention is crushed by the way that every one-level is classified and limited to granite waste material, not only reduces granite
The broken difficulty of waste material, also reduce the magnetic force between particle after granite waste material crushes, avoid being bonded between particle, be beneficial to
Follow-up deferrization process, reduce the residual quantity of iron.
3rd, the present invention selects wet type electromagnetic magnetic separator, can effectively avoid because dust occurs in short grained granite waste material
Fly upward and influence magnetic separation effect.
Embodiment:
Below in conjunction with instantiation, the invention will be further described:
Embodiment 1 --- the method that ceramics are produced using granite waste material
It comprises the following steps:
A, granite waste material is dry grinded into a diameter of 40mm middle stone pellet, the gravelstone grain by the middle stone pellet dry grinding into 20mm
Material, the sand grains by gravelstone pellet dry grinding into 5mm;
B, water is added to be ground into stone slurry the sand grains, the solid particle grading of the stone slurry is:
A diameter of 1mm~1.5mm:20%;
A diameter of 2mm~3mm:50%;
A diameter of more than 3mm:≤3%;
C, stone slurry is subjected to preliminary magnetic separation to remove in powder in the wet type electromagnetic magnetic separator of 15000 Gauss field strength
95.9% iron and the metallics such as 70% biotite and magnesium, silicon, titanium, niobium and objectionable impurities;
D, it is 30wt% that stone slurry will be obtained by preliminary magnetic separation and is diluted to solid content, then in the wet type electromagnetic of 50000 Gauss field strength
Further magnetic separation is carried out in magnetic separator, so as to further remove the metallicses such as iron removaling, magnesium, silicon, titanium, niobium and objectionable impurities;
E, stones of the 15kg Jing Guo further magnetic separation is starched and mixed with 30kg feldspars, 25kg sands, 15kg clays, and be put into ball mill
In be milled to gained mud fineness be that 250 mesh sieves are tailed over as 0.8%;
F, obtained mud is sprayed into the powder that water content is 6.0% using spray drying tower;
G, gained powder is put into grinding tool and is pressed into base substrate, then fired 40 minutes at 1200 DEG C.
Intermediate product made from the present embodiment --- the stone obtained by D step process is starched, the content of its solid constituent
For:K2O 7.1%, Na2O33.6%, AL2O316.9%, SiO261%, Fe2O3 0.1%, TiO20.06%, CaO 0.68%, MgO
0.04%, whiteness 56.3%.
Embodiment 2 --- the method that ceramics are produced using granite waste material
It comprises the following steps:
A, granite waste material is dry grinded into a diameter of 60mm middle stone pellet, the gravelstone grain by the middle stone pellet dry grinding into 40mm
Material, the sand grains by gravelstone pellet dry grinding into 15mm;
B, water is added to be ground into stone slurry the sand grains, the solid particle grading of the stone slurry is:
A diameter of 1mm~1.5mm:30%;
A diameter of 2mm~3mm:60%;
A diameter of more than 3mm:≤3%;
C, stone slurry is subjected to preliminary magnetic separation to remove in powder in the wet type electromagnetic magnetic separator of 16000 Gauss field strength
96% iron and the metallics such as 90% biotite and magnesium, silicon, titanium, niobium and objectionable impurities;
D, it is 25wt% that stone slurry will be obtained by preliminary magnetic separation and is diluted to solid content, then in the wet type electromagnetic of 60000 Gauss field strength
Further magnetic separation is carried out in magnetic separator, so as to further remove the metallicses such as iron removaling, magnesium, silicon, titanium, niobium and objectionable impurities;
E, stones of the 25kg Jing Guo further magnetic separation is starched and mixed with 45kg feldspars, 35kg sands, 20kg clays, and be put into ball mill
In be milled to gained mud fineness be that 250 mesh sieves are tailed over as 1.2%;
F, obtained mud is sprayed into the powder that water content is 7.0% using spray drying tower;
G, gained powder is put into grinding tool and is pressed into base substrate, then fired 30 minutes at 1220 DEG C.
Intermediate product made from the present embodiment --- the stone obtained by D step process is starched, and its each solid constituent contains
Measure and be:K2O 8.0%, Na2O33.8%, AL2O316.7%, SiO260%, Fe2O3 0.09%, TiO20.05%, CaO 0.64%,
MgO 0.03%, whiteness 56.3%.
Embodiment 3 --- the method that ceramics are produced using granite waste material
It comprises the following steps:
A, granite waste material is dry grinded into a diameter of 55mm middle stone pellet, the gravelstone grain by the middle stone pellet dry grinding into 28mm
Material, the sand grains by gravelstone pellet dry grinding into 10mm;
B, water is added to be ground into stone slurry the sand grains, the solid particle grading of the stone slurry is:
A diameter of 1mm~1.5mm:28%;
A diameter of 2mm~3mm:57%;
A diameter of more than 3mm:≤3%;
C, stone slurry is subjected to preliminary magnetic separation to remove in powder in the wet type electromagnetic magnetic separator of 15500 Gauss field strength
More than 95% iron and the metallics such as 88% biotite and magnesium, silicon, titanium, niobium and objectionable impurities;
D, it is 30wt% that stone slurry will be obtained by preliminary magnetic separation and is diluted to solid content, then in the wet type electromagnetic of 58000 Gauss field strength
Further magnetic separation is carried out in magnetic separator, so as to further remove the metallicses such as iron removaling, magnesium, silicon, titanium, niobium and objectionable impurities;
E, stones of the 21kg Jing Guo further magnetic separation is starched and mixed with 38kg feldspars, 28kg sands, 18kg clays, and be put into ball mill
In be milled to gained mud fineness be that 250 mesh sieves are tailed over as 1.0%;
F, obtained mud is sprayed into the powder that water content is 6.2% using spray drying tower;
G, gained powder is put into grinding tool and is pressed into base substrate, then fired 40 minutes at 1150 DEG C.
Intermediate product made from the present embodiment --- the stone obtained by D step process is starched, and its each solid constituent contains
Measure and be::K2O 7.2%, Na2O33.9%, AL2O316.8%, SiO261.5%, Fe2O3 0.11%, TiO20.05%, CaO
0.60%, MgO 0.03%, whiteness 56.3%.
Comparative example 1
It comprises the following steps:
A, granite waste material is dry grinded into a diameter of 40mm middle stone pellet, the gravelstone grain by the middle stone pellet dry grinding into 20mm
Material, the sand grains by gravelstone pellet dry grinding into 5mm;
B, water is added to be ground into stone slurry the sand grains;
C, stone slurry is subjected to preliminary magnetic separation to remove in powder in the wet type electromagnetic magnetic separator of 15000 Gauss field strength
95.9% iron and the metallics such as 70% biotite and magnesium, silicon, titanium, niobium and objectionable impurities;
D, it is 30wt% that stone slurry will be obtained by preliminary magnetic separation and is diluted to solid content, then in the wet type electromagnetic of 50000 Gauss field strength
Further magnetic separation is carried out in magnetic separator, so as to further remove the metallicses such as iron removaling, magnesium, silicon, titanium, niobium and objectionable impurities;
E, stones of the 15kg Jing Guo further magnetic separation is starched and mixed with 30kg feldspars, 25kg sands, 15kg clays, and be put into ball mill
In be milled to gained mud fineness be that 250 mesh sieves are tailed over as 0.8%;
F, obtained mud is sprayed into the powder that water content is 6.0% using spray drying tower;
G, gained powder is put into grinding tool and is pressed into base substrate, then fired 40 minutes at 1200 DEG C.
Intermediate product made from this comparative example --- the stone obtained by D step process is starched, its Fe2O3Content be
0.25%。
Comparative example 2
It comprises the following steps:
A, granite waste material is dry grinded into a diameter of 60mm middle stone pellet, the gravelstone grain by the middle stone pellet dry grinding into 40mm
Material, the sand grains by gravelstone pellet dry grinding into 15mm;
B, water is added to be ground into stone slurry the sand grains;
C, stone slurry is subjected to preliminary magnetic separation to remove in powder in the wet type electromagnetic magnetic separator of 16000 Gauss field strength
90% iron and the metallics such as 60% biotite and magnesium, silicon, titanium, niobium and objectionable impurities;
D, it is 25wt% that stone slurry will be obtained by preliminary magnetic separation and is diluted to solid content, then in the wet type electromagnetic of 60000 Gauss field strength
Further magnetic separation is carried out in magnetic separator, so as to further remove the metallicses such as iron removaling, magnesium, silicon, titanium, niobium and objectionable impurities;
E, stones of the 25kg Jing Guo further magnetic separation is starched and mixed with 45kg feldspars, 35kg sands, 20kg clays, and be put into ball mill
In be milled to gained mud fineness be that 250 mesh sieves are tailed over as 1.2%;
F, obtained mud is sprayed into the powder that water content is 7.0% using spray drying tower;
G, gained powder is put into grinding tool and is pressed into base substrate, then fired 30 minutes at 1220 DEG C.
Intermediate product made from this comparative example --- the stone obtained by D step process is starched, its Fe2O3Content be
0.22%。
Comparative example 3
It comprises the following steps:
A, granite waste material is dry grinded into a diameter of 55mm middle stone pellet, the gravelstone grain by the middle stone pellet dry grinding into 28mm
Material, the sand grains by gravelstone pellet dry grinding into 10mm;
B, water is added to be ground into stone slurry the sand grains;
C, stone slurry is subjected to preliminary magnetic separation to remove in powder in the wet type electromagnetic magnetic separator of 15500 Gauss field strength
More than 95% iron and the metallics such as 88% biotite and magnesium, silicon, titanium, niobium and objectionable impurities;
D, it is 30wt% that stone slurry will be obtained by preliminary magnetic separation and is diluted to solid content, then in the wet type electromagnetic of 58000 Gauss field strength
Further magnetic separation is carried out in magnetic separator, so as to further remove the metallicses such as iron removaling, magnesium, silicon, titanium, niobium and objectionable impurities;
E, stones of the 21kg Jing Guo further magnetic separation is starched and mixed with 38kg feldspars, 28kg sands, 18kg clays, and be put into ball mill
In be milled to gained mud fineness be that 250 mesh sieves are tailed over as 1.0%;
F, obtained mud is sprayed into the powder that water content is 6.2% using spray drying tower;
G, gained powder is put into grinding tool and is pressed into base substrate, then fired 40 minutes at 1150 DEG C.
Intermediate product made from this comparative example --- the stone obtained by D step process is starched, its Fe2O3Content be
0.20%。
Claims (2)
- A kind of 1. method that ceramics are produced using granite waste material, it is characterised in that comprise the following steps:A, first granite waste material is dry grinded into a diameter of 40mm~60mm middle stone pellet, then will the middle stone pellet dry grind into 20mm~40mm gravelstone pellet, then the gravelstone pellet is dry grinded into 5mm~15mm sand grains again;B, water is added to be ground into stone slurry the sand grains, the solid particle grading of the stone slurry is:A diameter of 1mm~1.5mm:20%~30%;A diameter of 2mm~3mm:50%~60%;A diameter of more than 3mm:≤3%;C, the stone is starched and carries out preliminary magnetic separation in the magnetic separator of the Gauss field strength of 15000 Gauss field strength~16000 to remove More than 95% iron and the metallics such as 70%~90% biotite and magnesium, silicon, titanium, niobium and objectionable impurities in stone slurry;D, stone slurry will be obtained by preliminary magnetic separation, and to be diluted to solid content be 20wt%~30wt%, then 50000 Gauss field strength~ Further magnetic separation is carried out in the magnetic separator of 60000 Gauss field strength;E, by weight, by the stone slurry of 15 parts~25 parts further magnetic separation of process and 30 parts~45 parts feldspars, 25 parts~35 parts Sand, the mixing of 15 parts~20 parts clays, and be put into and the fineness of gained mud is milled in ball mill is tailed over for 250 mesh sieves 0.8% In the range of~1.2%;F, obtained mud is sprayed into the powder that water content is 6.0%~7.0% using spray drying tower;G, gained powder is put into grinding tool and is pressed into base substrate, be then fired.
- 2. the method according to claim 1 that ceramics are produced using granite waste material, it is characterised in that:The preliminary magnetic of E steps The magnetic separator of the further magnetic separation of magnetic separator and F-step of selection is wet type electromagnetic magnetic separator.
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