CN106242328A - A kind of Portland clinker - Google Patents
A kind of Portland clinker Download PDFInfo
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- CN106242328A CN106242328A CN201610668137.3A CN201610668137A CN106242328A CN 106242328 A CN106242328 A CN 106242328A CN 201610668137 A CN201610668137 A CN 201610668137A CN 106242328 A CN106242328 A CN 106242328A
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- China
- Prior art keywords
- clinker
- gross mass
- gangue
- grog
- account
- Prior art date
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- Granted
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- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 54
- 239000002994 raw material Substances 0.000 claims abstract description 29
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims abstract description 24
- 239000000377 silicon dioxide Substances 0.000 claims abstract description 21
- 239000004927 clay Substances 0.000 claims abstract description 20
- 235000019738 Limestone Nutrition 0.000 claims abstract description 14
- 239000006028 limestone Substances 0.000 claims abstract description 14
- 239000004576 sand Substances 0.000 claims abstract description 12
- 229910052500 inorganic mineral Inorganic materials 0.000 claims abstract description 11
- 229910052742 iron Inorganic materials 0.000 claims abstract description 11
- 239000011707 mineral Substances 0.000 claims abstract description 11
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims abstract description 10
- 238000002156 mixing Methods 0.000 claims abstract description 8
- 229910052593 corundum Inorganic materials 0.000 claims abstract description 7
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 claims abstract description 7
- 229910001845 yogo sapphire Inorganic materials 0.000 claims abstract description 7
- 229910052918 calcium silicate Inorganic materials 0.000 claims abstract description 5
- 235000012241 calcium silicate Nutrition 0.000 claims abstract description 5
- JHLNERQLKQQLRZ-UHFFFAOYSA-N calcium silicate Chemical compound [Ca+2].[Ca+2].[O-][Si]([O-])([O-])[O-] JHLNERQLKQQLRZ-UHFFFAOYSA-N 0.000 claims abstract description 5
- BCAARMUWIRURQS-UHFFFAOYSA-N dicalcium;oxocalcium;silicate Chemical compound [Ca+2].[Ca+2].[Ca]=O.[O-][Si]([O-])([O-])[O-] BCAARMUWIRURQS-UHFFFAOYSA-N 0.000 claims abstract description 5
- 239000000463 material Substances 0.000 claims description 18
- 239000000203 mixture Substances 0.000 claims description 15
- 239000000126 substance Substances 0.000 claims description 6
- 238000004458 analytical method Methods 0.000 claims description 4
- 229910052681 coesite Inorganic materials 0.000 claims description 2
- 229910052906 cristobalite Inorganic materials 0.000 claims description 2
- 229910052682 stishovite Inorganic materials 0.000 claims description 2
- 229910052905 tridymite Inorganic materials 0.000 claims description 2
- 239000004568 cement Substances 0.000 abstract description 27
- 238000000227 grinding Methods 0.000 abstract description 11
- 230000007423 decrease Effects 0.000 abstract description 4
- 238000005265 energy consumption Methods 0.000 abstract description 2
- 239000002912 waste gas Substances 0.000 abstract description 2
- 230000003247 decreasing effect Effects 0.000 abstract 1
- 238000007599 discharging Methods 0.000 abstract 1
- 230000007613 environmental effect Effects 0.000 abstract 1
- 239000004615 ingredient Substances 0.000 description 20
- 238000000034 method Methods 0.000 description 15
- 239000003245 coal Substances 0.000 description 14
- 238000004519 manufacturing process Methods 0.000 description 13
- 235000010755 mineral Nutrition 0.000 description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- 239000011398 Portland cement Substances 0.000 description 8
- 239000000292 calcium oxide Substances 0.000 description 7
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 7
- 238000001035 drying Methods 0.000 description 7
- 238000001354 calcination Methods 0.000 description 6
- 238000002386 leaching Methods 0.000 description 6
- 238000000354 decomposition reaction Methods 0.000 description 5
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 4
- 235000011941 Tilia x europaea Nutrition 0.000 description 4
- 238000003837 high-temperature calcination Methods 0.000 description 4
- 239000004571 lime Substances 0.000 description 4
- 239000007791 liquid phase Substances 0.000 description 4
- 239000000395 magnesium oxide Substances 0.000 description 4
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 4
- 230000000704 physical effect Effects 0.000 description 4
- 229910052604 silicate mineral Inorganic materials 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 239000004567 concrete Substances 0.000 description 3
- 238000010348 incorporation Methods 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 238000011160 research Methods 0.000 description 3
- 235000012239 silicon dioxide Nutrition 0.000 description 3
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- CQBLUJRVOKGWCF-UHFFFAOYSA-N [O].[AlH3] Chemical compound [O].[AlH3] CQBLUJRVOKGWCF-UHFFFAOYSA-N 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- AGWMJKGGLUJAPB-UHFFFAOYSA-N aluminum;dicalcium;iron(3+);oxygen(2-) Chemical compound [O-2].[O-2].[O-2].[O-2].[O-2].[Al+3].[Ca+2].[Ca+2].[Fe+3] AGWMJKGGLUJAPB-UHFFFAOYSA-N 0.000 description 2
- 230000003321 amplification Effects 0.000 description 2
- 239000011575 calcium Substances 0.000 description 2
- 229910052791 calcium Inorganic materials 0.000 description 2
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- HOOWDPSAHIOHCC-UHFFFAOYSA-N dialuminum tricalcium oxygen(2-) Chemical compound [O--].[O--].[O--].[O--].[O--].[O--].[Al+3].[Al+3].[Ca++].[Ca++].[Ca++] HOOWDPSAHIOHCC-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 238000003199 nucleic acid amplification method Methods 0.000 description 2
- 238000011017 operating method Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000003908 quality control method Methods 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- 239000002893 slag Substances 0.000 description 2
- 239000002910 solid waste Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 239000011593 sulfur Substances 0.000 description 2
- 229910052717 sulfur Inorganic materials 0.000 description 2
- DLYUQMMRRRQYAE-UHFFFAOYSA-N tetraphosphorus decaoxide Chemical compound O1P(O2)(=O)OP3(=O)OP1(=O)OP2(=O)O3 DLYUQMMRRRQYAE-UHFFFAOYSA-N 0.000 description 2
- 239000011573 trace mineral Substances 0.000 description 2
- 235000013619 trace mineral Nutrition 0.000 description 2
- 235000019976 tricalcium silicate Nutrition 0.000 description 2
- 229910021534 tricalcium silicate Inorganic materials 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- MBMLMWLHJBBADN-UHFFFAOYSA-N Ferrous sulfide Chemical compound [Fe]=S MBMLMWLHJBBADN-UHFFFAOYSA-N 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 238000003556 assay Methods 0.000 description 1
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000010881 fly ash Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 229910052909 inorganic silicate Inorganic materials 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000004570 mortar (masonry) Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- CHWRSCGUEQEHOH-UHFFFAOYSA-N potassium oxide Chemical compound [O-2].[K+].[K+] CHWRSCGUEQEHOH-UHFFFAOYSA-N 0.000 description 1
- 229910001950 potassium oxide Inorganic materials 0.000 description 1
- 238000005036 potential barrier Methods 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 238000012797 qualification Methods 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- KKCBUQHMOMHUOY-UHFFFAOYSA-N sodium oxide Chemical compound [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 description 1
- 229910001948 sodium oxide Inorganic materials 0.000 description 1
- 238000003746 solid phase reaction Methods 0.000 description 1
- 238000010671 solid-state reaction Methods 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 238000005406 washing Methods 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
- C04B7/00—Hydraulic cements
- C04B7/24—Cements from oil shales, residues or waste other than slag
-
- 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
- C04B7/00—Hydraulic cements
- C04B7/36—Manufacture of hydraulic cements in general
-
- 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
- Y02P40/10—Production of cement, e.g. improving or optimising the production methods; Cement grinding
-
- 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
- Y02P40/10—Production of cement, e.g. improving or optimising the production methods; Cement grinding
- Y02P40/121—Energy efficiency measures, e.g. improving or optimising the production methods
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Organic Chemistry (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Curing Cements, Concrete, And Artificial Stone (AREA)
- Treatment Of Sludge (AREA)
Abstract
The invention provides a kind of Portland clinker, it is 0.5~1.5% that clinker f CaO controls, clinker liter heavily controls to be 1280~1350 grams per liters, and the granularity of this clinker is 5~15mm, and alite and belite mineral summation content are more than 75%, clinker includes: limestone 83%~86%, iron ore 1.5%~2.5%, gangue 3%~5%, clay 6%~8%, silica sand 1%~3%, controls SiO after the mixing of each raw material2Account for the 10~15% of gross mass, Al2O3Account for the 2.5~3.5% of gross mass, Fe2O3Accounting for the 1.2~2.0% of gross mass, CaO accounts for the 40~45% of gross mass.The clinker heat consumption of the present invention is remarkably decreased, and cement grinding mill and rotary kiln yield are significantly improved, and reduce energy consumption, decrease CO2、NOxDeng the discharge of waste gas, meet national energy-saving and reduce discharging environmental protection policy.
Description
Technical field
The present invention relates to Portland clinker production technical field, be specifically related to one and utilize gangue ingredient to produce silicon
The method of acid salt cement grog.
Background technology
Gangue be mine during and coal washing during the solid waste of discharge, be a kind of in coalification course with coal
Relatively low, harder than the coal black gray expandable rock of a kind of phosphorus content of layer association.Its main component is similar to clay, with silicon dioxide,
Aluminium oxide is main, additionally contains a small amount of ferrum oxide, calcium oxide, magnesium oxide, sodium oxide, potassium oxide, phosphorus pentoxide, three oxidations
Sulfur and trace rare element.Gangue is China's annual emissions and the industrial residue of accumulative amount of storage maximum at present, and gangue is abandoned
Putting and, need not take tract, the sulfide that it contains escapes or leaching meeting atmosphere pollution, farmland and water body.Therefore, research should
Having highly important social meaning with gangue, owing to it has and clay and similar chemical composition thereof, and clay is water
The raw material that in mud production, silica-aluminum materials generally uses, the reaction activity of clay is higher makes cement energy consumption too high, and clay
Exploitation destroys vegetation, damages field, causes many developed countries to prohibit the use of clay cement baking.Therefore research gangue
It is applied to the production of Portland clinker as raw materials for production, both meets the resoures recycling based industry policy of country, protection
Environment, can be again cement production enterprise energy-saving and emission-reduction, reduce cost so that it is turn waste into wealth, have important economic benefit and society
Benefit.
Summary of the invention
It is an object of the invention to for problem above, it is provided that a kind of utilize gangue ingredient to produce Portland clinker
Method, it is possible to increase clinker quality, improves burnability of raw material, improves the yield of rotary kiln, reduces sinter leaching heat consumption, improves water
The performance of mud grog.
A kind of Portland clinker, it is 0.5~1.5% that clinker f-CaO controls, clinker liter heavily control be
1280~1350 grams per liters, the granularity of this clinker is 5~15mm, and alite and belite mineral summation content are 75%
Above.
Described clinker include following weight portion raw material composition: limestone 83%~86%, iron ore 1.5%~
2.5%, gangue 3%~5%, clay 6%~8%, silica sand 1%~3%, control SiO after the mixing of each raw material2Account for gross mass
10~15%, Al2O3Account for the 2.5~3.5% of gross mass, Fe2O3Account for the 1.2~2.0% of gross mass, CaO account for gross mass 40~
45%.
More preferably clinker includes that the raw material of following weight portion forms: limestone 85%, iron ore 2%, coal
Spoil 4%, clay 7%, silica sand 2%, control SiO after the mixing of each raw material2Account for the 11.5~13% of gross mass, Al2O3Account for gross mass
2.7~3%, Fe2O3Accounting for the 1.6~1.9% of gross mass, CaO accounts for the 42.5~44% of gross mass.
In gangue, control chemical composition CaO:3~6.5%, SiO2: 55~60%, Al2O3: 17~20%, Fe2O3:
4.2~6.5%, MgO:1~2%, SO3: 0.5~1%;Analysis Values is Aad: 84~88%, Vad: 3~5.5%, Mad:
0.2~0.35%, FCad: 8~10%, Qnet.ad: 100~800kcal/kg.
The invention provides a kind of method utilizing gangue ingredient to produce Portland clinker, specifically include following step
Rapid: to be prepared as dry powder raw material by broken, pre-homogenizing, dispensing, drying, grinding, then raw material are fed new dry process predecomposition
Kiln carries out preheating, decomposing, after after high-temperature calcination cooling obtain grog, in described blending process by the 50 of original clay~
60wt% replaces with gangue, particularly as follows:
1) raw materials for production limestone, clay, iron ore, silica sand, gangue are crushed to respectively≤50mm be stored in heap
In canopy;
2) after in mass, limestone, clay, iron ore, silica sand, gangue being mixed in proportion, feeding is dried and is held concurrently
Grinding system carries out grinding, controls grinding finished product water content≤1.5wt%, the residue on sieve≤16wt% of 80 tm screen, obtains
The raw material for powdered;
3) raw material after homogenizing are fed dry method nsp kiln to carry out preheating, decomposing, then carry out in cement rotary kiln
High-temperature calcination, calcining heat is 1300~1450 DEG C (further preferred temperature is 1400 DEG C), and 8-10min is (the most excellent in calcining
Selecting calcination time is 9min), the material obtaining the partial melting shape that material amount of liquid phase is 25-28% (more preferably controls
Material amount of liquid phase is 25-28%), by the material of molten on grate-cooler with cold with 50~70 DEG C/min of high pressure positive blower air blast
But speed be cooled to 60~100 DEG C obtain Portland clinker (more preferably 60 DEG C/min rate of cooling cool down
To 70 DEG C).
Step 3) in, dry method nsp kiln specification is ¢ 4.8m × 74m, passes through 5 grades of preheatings, divides in dry method nsp kiln
Solution system operates, and control material enters the resolution ratio of rotary kiln simultaneously is 90~95%.5 grades of described preheatings, decomposing systems
For, controlling rotary cement kiln system decomposition furnace outlet temperature is 860~870 DEG C;Rotary cement kiln rear smoke-box temperature be 950~
1050℃;Cement rotary kiln inner second air temperature is 1150~1200 DEG C;In cement rotary kiln, tertiary air temperature is 950~1000 DEG C;
Grate-cooler comb room promotes number of times to be 11~12rpm.
Above-mentioned steps be explained further into: control rotary cement kiln system decomposition furnace outlet temperature by original 880~890
DEG C drop to 860~870 DEG C;Kiln tail smoke-box temperature is dropped to 950~1050 DEG C by 1000~1100 DEG C;Secondary air temperature by 1100~
1150 DEG C bring up to 1150~1200 DEG C;Tertiary air temperature is brought up to 950~1000 DEG C by 880~950 DEG C;One section, grate-cooler comb room
Number of times is promoted to be brought up to 11~12rpm by 9~10rpm.Control the material calcination time 8~10min at clinkering zone, material liquid phase
Amount is 25~28%, it is ensured that grog knot grain size is uniform, and crystal development is good, quickly cools down after entering grate-cooler.This technique walks
In Zhou, the former parameter is the technique being not added with gangue, such as: control rotary cement kiln system decomposition furnace outlet temperature by
Originally 880~890 DEG C drop to 860~870 DEG C, are: when being not added with gangue, rotary cement kiln system decomposition furnace outlet temperature
Degree is 880~890 DEG C, through adding the raw material of gangue, when entering cement rotary furnace, and rotary cement kiln system decomposition furnace outlet
Temperature is 860~870 DEG C, lower same.
The method have the advantages that
1) gangue ingredient is utilized to produce Portland clinker scheme, owing to gangue is multiple containing sulfur, aluminum, ferrum etc.
The oxygen-enriched mineral of trace element, the crystalline phase potential barrier of these mineral is more weak, just can be fast time during high-speed heating more than 800 DEG C
Speed puts oxygen, and the oxygen released just plays the internal depolymerization of cement raw material and goes out [SiO4]-4The effect of reactivity body, thus effectively promote
Entering grog A ore deposit to burn till, the Macro and microelements in gangue also contributes to the appearance ahead of time of grog liquid phase simultaneously, effectively reduces material
Fusing point, promote that further grog A ore deposit generates;Owing to A ore deposit quantity increases, edge, A ore deposit is more clear than in the past, and A ore deposit prism-shaped reduces
Tabular increases, and A ore deposit occurs in the phenomenon around cavity and reduces, and the physical property of portland cement clinker has clear improvement, normal consistency
Being dropped to 23.8% by original 25%, mortar fluidity is risen to 210mm by original 195mm.
2) gangue ingredient is utilized to produce Portland clinker scheme, owing to the addition of gangue can use high KH, height
SM dispensing, adding the content of silicate mineral in grog, the portland cement clinker intensity amplification of production is notable, and resistance to compression in three days improves
2~3MPa, resistance to compression in 28 days improves 1~about 2MPa, and in cement, blending amount of mixture material improves 3~4%.
3) gangue ingredient is utilized to produce Portland clinker scheme, owing to gangue containing relatively low caloric value,
Can effectively facilitate the reduction of sinter leaching coal consumption, a small amount of trace element in addition contained in gangue effectively reduces material
High temperature fusing point and viscosity, improve the burn-ability of raw material, accelerate the carrying out of solid state reaction so that sinter leaching coal consumption is further
Declining, the yield of cement grinding mill and rotary kiln is greatly improved, and is greatly saved the energy, reduces production cost, reduces CO2、NOXDeng
The discharge of waste gas.
4) portland cement clinker prepared by the method provided by the present invention, owing to its physical property significantly improves so that water
Mud mill yield improves;The workability of cement, water-retaining property, the compatibility etc. of cement and admixture are obtained for raising.
Decrease 3~5min with the little pulverizing time consuming of the portland cement clinker of this programme production, be applied to the closed circuit water of Φ 4.2 × 13m
Mud grinds, and cement grinding mill yield can improve 10~20t/h.Concrete prepared by the cement produced with this grog, ensure its service behaviour and
In the case of mass conservation, the consumption of additive can be less with 8~10%.
5) utilize gangue ingredient to produce Portland clinker scheme, not only consume substantial amounts of solid waste bastard coal
Stone, decreases the demand to clay resource, protects agricultural arable land;Too increase in cement the incorporation mixing material simultaneously, disappear
Consume a large amount of industrial waste slag such as slag, flyash etc., reduced the stacking of waste residue, be conducive to beautifying ecological environment.
Detailed description of the invention
Further illustrate the present invention below in conjunction with embodiment, but the scope of protection of present invention is not limited to implement
The scope of example statement.
Embodiment 1:
Utilizing the method that gangue ingredient produces Portland clinker, in first enterprise, new dry process nsp kiln is carried out,
Concrete operating procedure is:
1) clinker raw materials for production limestone, clay, iron ore, silica sand, gangue etc. are crushed to certain particle diameter model
Enclose and be stored in heap canopy.
2) by limestone 85%, iron ore 2%, gangue 4%, clay 7%, silica sand 2% is mixed in the ratio of mass fraction
Close uniformly, wherein control content of MgO≤2.5wt% in limestone, caloric value Q of ganguenet.ad≤800kcal/kg。
3) the vertical of said mixture material feeding band hot blast is carried out grinding during air swept mill, control grinding finished product water content
≤ 1.5wt%, 80 μm tail over≤16wt%, the raw material for powdered obtained.
4) raw material after homogenizing are fed new dry process nsp kiln to carry out preheating, decomposing, then in cement rotary kiln
Carrying out high-temperature calcination, calcining heat is 1400 DEG C, obtains molten state material and forms that size is all neat, physically well develops, rich in A Li
The special crystalline particulate body with belite mineral, last cooled machine is quickly cooled to 70 DEG C and obtains portland cement clinker.
Portland cement clinker quality control index: f-CaO 0.5~1.5%, liter focus on 1280~1350 grams per liters.
Clinker moduli span of control is:
Lime saturation factor (degree of the oxidized calcium of silicon dioxide saturated one-tenth tricalcium silicate in grog): KH=0.93 ±
0.02;
Silica modulus (clinker silicate mineral and the ratio of solvent mineral): SM=2.7 ± 0.1;
Aluminium-oxygen modulus (tricalcium aluminate and the ratio of tetra calcium aluminoferrite in grog fluxing mineral): IM=1.6 ± 0.1.
Wherein in embodiment 1, the chemical composition of raw material is shown in Table 1-1:
Table 1-1
Production to be strengthened to the raw-material pre-homogenizing such as limestone, clay, gangue, troilite, silica sand and moisture
Control, it is ensured that the equalization stable of mixed material composition;Strengthen raw material composition inspection, improve assay accuracy;Adopt
By online Automatic Detection and Control program, it is achieved the instant of raw material composition adjusts automatically.Improve the qualification rate of KH, SM, IM three ratio.
In embodiment 1, with grog chemical analysis results contrast table 1-2 before and after gangue ingredient:
Table 1-2
With grog physical property contrast table 1-3 before and after gangue ingredient:
Table 1-3
It is shown in Table 1-4 with the yield of gangue rotary kiln and grog mark coal consumption:
Table 1-4
Gangue volume | The daily output | Mark coal consumption (kg/t.cli) |
0% | 5950 | 105.6 |
4% | 6100 | 101.3 |
After upper table data know incorporation gangue ingredient, lime saturation ratio and the silica modulus of grog can be properly increased, carry
The content of silicate mineral in high grog, improves grog performance, and the daily output of grog improves 150t/h, grog mark coal consumption
Have dropped 4.3kg/t, 3 days intensity of grog improves 3.1MPa, and within 28 days, intensity improves 2MPa.To sum up, gangue ingredient is used
After, grog yield and quality improves a lot, and grog grindability the most effectively promotes, and grog performance is improved, sinter leaching heat consumption
Decline substantially.
Meanwhile, by the grog research similar with Present Domestic using gangue ingredient to produce, the Integrated comparative of similar technique,
It is shown in Table A:
Table A
Sequence number | Title | Before gangue mixes | After gangue mixes | Amplification |
1 | 3 days comprcssive strength (MPa) of grog | 31.2 | 34.3 | +3.1 |
2 | 28 days comprcssive strength (MPa) of grog | 56.5 | 58.5 | +2.0 |
3 | Rotary kiln yield (t/d) | 5950 | 6100 | +150 |
4 | Grog mark coal consumption (kg/t.cli) | 105.6 | 101.3 | -4.3 |
5 | Grog consumptive use of water normal consistence (ml) | 125 | 11 | -6 |
6 | P.O42.5 cement mixture volume (%) | 15 | 18 | +3 |
7 | P.C32.5 cement mixture volume (%) | 36 | 40 | +4 |
8 | The little time consuming of grog (min) | 36 | 33 | -3 |
9 | The grog presetting period (min) | 102 | 96 | -6 |
10 | Grog final setting time (min) | 152 | 150 | -2 |
Visible, produce Portland clinker with gangue ingredient, above-mentioned every production and technical indication has reached current the most
Advanced international level.
Embodiment 2:
Utilizing the method that gangue ingredient produces Portland clinker, in first enterprise, new dry process nsp kiln is carried out,
Concrete operating procedure is:
1) clinker raw materials for production limestone, clay, iron ore, silica sand, gangue etc. are crushed to certain particle diameter model
Enclose and be stored in heap canopy.
2) by limestone 83%, iron ore 1.8%, gangue 4.2%, clay 6.4%, mass fraction pressed by silica sand 3%
Ratio mix homogeneously, wherein controls content of MgO≤2.5wt% in limestone, caloric value Q of ganguenet.ad≤800kcal/
kg。
3) the vertical of said mixture material feeding band hot blast is carried out grinding during air swept mill, control grinding finished product water content
≤ 1.5wt%, 80 μm tail over≤16wt%, the raw material for powdered obtained.
4) raw material after homogenizing are fed new dry process nsp kiln to carry out preheating, decomposing, then in cement rotary kiln
Carrying out high-temperature calcination, calcining heat is 1450 DEG C, obtains molten state material and forms that size is all neat, physically well develops, rich in A Li
The special crystalline particulate body with belite mineral, last cooled machine is quickly cooled to 100 DEG C and obtains portland cement clinker.
Portland cement clinker quality control index: f-CaO 0.5~1.5%, liter focus on 1280~1350 grams per liters.
Clinker moduli span of control is:
Lime saturation factor (degree of the oxidized calcium of silicon dioxide saturated one-tenth tricalcium silicate in grog): KH=0.93 ±
0.02;
Silica modulus (clinker silicate mineral and the ratio of solvent mineral): SM=2.7 ± 0.1;
Aluminium-oxygen modulus (tricalcium aluminate and the ratio of tetra calcium aluminoferrite in grog fluxing mineral): IM=1.6 ± 0.1.
Utilizing the method that gangue ingredient produces Portland clinker, in second enterprise, new dry process nsp kiln is carried out,
The grog result produced is as follows:
In embodiment 2, with grog chemical analysis results contrast table 2-1 before and after gangue ingredient:
Table 2-1
With grog physical property contrast table 2-2 before and after gangue ingredient:
Table 2-2
It is shown in Table 2-3 with the yield of rotary kiln and grog mark coal consumption before and after gangue:
Table 2-3
Gangue volume | The daily output (t/d) | Mark coal consumption (kg/t.cli) |
0% | 5980 | 126 |
4.2% | 6106 | 102.8 |
After upper table data know incorporation gangue ingredient, in the situation of the lime saturation ratio and silica modulus properly increasing grog
Under, the daily output of grog improves 126t/h, and grog mark coal consumption have dropped 3.2kg/t, and 3 days intensity of grog improves 3.8MPa,
28 days intensity improves 1.9MPa, and little time consuming shortens 4min.To sum up, after using gangue ingredient, grog yield and quality has relatively
Improving greatly, grog grindability, grog performance have clear improvement, and sinter leaching heat consumption declines substantially.
Claims (3)
1. a Portland clinker, it is characterised in that it is 0.5~1.5% that clinker f-CaO controls, clinker liter
Heavily controlling is 1280~1350 grams per liters, and the granularity of this clinker is 5~15mm, and alite and belite mineral summation contain
Amount is more than 75%, and clinker includes that the raw material of following weight portion forms: limestone 83%~86%, iron ore 1.5%~2.5%,
Gangue 3%~5%, clay 6%~8%, silica sand 1%~3%, control SiO after the mixing of each raw material2Account for the 10~15% of gross mass, Al2O3
Account for the 2.5~3.5% of gross mass, Fe2O3Accounting for the 1.2~2.0% of gross mass, CaO accounts for the 40~45% of gross mass.
Portland clinker the most according to claim 1, it is characterised in that clinker includes the former of following weight portion
Material composition: limestone 85%, iron ore 2%, gangue 4%, clay 7%, silica sand 2%, controls SiO after the mixing of each raw material2Account for gross mass
11.5~13%, Al2O3Account for the 2.7~3% of gross mass, Fe2O3Accounting for the 1.6~1.9% of gross mass, CaO accounts for the 42.5 of gross mass
~44%.
Portland clinker the most according to claim 1 and 2, it is characterised in that in gangue, controls chemical composition
CaO:3~6.5%, SiO2: 55~60%, Al2O3: 17~20%, Fe2O3: 4.2~6.5%, MgO:1~2%, SO3: 0. 5~1%;
Analysis Values is Aad: 84~88%, Vad: 3~5.5%, Mad: 0.2~0.35%, FCad: 8~10%, Qnet.ad: 100~
800kcal/kg。
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