CN1927755A - Fluid-bed boiler fly ash autoclaved brick and preparation method thereof - Google Patents
Fluid-bed boiler fly ash autoclaved brick and preparation method thereof Download PDFInfo
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- CN1927755A CN1927755A CNA200610068806XA CN200610068806A CN1927755A CN 1927755 A CN1927755 A CN 1927755A CN A200610068806X A CNA200610068806X A CN A200610068806XA CN 200610068806 A CN200610068806 A CN 200610068806A CN 1927755 A CN1927755 A CN 1927755A
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- fly ash
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- bed boiler
- boiler fly
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- 239000010881 fly ash Substances 0.000 title claims abstract description 56
- 239000011449 brick Substances 0.000 title claims abstract description 52
- 238000002360 preparation method Methods 0.000 title claims description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 28
- 239000002893 slag Substances 0.000 claims abstract description 23
- 239000004575 stone Substances 0.000 claims abstract description 13
- 238000005096 rolling process Methods 0.000 claims abstract description 11
- 238000010025 steaming Methods 0.000 claims abstract description 10
- 239000000203 mixture Substances 0.000 claims description 15
- 239000002994 raw material Substances 0.000 claims description 11
- 238000000748 compression moulding Methods 0.000 claims description 10
- FGIUAXJPYTZDNR-UHFFFAOYSA-N potassium nitrate Chemical compound [K+].[O-][N+]([O-])=O FGIUAXJPYTZDNR-UHFFFAOYSA-N 0.000 claims description 10
- 230000009977 dual effect Effects 0.000 claims description 8
- 238000003756 stirring Methods 0.000 claims description 8
- 238000010298 pulverizing process Methods 0.000 claims description 7
- 238000000465 moulding Methods 0.000 claims description 4
- 238000000034 method Methods 0.000 abstract description 2
- 238000002156 mixing Methods 0.000 abstract description 2
- 239000003818 cinder Substances 0.000 abstract 1
- 238000003825 pressing Methods 0.000 abstract 1
- 239000000047 product Substances 0.000 description 18
- 239000010884 boiler slag Substances 0.000 description 9
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 8
- 238000001035 drying Methods 0.000 description 5
- 235000012255 calcium oxide Nutrition 0.000 description 4
- 239000000292 calcium oxide Substances 0.000 description 4
- 238000002485 combustion reaction Methods 0.000 description 4
- 239000003245 coal Substances 0.000 description 3
- 239000004615 ingredient Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 230000029087 digestion Effects 0.000 description 2
- 238000010304 firing Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 239000005997 Calcium carbide Substances 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 241000565356 Fraxinus pennsylvanica Species 0.000 description 1
- 229910004298 SiO 2 Inorganic materials 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 238000003556 assay Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 239000011083 cement mortar Substances 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 229910052602 gypsum Inorganic materials 0.000 description 1
- 239000010440 gypsum Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229920001296 polysiloxane Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000007639 printing Methods 0.000 description 1
- 230000011218 segmentation Effects 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- CLZWAWBPWVRRGI-UHFFFAOYSA-N tert-butyl 2-[2-[2-[2-[bis[2-[(2-methylpropan-2-yl)oxy]-2-oxoethyl]amino]-5-bromophenoxy]ethoxy]-4-methyl-n-[2-[(2-methylpropan-2-yl)oxy]-2-oxoethyl]anilino]acetate Chemical compound CC1=CC=C(N(CC(=O)OC(C)(C)C)CC(=O)OC(C)(C)C)C(OCCOC=2C(=CC=C(Br)C=2)N(CC(=O)OC(C)(C)C)CC(=O)OC(C)(C)C)=C1 CLZWAWBPWVRRGI-UHFFFAOYSA-N 0.000 description 1
- 230000000007 visual effect Effects 0.000 description 1
Images
Classifications
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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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/91—Use of waste materials as fillers for mortars or concrete
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- Processing Of Solid Wastes (AREA)
Abstract
The present invention relates to one kind of fluidized bed boiler flyash steaming and pressurizing brick and its making process. The brick is made with flyash in 40-50 wt%, cinder and/or stone bits in 30-40 wt% and carbide slag in 20- 25 wt%, and through mixing after adding water, rolling to crushing, pressing to form and high pressure steam curing. The present invention has best utilization of slag resource, low cost and environment friendship, and the product has high quality, high strength, small shrinkage, high antifreezing performance and high stability.
Description
Technical field
The present invention relates to a kind of preparation method of fluid-bed boiler fly ash autoclaved brick, utilize industrial residue to produce composition brick.
Background technology
Flyash brick production has had document announcement, and situation is as follows:
(1) raw material of the flyash brick of comparative maturity production now is with the flyash behind the coal powder boiler combustion.This flyash granularity is little, carbon content is low, is generally less than 8%, and calcium, silicone content are higher relatively, is easy to be utilized.And circular fluid bed output flyash takes on a red color, and is red ash, and carbon content is too high, generally about 20%, affects the application of brickmaking, mainly shows aspects such as finished bricks weak strength, freeze-thaw-index error.
(2) agglutinate that existing flyash brick is commonly used is a unslaked lime, and the unslaked lime price is higher, but also needs to use ball mill levigate, the digestion time of also wanting 2～3 hours during use.
(3) aggregate: need the grain composition requirement.
And existing flyash brick product drying shrinking percentage is bigger, generally 0.6～1.0%, the body of wall of building by laying bricks or stones is easy to produce the crack, the interior wall top of exterior wall junction in the crack mainly occurs in, be the splayed configuration diagonal crack, gable middle part: the door-window opening upper and lower is 45 degree oblique segmentations and window opening mouth wall along the vertical or ladder crack of perpends and brick middle part; The horizontal slit that also has the roof parapet.
Existing flyash brick all is compression molding, and the brick smooth surface is poor with the conventional cement mortar cohesive force, causes masonry shear strength low, is unfavorable for using in the area of providing fortification against earthquakes.
Summary of the invention
The object of the present invention is to provide a kind of fluid-bed boiler fly ash autoclaved brick and preparation method thereof, make full use of slag ingredient, cost is low, and the protection environment has obtained good quality product again.
Fluid-bed boiler fly ash autoclaved brick of the present invention makes after batching, moulding and steaming are pressed, and its raw material weight percentage composition is: flyash 40～50%, slag are or/and stone nitre 30～40% and carbide slag 20～25%.
The spent material calcium carbide slag replaces unslaked lime, has eliminated the primary pollution source in chemical plant, and cost is lower by about 3/4 than unslaked lime, and without digestion time, and need not join gypsum, and greatly reduce raw materials cost, protected environment.
Utilize stone nitre or/and boiler slag replaces aggregate, water-absorbent is strong, can increase product strength.Stone nitre also can mix use or/and slag can be selected one list usefulness, preferably to meromict, guarantees product strength.
The raw materials used flyash of the present invention, slag, stone nitre and carbide slag are fetched direct use and are got final product.The performance condition basically identical of used fluid-bed boiler fly ash can be general, and slag is pulverized coal firing boiler slag or fluidized-bed combustion boiler slag, can.With the surface design of autoclaved brick is uneven surface, increases surfaceness, improves the cohesive force of building by laying bricks or stones, strengthens shear strength, guarantees the steadiness of masonry panel.Can be directly with brand printing on the surface, form roughness, both formed uneven surface.
The preparation method of fluid-bed boiler fly ash autoclaved brick of the present invention adds water with batching and mixes, and compression moulding after wheel roller is pulverized gets product through high-pressure steaming and cultivating.
Wherein:
The batching amount of water is controlled to be 5～15% of batching gross weight and suits.The water that uses can use autoclave agglomerative water, has both saved the water source, has improved the quality and the quality product of water again, has reduced product cost, has realized recycle.
Batching stirs and adopts well behaved dual horizontal axle forced mixer to stir, and guarantees good stirring and mixing effect.
The rolling pulverizing time of wheel roller is controlled to be 3～5 minutes and suits.
The preferred 1000 tons of hydraulic forming machines compacting of compression moulding, as HF1100 ton hydraulic brick press machine, forming pressure is 100MPa, can solve adobe gassiness, slabbing and autoclaved brick drying shrinkage defective, and improves the product real density.
Steam to press and handle: formed green brick is placed in the autoclave, feed water vapor in autoclave, pressure reaches 0.8～1MPa, and temperature reaches 180～200 ℃, 5～6 hours constant temperature and pressure hold-times, the product of natural then decrease temperature and pressure after 2～3 hours.
The generally existing flyash brick of the compressive strength rate of autoclaved fly ash brick improves 50～100Kg/cm2, and drying shrinkage value also greatly reduces, and the performance of brick obviously improves.The drying shrinkage value is decreased to 0.40mm/m by original 0.66mm/m (the JC239-2001 salable product are less than 0.75mm/m), helps applying of fly ash autoclaved brick.
Fly ash autoclaved brick of the present invention and the contrast of flyash brick quality index see Table 1.
Table 1, autoclaved fly ash brick of the present invention and flyash brick quality index contrast table
| Interventions Requested | The flyash brick standard-required | Assay | Individual event is judged | |
| Size deviation mm | Premium grads | Long ± 2 wide ± 2 are thick ± and 1 | -2 -2 -1 | Reach premium grads |
| Visual appearance | Respective level unacceptable product brick≤5 | 46 of premium gradss; 4 of acceptable end products | Reach premium grads | |
| Aberration | Should be not remarkable | Not remarkable | Reach standard | |
| Intensity MPa | Ultimate compression strength mean value 〉=15.0 monolithic minimum value 〉=12.0 folding strength minimum value 〉=3.3 monolithic minimum value 〉=2.6 | 15.0 13.8 3.3 2.9 | Reach MU15 | |
| Frost resistance | 15 freeze-thaw cycle dry mass loss monolithic maximum value≤2.0% ultimate compression strength mean value 〉=12.0Mpa | 1.1％ 13.3Mpa | Reach MU15 | |
| Drying shrinkage value | Mean value≤0.65mm/m | 0.40mm/m | Reach premium grads | |
Fluid-bed boiler fly ash autoclaved brick of the present invention makes full use of slag ingredient, and the realization resources circulation is utilized again, and cost is low, and the protection environment has obtained good quality product again, the intensity height, and shrinkage value is little, and frost resistance is good, good stability.
Description of drawings
Fig. 1, process flow diagram of the present invention.
Embodiment
The invention will be further described below in conjunction with embodiment.
Used fluid-bed boiler fly ash material composition sees Table 2.
Table 2, fluid-bed boiler fly ash material composition table
| Numbering | Analyze composition (weight %) | ||||||
| SiO 2 | Al 2O 3 | SO 4 2- | Loss on ignition | 325 mesh sieves sieve down | Quality | Remarks | |
| The 1# boiler | 41.98 | 23.20 | 2.08 | 14.82 | 68.81 | Not up to standard | Fluidized-bed combustion boiler |
| The 2# boiler | 40.44 | 22.40 | 2.14 | 17.31 | 77.37 | Not up to standard | Fluidized-bed combustion boiler |
Embodiment 1
1, get the raw materials ready:
(1) flyash: the flyash in the 1# of the heat power plant boiler electricity dust-collecting bin is transported to brick field squeezes into bulk cement storage tank.
(2) it is other standby slag, stone nitre to be transported to batch hopper.
(3) it is other standby carbide slag to be transported to batch hopper.
2, the ingredients by weight percentage composition is:
Flyash 40%, 1# boiler slag or stone nitre 40% and carbide slag 20%.
3, stir:
To prepare burden and drop in the dual horizontal axle forced mixer, the water that adds batching gross weight 10% mixes stirring.
4, rolling:
The compound that stirs is put into wheel roller through 4 minutes rollings.
5, brickmaking:
The moulding mixture that is mixed into that rolling is good is sent into HF1100 ton hydraulic brick press machine and is pressed, and forming pressure is 100MPa, suppresses 32 blocks of standard squares at every turn.Rough trade mark is arranged on the compacting tool set, make the mould brick of compacting form uneven surface.
6, sign indicating number base:
With per 64 of moulding adobe is one group, is seated on the dull and stereotyped steam-cured dolly totally 11 layers 1408 with mechanical manipulator.
7, high pressure steams oxygen:
Steam-cured dolly is pushed in the autoclave, in autoclave, feeds water vapor, pressure 1MPa, 180 ℃ of temperature, constant temperature and pressure kept 5 hours, natural decrease temperature and pressure open after 3 hours still unload product.
Embodiment 2
Fluid-bed boiler fly ash autoclaved brick of the present invention, the raw material weight percentage composition is: 1# boiler fly ash 50%, 1# boiler slag and stone nitre half-and-half amount to 30% and carbide slag 20%.
The preparation method:
Batching is added water mixed by dual horizontal axle forced mixer, amount of water is pulverized through wheel roller for 12% of the batching gross weight, the rolling pulverizing time is 5 minutes, utilizes the compression moulding of HF1100 ton hydraulic forming machine, and forming pressure is 100MPa, rough decorative pattern is arranged on the compacting tool set, be used to form uneven surface, after the high-pressure steaming and cultivating processing, feed water vapor, pressure 0.8MPa, 200 ℃ of temperature, 6 hours constant temperature and pressure hold-times, natural then decrease temperature and pressure 2 hours gets product.
Embodiment 3
Fluid-bed boiler fly ash autoclaved brick of the present invention, the raw material weight percentage composition is: 1# boiler fly ash 45%, stone nitre 30% and carbide slag 25%.
The preparation method:
Batching is added water to be mixed by dual horizontal axle forced mixer, amount of water is 7% of the batching gross weight, pulverize through wheel roller, the rolling pulverizing time is 5 minutes, utilize the compression moulding of HF1100 ton hydraulic forming machine, forming pressure is 100MPa, rough decorative pattern is arranged on the compacting tool set, be used to form uneven surface, after high-pressure steaming and cultivating is handled, feeding pressure is that 0.9MPa, temperature are 185 ℃ water vapor, 5.5 hours constant temperature and pressure hold-times, natural then decrease temperature and pressure 2.5 hours can be finished product.
Embodiment 4
Fluid-bed boiler fly ash autoclaved brick of the present invention, the raw material weight percentage composition is: 1# boiler fly ash 42%, 1# boiler slag 36% and carbide slag 22%.
The preparation method:
Batching is added water to be mixed by dual horizontal axle forced mixer, amount of water is 13% of the batching gross weight, pulverize through wheel roller, the rolling pulverizing time is 4 minutes, utilize the compression moulding of HF1100 ton hydraulic forming machine, forming pressure is 100MPa, rough decorative pattern is arranged on the compacting tool set, be used to form uneven surface, after high-pressure steaming and cultivating is handled, feeding pressure is that 1MPa, temperature are 190 ℃ water vapor, 5 hours constant temperature and pressure hold-times, natural then decrease temperature and pressure 3 hours can be finished product.
Embodiment 5
Fluid-bed boiler fly ash autoclaved brick of the present invention, the raw material weight percentage composition is: 1# boiler fly ash 47%, stone nitre 30% and carbide slag 23%.
The preparation method:
Batching is added water to be mixed by dual horizontal axle forced mixer, amount of water is 10% of the batching gross weight, pulverize through wheel roller, the rolling pulverizing time is 5 minutes, utilize the compression moulding of HF1100 ton hydraulic forming machine, forming pressure is 100MPa, rough decorative pattern is arranged on the compacting tool set, be used to form uneven surface, after high-pressure steaming and cultivating is handled, feeding pressure is that 0.85MPa, temperature are 195 ℃ water vapor, 5.5 hours constant temperature and pressure hold-times, natural then decrease temperature and pressure 3 hours can be finished product.
Embodiment 6
Fluid-bed boiler fly ash autoclaved brick of the present invention, the raw material weight percentage composition is: 1# boiler fly ash 47%, 1# boiler slag 30% and carbide slag 23%.
The preparation method:
Batching is added water to be mixed by dual horizontal axle forced mixer, amount of water is 11% of the batching gross weight, pulverize through wheel roller, the rolling pulverizing time is 4.5 minutes, utilizes the compression moulding of HF1100 ton hydraulic forming machine, forming pressure is 100MPa, handle through high-pressure steaming and cultivating, feeding pressure is that 0.8MPa, temperature are 200 ℃ water vapor, 5 hours constant temperature and pressure hold-times, natural then decrease temperature and pressure 2.5 hours can be finished product.
1# boiler fly ash among the embodiment 1-6 is replaced by the 2# boiler fly ash, carries out same test, obtain essentially identical result.
1# boiler fly ash among the embodiment 1-6 is replaced by the 2# boiler fly ash, slag wherein is replaced by the 2# boiler slag, carry out same test, obtain essentially identical result.
Slag among the embodiment 1-6 is replaced by the pulverized coal firing boiler slag, carries out same test, obtain essentially identical result.
Claims (8)
1, a kind of fluid-bed boiler fly ash autoclaved brick makes after batching, moulding and steaming are pressed, and it is characterized in that the raw material weight percentage composition is: flyash 40～50%, slag are or/and stone nitre 30～40% and carbide slag 20～25%.
2, fluid-bed boiler fly ash autoclaved brick according to claim 1, the surface that it is characterized in that autoclaved brick is a uneven surface.
3, the preparation method of the described fluid-bed boiler fly ash autoclaved brick of a kind of claim 1 is characterized in that batching is added water to mix, and compression moulding after wheel roller is pulverized gets product through high-pressure steaming and cultivating.
4, the preparation method of fluid-bed boiler fly ash autoclaved brick according to claim 3, the amount of water that it is characterized in that preparing burden is 5～15% of batching gross weight.
5, the preparation method of fluid-bed boiler fly ash autoclaved brick according to claim 4 is characterized in that batching stirs employing dual horizontal axle forced mixer and stirs.
6, the preparation method of fluid-bed boiler fly ash autoclaved brick according to claim 5, the rolling pulverizing time that it is characterized in that wheel roller is 3～5 minutes.
7, according to the preparation method of claim 3,4,5 or 6 described fluid-bed boiler fly ash autoclaved bricks, it is characterized in that compression moulding utilizes 1000 tons of hydraulic forming machine compactings, forming pressure is 100MPa.
8, the preparation method of fluid-bed boiler fly ash autoclaved brick according to claim 7, it is characterized in that formed green brick is placed in the autoclave, in autoclave, feed water vapor, pressure reaches 0.8～1MPa, temperature reaches 180～200 ℃, 5～6 hours constant temperature and pressure hold-times, the product of natural then decrease temperature and pressure after 2～3 hours.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB200610068806XA CN100425561C (en) | 2006-09-09 | 2006-09-09 | Fluid-bed boiler fly ash autoclaved brick and preparation method thereof |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB200610068806XA CN100425561C (en) | 2006-09-09 | 2006-09-09 | Fluid-bed boiler fly ash autoclaved brick and preparation method thereof |
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| CN1927755A true CN1927755A (en) | 2007-03-14 |
| CN100425561C CN100425561C (en) | 2008-10-15 |
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101879746A (en) * | 2010-06-23 | 2010-11-10 | 南京大学 | Method for preparing circulating fluid bed (CFB) bottom slag base polymer material |
| CN101564866B (en) * | 2008-12-19 | 2011-10-19 | 福建工程学院 | Production technology for concrete building block of autoclaving and air entraining of circulating fluid bed fly ash |
| CN102850037A (en) * | 2012-07-22 | 2013-01-02 | 马吉波 | Production process and formula of novel environment-friendly fly ash load-bearing brick |
| CN105669124A (en) * | 2016-01-07 | 2016-06-15 | 湖北东元坤新型建材有限公司 | Autoclaved fly ash solid brick |
| CN107814553A (en) * | 2017-09-27 | 2018-03-20 | 石狮市鸿辉环保建材有限公司 | A kind of production method of domestic sewage factory firing sludge clinker bricks in environmental protection |
| CN112028599A (en) * | 2020-08-28 | 2020-12-04 | 山东华鲁恒升化工股份有限公司 | Formula and preparation method of autoclaved fly ash brick |
| CN113105205A (en) * | 2021-04-26 | 2021-07-13 | 石嘴山市益瑞生态科技有限公司 | Full-waste-residue autoclaved fly ash brick and preparation method thereof |
| CN113213886A (en) * | 2021-05-12 | 2021-08-06 | 中北大学 | Fly ash autoclaved environment-friendly brick and preparation method thereof |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1048697A (en) * | 1989-07-10 | 1991-01-23 | 抚顺辽宁发电厂科技开发服务处 | The production method of coal-ash immersion brick |
| CN1020891C (en) * | 1989-12-17 | 1993-05-26 | 唐山冀电粉煤灰综合利用科研所 | Method for producing powdered coal ash brick |
| CN1093688A (en) * | 1993-04-10 | 1994-10-19 | 施东奎 | Pure industrial residue no-baked no-steamed building bearing brick and furring tile and preparation method thereof |
| CN100389088C (en) * | 2005-02-08 | 2008-05-21 | 张清学 | Building block, brick without baking and steaming and its manufacturing technology |
-
2006
- 2006-09-09 CN CNB200610068806XA patent/CN100425561C/en active Active
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101564866B (en) * | 2008-12-19 | 2011-10-19 | 福建工程学院 | Production technology for concrete building block of autoclaving and air entraining of circulating fluid bed fly ash |
| CN101879746A (en) * | 2010-06-23 | 2010-11-10 | 南京大学 | Method for preparing circulating fluid bed (CFB) bottom slag base polymer material |
| CN102850037A (en) * | 2012-07-22 | 2013-01-02 | 马吉波 | Production process and formula of novel environment-friendly fly ash load-bearing brick |
| CN105669124A (en) * | 2016-01-07 | 2016-06-15 | 湖北东元坤新型建材有限公司 | Autoclaved fly ash solid brick |
| CN107814553A (en) * | 2017-09-27 | 2018-03-20 | 石狮市鸿辉环保建材有限公司 | A kind of production method of domestic sewage factory firing sludge clinker bricks in environmental protection |
| CN112028599A (en) * | 2020-08-28 | 2020-12-04 | 山东华鲁恒升化工股份有限公司 | Formula and preparation method of autoclaved fly ash brick |
| CN113105205A (en) * | 2021-04-26 | 2021-07-13 | 石嘴山市益瑞生态科技有限公司 | Full-waste-residue autoclaved fly ash brick and preparation method thereof |
| CN113213886A (en) * | 2021-05-12 | 2021-08-06 | 中北大学 | Fly ash autoclaved environment-friendly brick and preparation method thereof |
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| Publication number | Publication date |
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| CN100425561C (en) | 2008-10-15 |
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