CN116395997A - A kind of auxiliary gelling material and its preparation method and application - Google Patents
A kind of auxiliary gelling material and its preparation method and application Download PDFInfo
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- CN116395997A CN116395997A CN202310448782.4A CN202310448782A CN116395997A CN 116395997 A CN116395997 A CN 116395997A CN 202310448782 A CN202310448782 A CN 202310448782A CN 116395997 A CN116395997 A CN 116395997A
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- 239000000463 material Substances 0.000 title claims abstract description 87
- 238000002360 preparation method Methods 0.000 title claims abstract description 35
- 239000004927 clay Substances 0.000 claims abstract description 66
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims abstract description 45
- 239000000843 powder Substances 0.000 claims abstract description 44
- 230000033558 biomineral tissue development Effects 0.000 claims abstract description 40
- 238000000034 method Methods 0.000 claims abstract description 27
- 238000001354 calcination Methods 0.000 claims abstract description 18
- 238000001035 drying Methods 0.000 claims abstract description 9
- 238000000227 grinding Methods 0.000 claims abstract description 9
- 238000001914 filtration Methods 0.000 claims abstract description 8
- 238000005119 centrifugation Methods 0.000 claims abstract description 5
- 230000001089 mineralizing effect Effects 0.000 claims abstract description 3
- 238000009736 wetting Methods 0.000 claims abstract description 3
- 238000003825 pressing Methods 0.000 claims abstract 2
- 239000004568 cement Substances 0.000 claims description 34
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 28
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 20
- 239000001569 carbon dioxide Substances 0.000 claims description 14
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 14
- 239000000706 filtrate Substances 0.000 claims description 13
- 239000002245 particle Substances 0.000 claims description 12
- 239000010419 fine particle Substances 0.000 claims description 10
- 239000007788 liquid Substances 0.000 claims description 5
- 238000002156 mixing Methods 0.000 claims description 5
- 238000001556 precipitation Methods 0.000 claims description 5
- 239000007787 solid Substances 0.000 claims description 4
- 239000004567 concrete Substances 0.000 claims description 3
- 239000011148 porous material Substances 0.000 claims description 2
- 239000000047 product Substances 0.000 claims 1
- 238000005265 energy consumption Methods 0.000 abstract description 8
- 239000011398 Portland cement Substances 0.000 abstract description 6
- 239000004566 building material Substances 0.000 abstract description 3
- 238000005507 spraying Methods 0.000 abstract description 2
- 230000000052 comparative effect Effects 0.000 description 36
- 239000000203 mixture Substances 0.000 description 16
- 239000002002 slurry Substances 0.000 description 12
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 description 11
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 10
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 9
- 239000000243 solution Substances 0.000 description 9
- 239000007921 spray Substances 0.000 description 9
- 239000004480 active ingredient Substances 0.000 description 7
- 239000000126 substance Substances 0.000 description 6
- 229910000019 calcium carbonate Inorganic materials 0.000 description 5
- 238000010276 construction Methods 0.000 description 5
- 229910052622 kaolinite Inorganic materials 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 4
- 230000008929 regeneration Effects 0.000 description 4
- 238000011069 regeneration method Methods 0.000 description 4
- 238000007873 sieving Methods 0.000 description 4
- 229910001220 stainless steel Inorganic materials 0.000 description 4
- 239000010935 stainless steel Substances 0.000 description 4
- AKEJUJNQAAGONA-UHFFFAOYSA-N sulfur trioxide Chemical compound O=S(=O)=O AKEJUJNQAAGONA-UHFFFAOYSA-N 0.000 description 4
- 239000006004 Quartz sand Substances 0.000 description 3
- 230000001133 acceleration Effects 0.000 description 3
- 229910000323 aluminium silicate Inorganic materials 0.000 description 3
- 239000007864 aqueous solution Substances 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 239000000404 calcium aluminium silicate Substances 0.000 description 3
- 235000012215 calcium aluminium silicate Nutrition 0.000 description 3
- WNCYAPRTYDMSFP-UHFFFAOYSA-N calcium aluminosilicate Chemical compound [Al+3].[Al+3].[Ca+2].[O-][Si]([O-])=O.[O-][Si]([O-])=O.[O-][Si]([O-])=O.[O-][Si]([O-])=O WNCYAPRTYDMSFP-UHFFFAOYSA-N 0.000 description 3
- 229940078583 calcium aluminosilicate Drugs 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 239000002734 clay mineral Substances 0.000 description 3
- 239000002131 composite material Substances 0.000 description 3
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000000945 filler Substances 0.000 description 3
- 238000006703 hydration reaction Methods 0.000 description 3
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 3
- 239000002244 precipitate Substances 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- 239000000377 silicon dioxide Substances 0.000 description 3
- 239000006228 supernatant Substances 0.000 description 3
- 230000002195 synergetic effect Effects 0.000 description 3
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N Calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 description 2
- 235000019738 Limestone Nutrition 0.000 description 2
- 238000002441 X-ray diffraction Methods 0.000 description 2
- -1 aluminate ions Chemical class 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- 229910001424 calcium ion Inorganic materials 0.000 description 2
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 2
- 239000000292 calcium oxide Substances 0.000 description 2
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 2
- XFWJKVMFIVXPKK-UHFFFAOYSA-N calcium;oxido(oxo)alumane Chemical compound [Ca+2].[O-][Al]=O.[O-][Al]=O XFWJKVMFIVXPKK-UHFFFAOYSA-N 0.000 description 2
- 238000011049 filling Methods 0.000 description 2
- 239000006028 limestone Substances 0.000 description 2
- 239000007791 liquid phase Substances 0.000 description 2
- 239000000395 magnesium oxide Substances 0.000 description 2
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 2
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 2
- 238000004537 pulping Methods 0.000 description 2
- 239000003469 silicate cement Substances 0.000 description 2
- 235000012239 silicon dioxide Nutrition 0.000 description 2
- 230000009466 transformation Effects 0.000 description 2
- 239000005995 Aluminium silicate Substances 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 238000007605 air drying Methods 0.000 description 1
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 description 1
- 235000012211 aluminium silicate Nutrition 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 239000000378 calcium silicate Substances 0.000 description 1
- 229910052918 calcium silicate Inorganic materials 0.000 description 1
- OYACROKNLOSFPA-UHFFFAOYSA-N calcium;dioxido(oxo)silane Chemical compound [Ca+2].[O-][Si]([O-])=O OYACROKNLOSFPA-UHFFFAOYSA-N 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- GUJOJGAPFQRJSV-UHFFFAOYSA-N dialuminum;dioxosilane;oxygen(2-);hydrate Chemical compound O.[O-2].[O-2].[O-2].[Al+3].[Al+3].O=[Si]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O GUJOJGAPFQRJSV-UHFFFAOYSA-N 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 150000004683 dihydrates Chemical class 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 229910001653 ettringite Inorganic materials 0.000 description 1
- 239000010881 fly ash Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 229910052602 gypsum Inorganic materials 0.000 description 1
- 239000010440 gypsum Substances 0.000 description 1
- 238000003837 high-temperature calcination Methods 0.000 description 1
- 229910052900 illite Inorganic materials 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 229910052901 montmorillonite Inorganic materials 0.000 description 1
- VGIBGUSAECPPNB-UHFFFAOYSA-L nonaaluminum;magnesium;tripotassium;1,3-dioxido-2,4,5-trioxa-1,3-disilabicyclo[1.1.1]pentane;iron(2+);oxygen(2-);fluoride;hydroxide Chemical compound [OH-].[O-2].[O-2].[O-2].[O-2].[O-2].[F-].[Mg+2].[Al+3].[Al+3].[Al+3].[Al+3].[Al+3].[Al+3].[Al+3].[Al+3].[Al+3].[K+].[K+].[K+].[Fe+2].O1[Si]2([O-])O[Si]1([O-])O2.O1[Si]2([O-])O[Si]1([O-])O2.O1[Si]2([O-])O[Si]1([O-])O2.O1[Si]2([O-])O[Si]1([O-])O2.O1[Si]2([O-])O[Si]1([O-])O2.O1[Si]2([O-])O[Si]1([O-])O2.O1[Si]2([O-])O[Si]1([O-])O2 VGIBGUSAECPPNB-UHFFFAOYSA-L 0.000 description 1
- 230000006911 nucleation Effects 0.000 description 1
- 238000010899 nucleation Methods 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 229920005646 polycarboxylate Polymers 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
- 235000019353 potassium silicate Nutrition 0.000 description 1
- 238000011085 pressure filtration Methods 0.000 description 1
- 239000010453 quartz Substances 0.000 description 1
- 150000005837 radical ions Chemical class 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 1
- 238000003892 spreading Methods 0.000 description 1
- 230000007480 spreading Effects 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000008030 superplasticizer Substances 0.000 description 1
- 238000002411 thermogravimetry Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000002023 wood Substances 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
- C04B12/00—Cements not provided for in groups C04B7/00 - C04B11/00
- C04B12/005—Geopolymer cements, e.g. reaction products of aluminosilicates with alkali metal hydroxides or silicates
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Organic Chemistry (AREA)
- Curing Cements, Concrete, And Artificial Stone (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
本发明涉及市政工程及建筑材料技术领域,具体涉及一种辅助胶凝材料及其制备方法和应用。该辅助胶凝材料包括闪烧粘土和矿化再生微粉;闪烧粘土的制备方法包括将工程弃土经制浆、压滤后得泥饼,将泥饼依次进行湿法过滤、离心、干燥和粉磨,得粘土粉末,再将粘土粉末进行煅烧;矿化再生微粉的制备方法包括将再生微粉经半干法矿化再经干燥、粉磨得矿化再生微粉,其中半干法矿化的具体步骤包括:向平摊开的再生微粉表面喷洒氢氧化钠溶液进行润湿,然后置于相对湿度为80%RH~100%RH的环境中进行矿化。该辅助胶凝材料可以大比例替代普通硅酸盐水泥,且制备方法耗能低、用时短、效率高。The invention relates to the technical field of municipal engineering and building materials, in particular to an auxiliary gelling material and its preparation method and application. The auxiliary gelling material includes flash-fired clay and mineralized regenerated micropowder; the preparation method of the flash-fired clay includes slurrying and pressing the engineering spoil to obtain a mud cake, and performing wet filtration, centrifugation, drying and drying of the mud cake in sequence. Grinding to obtain clay powder, and then calcining the clay powder; the preparation method of mineralized regenerated micropowder includes mineralizing regenerated micropowder through semi-dry method and then drying and grinding to obtain mineralized regenerated micropowder, wherein semi-dry method mineralized The specific steps include: spraying sodium hydroxide solution on the flat surface of the regenerated micropowder for wetting, and then placing it in an environment with a relative humidity of 80%RH to 100%RH for mineralization. The auxiliary cementitious material can replace ordinary portland cement in a large proportion, and the preparation method has low energy consumption, short time consumption and high efficiency.
Description
技术领域technical field
本发明涉及市政工程及建筑材料技术领域,具体涉及一种辅助胶凝材料及其制备方法和应用。The invention relates to the technical field of municipal engineering and building materials, in particular to an auxiliary gelling material and its preparation method and application.
背景技术Background technique
城市群人口的持续快速增长导致对居住和交通基础设施的需求与日俱增,仅深圳市各类建筑及市政工程每年产生的工程弃土就接近1亿吨,因此,对工程弃土的处置与消纳日益成为建设“无废城市”的瓶颈问题。目前工程弃土的资源化利用多以水泥或水玻璃为粘合剂、以工程弃土为填充料制备建筑材料。The continuous and rapid growth of the population of the urban agglomeration has led to an increasing demand for residential and transportation infrastructure. The engineering spoils generated by various buildings and municipal projects in Shenzhen alone are close to 100 million tons every year. Therefore, the disposal and consumption of engineering spoils It has increasingly become a bottleneck in the construction of "zero waste cities". At present, the resource utilization of engineering spoils mostly uses cement or water glass as a binder and engineering spoils as fillers to prepare building materials.
城市建设除了会产生大量工程弃土之外,还会产生大量建筑物的拆除物料,部分拆除物料可回收生产再生骨料,但在生产再生骨料的过程中会产生重量占比约10%~20%的副产品再生微粉,目前对再生微粉的资源化利用与工程弃土类似,多作为填充料使用。In addition to a large amount of engineering spoils, urban construction will also produce a large amount of building demolition materials. Some of the demolition materials can be recycled to produce recycled aggregates, but in the process of producing recycled aggregates, the weight of recycled aggregates will account for about 10%~ 20% of the by-product is recycled micropowder. Currently, the resource utilization of recycled micropowder is similar to that of engineering spoil, and it is mostly used as a filling material.
当前,工程弃土除作为填充料之外,还有通过煅烧工程弃土并将其作为水泥混合材料的现有技术,但采用的煅烧工艺耗时长、能耗高。同样地,对于再生微粉,除作为填充料使用之外,还存在通过二氧化碳矿化再生微粉并将其作为单纯的固碳材料、水泥混合材或混凝土的掺合料的应用。目前公开的二氧化碳矿化再生微粉多采用干法矿化或湿法矿化,但由于矿化反应过程既涉及气体在粉体表面的扩散,又涉及气体与粉体通过媒介水发生的反应,因此干法矿化的效率较低,而湿法矿化在搅拌过程中所需的能耗较高。尽管矿化再生微粉的火山灰活性高于石灰石的火山灰活性,但如果仅以矿化再生微粉作为水泥混合材,其性能仍低于目前普遍采用的以粒化高炉矿渣粉或粉煤灰制备的水泥混合材。At present, in addition to being used as a filler, there is an existing technology of calcining engineering spoil and using it as a cement mixture, but the calcination process is time-consuming and energy-intensive. Likewise, for recycled micropowder, in addition to being used as a filler, there are applications of regenerated micropowder mineralized by carbon dioxide and used as a pure carbon-fixing material, cement admixture, or concrete admixture. Currently disclosed carbon dioxide mineralization regenerated micropowder mostly adopts dry mineralization or wet mineralization, but because the mineralization reaction process involves both the diffusion of gas on the surface of the powder and the reaction between gas and powder through the medium water, so Dry mineralization is less efficient, while wet mineralization requires higher energy consumption during agitation. Although the pozzolanic activity of mineralized regenerated micropowder is higher than that of limestone, if only mineralized regenerated micropowder is used as a cement mixture, its performance is still lower than that of cement prepared from granulated blast furnace slag powder or fly ash commonly used at present. Mixed wood.
发明内容Contents of the invention
针对以上技术问题,本发明提供一种辅助胶凝材料及其制备方法和应用,该辅助胶凝材料的抗压强度良好,可代替部分水泥的使用,制备方法耗能低、用时短、效率高。In view of the above technical problems, the present invention provides an auxiliary cementitious material and its preparation method and application. The auxiliary cementitious material has good compressive strength and can replace part of the use of cement. The preparation method has low energy consumption, short time consumption and high efficiency .
为解决上述技术问题,本发明采用如下技术方案:In order to solve the problems of the technologies described above, the present invention adopts the following technical solutions:
本发明提供一种辅助胶凝材料,包括闪烧粘土和矿化再生微粉;The invention provides an auxiliary gelling material, including flash fired clay and mineralized regenerated micropowder;
所述闪烧粘土的制备方法具体包括:将工程弃土经制浆、压滤得泥饼,将所述泥饼依次进行湿法过滤、离心、干燥和粉磨,得粘土粉末,将所述粘土粉末在空气中以悬浮态进行煅烧得闪烧粘土,所述煅烧的温度为850℃~950℃,煅烧的时间为0.5s~1.5s;The preparation method of the flash-fired clay specifically comprises: pulping and press-filtering the engineering spoil to obtain a mud cake, and sequentially performing wet filtration, centrifugation, drying and grinding on the mud cake to obtain clay powder, and The clay powder is calcined in a suspended state in air to obtain flash-fired clay, the temperature of the calcination is 850°C-950°C, and the calcination time is 0.5s-1.5s;
所述矿化再生微粉的制备方法具体包括:将再生微粉经半干法矿化,再经干燥、粉磨得矿化再生微粉,所述半干法矿化的具体步骤包括:向平摊开的所述再生微粉表面喷洒氢氧化钠溶液进行润湿,然后置于相对湿度为80%RH~100%RH的环境中进行矿化。The preparation method of the mineralized regenerated micropowder specifically includes: mineralizing the regenerated micropowder through a semi-dry method, and then drying and grinding to obtain a mineralized regenerated micropowder. The specific steps of the semidry method mineralization include: The surface of the regenerated fine powder is sprayed with sodium hydroxide solution for wetting, and then placed in an environment with a relative humidity of 80%RH to 100%RH for mineralization.
本发明中制备闪烧粘土所用的泥饼由粘土和石英砂构成,因粘土矿物的粒径普遍小于石英砂的粒径,因此采用湿法过滤可尽可能地将石英砂除去,将粘土矿物尽可能多地过滤至滤液中,以提高粘土矿物在滤液离心后所得细颗粒物沉淀中的比重。所得粘土粉末中包含高岭石、伊利石、蒙脱石、石英等矿物,主要有效成分为高岭石,高温煅烧可使高岭石去羟基化,形成具有无定形结构的偏高岭土。并且,本发明提供的闪烧粘土的制备方法中,将粘土粉末在空气中以悬浮态进行煅烧,增大了粘土粉末的比表面积,使煅烧效率得以提高,且所用的煅烧时间与现有技术相比显著缩短,与现有技术的煅烧方式相比,不仅提高了制备效率,也更加节能。In the present invention, the mud cake used to prepare the flash clay is made of clay and quartz sand. Because the particle diameter of clay minerals is generally smaller than that of quartz sand, the quartz sand can be removed as much as possible by wet filtration, and the clay minerals can be removed as much as possible. It is possible to filter as much as possible into the filtrate to increase the specific gravity of clay minerals in the fine particulate matter precipitate obtained after centrifugation of the filtrate. The obtained clay powder contains minerals such as kaolinite, illite, montmorillonite, quartz and the like, and the main active ingredient is kaolinite. High-temperature calcination can dehydroxylate the kaolinite to form metakaolin with an amorphous structure. Moreover, in the method for preparing flash-fired clay provided by the present invention, the clay powder is calcined in a suspended state in the air, which increases the specific surface area of the clay powder and improves the calcining efficiency, and the calcining time used is the same as that of the prior art Compared with the calcination method of the prior art, it not only improves the preparation efficiency, but also saves energy.
本发明中制备矿化再生微粉所用的再生微粉是利用拆建物料生产再生骨料过程中的副产品,主要由硬化水泥浆构成,主要成分包括少量未水化水泥颗粒、羟钙石、水化铝硅酸钙凝胶、钙矾石、单硫型水化铝酸钙等。在二氧化碳矿化过程中,羟钙石转变为碳酸钙,其它组分脱钙形成铝硅酸凝胶,铝硅酸凝胶具有火山灰活性;碳酸钙不仅参与水化反应,还提供成核位点,起到加速水泥水化反应的作用。本发明提供的矿化再生微粉的制备方法采用半干法进行矿化,由于液相氢氧化钠溶液的存在,加速了二氧化碳在液相中的溶解,与干法矿化相比效率更高;而且,由于氢氧化钠溶液采用的是喷洒方式,因此再生微粉表面的液体量相对于湿法矿化更少,二氧化碳更容易在再生微粉的表面间扩散,而且无需湿法矿化过程中的持续搅拌操作,所需能耗更低。The regenerated micropowder used in the preparation of mineralized regenerated micropowder in the present invention is a by-product in the process of producing recycled aggregates from construction and demolition materials. It is mainly composed of hardened cement slurry, and its main components include a small amount of unhydrated cement particles, hydroxycalcite, and aluminum hydrate. Calcium silicate gel, ettringite, monosulfide calcium aluminate hydrate, etc. During the mineralization process of carbon dioxide, hexasite is transformed into calcium carbonate, and other components are decalcified to form aluminosilicate gel, which has pozzolanic activity; calcium carbonate not only participates in the hydration reaction, but also provides nucleation sites , to accelerate the cement hydration reaction. The preparation method of the mineralized regenerated micropowder provided by the present invention adopts a semi-dry method for mineralization. Due to the existence of liquid phase sodium hydroxide solution, the dissolution of carbon dioxide in the liquid phase is accelerated, and the efficiency is higher compared with dry mineralization; Moreover, because the sodium hydroxide solution is sprayed, the amount of liquid on the surface of the regenerated micro-powder is less than that of wet mineralization, and carbon dioxide is more likely to diffuse between the surfaces of the regenerated micro-powder, and there is no need for a continuous process of wet mineralization. Stirring operation requires less energy consumption.
结合第一方面,所述泥饼中颗粒的粒径小于2.36mm,此粒径以下可使构成泥饼的颗粒物得以快速分散。In combination with the first aspect, the particle size of the mud cake is less than 2.36 mm, and the particles constituting the mud cake can be quickly dispersed below this particle size.
结合第一方面,所述湿法过滤、离心、干燥和粉磨的具体步骤为:将所述泥饼与水按照1:20~50的质量比混合均匀后,使用孔径不大于25μm的筛网过滤并收集滤液,再将所得滤液离心并收集下层细颗粒物沉淀;将所述细颗粒物沉淀风干至含水率小于5%,之后进行粉磨、过筛,得粘土粉末,过筛的孔径为75μm。In combination with the first aspect, the specific steps of wet filtration, centrifugation, drying and grinding are as follows: after uniformly mixing the mud cake and water at a mass ratio of 1:20-50, use a sieve with a pore size not greater than 25 μm Filtrate and collect the filtrate, then centrifuge the obtained filtrate and collect the fine particle precipitate in the lower layer; air-dry the fine particle precipitate until the water content is less than 5%, and then grind and sieve to obtain clay powder with a sieved aperture of 75 μm.
结合第一方面,所述半干法矿化的具体步骤包括:将所述再生微粉按照平摊后厚度不大于1mm的标准摊开,按照固液质量比0.01~0.1的比例,将氢氧化钠溶液均匀喷洒在平摊开的再生微粉表面使其润湿,再将润湿后的再生微粉置于二氧化碳浓度为10%~30%、温度为20℃~30℃、相对湿度为80%RH~90%RH的环境中进行矿化,矿化时间不低于1h。In combination with the first aspect, the specific steps of the semi-dry method of mineralization include: spreading the regenerated fine powder according to the standard that the thickness of the regenerated micropowder is not greater than 1mm after being flattened, and adding sodium hydroxide The solution is evenly sprayed on the surface of the regenerated micropowder spread out to make it wet, and then the wetted regenerated micropowder is placed in a carbon dioxide concentration of 10%~30%, a temperature of 20°C~30°C, and a relative humidity of 80%RH~ Mineralization is carried out in an environment of 90% RH, and the mineralization time is not less than 1h.
优选地,矿化温度为20℃~25℃,矿化时间为1h~3h,该矿化时间可以保证矿化反应的充分进行。Preferably, the mineralization temperature is 20° C. to 25° C., and the mineralization time is 1 h to 3 h. The mineralization time can ensure that the mineralization reaction is fully carried out.
结合第一方面,所述氢氧化钠溶液的浓度为3g/L~5g/L。In combination with the first aspect, the concentration of the sodium hydroxide solution is 3g/L-5g/L.
结合第一方面,所述闪烧粘土和所述矿化再生微粉的质量比为1.5~2.2:1,优选为2:1,通过调整闪烧粘土和矿化再生微粉在辅助胶凝材料中的质量占比,可满足辅助胶凝材料在不同的应用中对性能的不同要求。In combination with the first aspect, the mass ratio of the flash-fired clay and the mineralized regenerated fine powder is 1.5-2.2:1, preferably 2:1, by adjusting the ratio of the flash-fired clay and the mineralized regenerated fine powder in the auxiliary The mass ratio can meet the different performance requirements of auxiliary cementitious materials in different applications.
本发明的第二方面提供一种辅助胶凝材料的制备方法,按照上述闪烧粘土的制备方法和矿化再生微粉的制备方法分别制备闪烧粘土和矿化再生微粉,将所得闪烧粘土和矿化再生微粉按1.5~2.2:1的质量比混合,即得。The second aspect of the present invention provides a method for preparing an auxiliary gelling material. According to the preparation method of the above-mentioned flash-fired clay and the preparation method of the mineralized regenerated micro-powder, the flash-fired clay and the mineralized regenerated micro-powder are respectively prepared, and the obtained flash-fired clay and the regenerated mineralized powder are prepared respectively. Mineralized regenerated micropowder is mixed according to the mass ratio of 1.5-2.2:1.
该制备方法包括闪烧粘土的制备和矿化再生微粉的制备,其中闪烧粘土的制备方法通过对煅烧温度和煅烧时间的控制,有效提高了煅烧效率,并形成了具有无定形结构的偏高岭土;矿化再生微粉的制备方法无需进行长时间搅拌,操作简单,耗能更低。The preparation method includes the preparation of flash-fired clay and the preparation of mineralized regenerated micropowder, wherein the preparation method of flash-fired clay effectively improves the calcination efficiency by controlling the calcination temperature and calcination time, and forms metakaolin with an amorphous structure ; The preparation method of the mineralized regenerated micropowder does not need to be stirred for a long time, the operation is simple, and the energy consumption is lower.
本发明的第三方面提供一种上述辅助胶凝材料在胶凝材料中的应用,将该辅助胶凝材料用于胶凝材料的制备中,获得的胶凝材料的抗压强度与普通硅酸盐水泥的抗压强度相当。The third aspect of the present invention provides a kind of application of above-mentioned auxiliary gelling material in cementitious material, this auxiliary gelling material is used in the preparation of cementitious material, the compressive strength of the obtained cementitious material is comparable to ordinary silicic acid The compressive strength of salt cement is comparable.
结合第三方面,所述胶凝材料还包括水泥。With reference to the third aspect, the cementitious material further includes cement.
结合第三方面,所述胶凝材料中水泥的质量占比为45%~60%。In combination with the third aspect, the mass proportion of cement in the cementitious material is 45%-60%.
在包含该辅助胶凝材料和水泥的胶凝材料中,辅助胶凝材料中闪烧粘土的主要活性成分为具有无定形结构的偏高岭土,在碱性条件下能溶出水合铝酸根离子和水合硅酸根离子,与水泥中溶出的钙离子反应生成水化铝硅酸钙凝胶;辅助胶凝材料中矿化再生微粉中的主要活性成分为纳米碳酸钙,以及水化铝硅酸钙脱钙形成的铝硅酸凝胶,铝硅酸凝胶与水泥中的钙离子反应,再度生成水化铝硅酸钙凝胶;纳米碳酸钙溶出的碳酸根离子可与水泥中的钙离子、水泥或偏高岭土中溶出的水合铝酸根离子反应,生成半碳及单碳型水化铝酸钙。因而,辅助胶凝材料含有的闪烧粘土与矿化再生微粉的主要活性成分在水泥水化反应中具有一定的协同作用。In the cementitious material comprising the auxiliary cementitious material and cement, the main active ingredient of the flash clay in the auxiliary cementitious material is metakaolin with an amorphous structure, which can dissolve hydrated aluminate ions and hydrated silicon under alkaline conditions. Acid radical ions react with calcium ions dissolved in cement to form calcium aluminosilicate hydrate gel; the main active ingredient in the mineralized regenerated micropowder in the auxiliary cementitious material is nano-calcium carbonate, which is formed by decalcification of calcium aluminosilicate hydrate The aluminosilicate gel, the aluminosilicate gel reacts with the calcium ions in the cement to generate calcium aluminosilicate hydrate gel again; The hydrated aluminate ion dissolved in kaolin reacts to form half-carbon and single-carbon calcium aluminate hydrate. Therefore, the flash-fired clay contained in the auxiliary cementitious material and the main active ingredient of the mineralized regenerated micropowder have a certain synergistic effect in the cement hydration reaction.
本发明的有益效果在于:本发明提供的辅助胶凝材料的制备方法用时短、耗能低、效率高,可以在短时间和低能耗的条件下完成闪烧粘土和矿化再生微粉的制备,所得辅助胶凝材料应用于胶凝材料时,由该辅助胶凝材料和普通水泥混合得到的复合水泥的性能与普通硅酸盐水泥的性能相当,因此该辅助胶凝材料可以大比例替代普通硅酸盐水泥的使用;并且通过调节该辅助胶凝材料中闪烧粘土和矿化再生微粉的比例还能平抑来源复杂的工程弃土和拆建物料导致的复合水泥的性能波动。The beneficial effects of the present invention are: the preparation method of the auxiliary gelling material provided by the present invention is short in time, low in energy consumption and high in efficiency, and can complete the preparation of flash fired clay and mineralized regenerated micropowder in a short time and low in energy consumption. When the obtained auxiliary cementitious material is applied to cementitious materials, the performance of the composite cement obtained by mixing the auxiliary cementitious material with ordinary cement is equivalent to that of ordinary Portland cement, so the auxiliary cementitious material can replace ordinary silicate cement in a large proportion. The use of salt cement; and by adjusting the ratio of flash-fired clay and mineralized regenerated micropowder in the auxiliary cementitious material, it can also stabilize the performance fluctuation of the composite cement caused by engineering spoils and demolition materials with complex sources.
具体实施方式Detailed ways
为了使本发明的目的、技术方案及优点更加清楚明白,以下结合具体实施例,对本发明进行进一步详细说明。应当理解,此处所描述的具体实施例仅仅用于解释本发明,并不用于限定本发明。In order to make the object, technical solution and advantages of the present invention clearer, the present invention will be further described in detail below in conjunction with specific embodiments. It should be understood that the specific embodiments described here are only used to explain the present invention, not to limit the present invention.
本发明实施例和对比例中使用的工程弃土来自深圳市南山区的某建筑工地,经脱水、制浆、压滤成泥饼,经孔径为2mm的筛网压滤,风干,风干后泥饼的化学组成以氧化物重量计如下:The engineering spoil used in the embodiment of the present invention and comparative example comes from a certain construction site in Nanshan District, Shenzhen City. After dehydration, pulping, and pressure filtration, it becomes a mud cake, and through a sieve with an aperture of 2mm, it is air-dried, and the mud after air-drying The chemical composition of the cake is as follows on an oxide weight basis:
。.
本发明实施例和对比例中使用的再生微粉,是在利用拆建物料生产再生骨料过程中由粒径小于2.36mm的再生细骨料经75μm的筛网筛分获得,再生微粉的化学组成以氧化物重量计如下:The regenerated micropowder used in the examples and comparative examples of the present invention is obtained by sieving the regenerated fine aggregate with a particle size of less than 2.36 mm through a 75 μm sieve in the process of producing recycled aggregates from construction and demolition materials. The chemical composition of the regenerated micropowder Calculated by oxide weight as follows:
。.
本发明实施例和对比例中使用的水泥为纯硅酸盐水泥,由P·I 42.5R等级的水泥熟料与二水石膏混磨而成,其化学组成以氧化物重量计如下:The cement used in the embodiments of the present invention and comparative examples is pure Portland cement, which is formed by mixing cement clinker and dihydrate gypsum of P·I 42.5R grade, and its chemical composition is as follows in terms of oxide weight:
。.
本发明实施例和对比例中使用的氢氧化钠为分析纯,纯度≥96%;二氧化碳气体为高纯度气体,纯度为99.99%;压缩空气为高纯度空气,纯度为99.999%;减水剂为聚羧酸盐减水剂。The sodium hydroxide used in the embodiment of the present invention and the comparative example is analytically pure, and the purity is ≥ 96%; the carbon dioxide gas is a high-purity gas, and the purity is 99.99%; the compressed air is high-purity air, and the purity is 99.999%; Polycarboxylate superplasticizer.
实施例1Example 1
本实施例提供一种辅助胶凝材料闪烧粘土的制备方法,具体步骤如下:This embodiment provides a method for preparing auxiliary cementitious material flash-fired clay, and the specific steps are as follows:
(1)将已风干的泥饼与水以1∶35的质量比混合均匀,制得颗粒物充分分散的泥浆;(1) Mix the air-dried mud cake and water evenly at a mass ratio of 1:35 to obtain a slurry in which the particles are fully dispersed;
(2)将泥浆通过孔径为25μm的筛网进行过滤,得到滤液;(2) filter the mud through a sieve with an aperture of 25 μm to obtain a filtrate;
(3)将滤液在离心机中以1000g的重力加速度离心10分钟,排出上层清液,得到细颗粒物沉淀;(3) The filtrate is centrifuged for 10 minutes with a gravitational acceleration of 1000g in a centrifuge, and the supernatant is discharged to obtain fine particle precipitation;
(4)将细颗粒物沉淀在自然条件下风干至含水率小于5%,粉磨并通过75μm的筛网,得到粘土粉末;(4) Air-dry the fine particles precipitated under natural conditions until the water content is less than 5%, grind and pass through a 75 μm sieve to obtain clay powder;
(5)将粘土粉末与压缩空气混合,从立式管式炉顶部喷入,粘土粉末以悬浮状态分散,炉内温度设置为900℃,煅烧1.0s,即得闪烧粘土。(5) Mix the clay powder with compressed air and spray it in from the top of the vertical tube furnace. The clay powder is dispersed in a suspended state. The temperature in the furnace is set at 900°C and calcined for 1.0s to obtain the flash fired clay.
实施例2Example 2
本实施例提供一种辅助胶凝材料闪烧粘土的制备方法,具体步骤如下:This embodiment provides a method for preparing auxiliary cementitious material flash-fired clay, and the specific steps are as follows:
(1)将已风干的泥饼与水以1:20的质量比混合均匀,制得颗粒物充分分散的泥浆;(1) Mix the air-dried mud cake and water evenly at a mass ratio of 1:20 to obtain a slurry in which the particles are fully dispersed;
(2)将泥浆通过孔径为25μm的筛网进行过滤,得到滤液;(2) filter the mud through a sieve with an aperture of 25 μm to obtain a filtrate;
(3)将滤液在离心机中以1000g的重力加速度离心15分钟,排出上层清液,得到细颗粒物沉淀;(3) The filtrate was centrifuged for 15 minutes with a gravitational acceleration of 1000g in a centrifuge, and the supernatant was discharged to obtain fine particle precipitation;
(4)将细颗粒物沉淀在自然条件下风干至含水率小于5%,粉磨并通过75μm的筛网,得到粘土粉末;(4) Air-dry the fine particles precipitated under natural conditions until the water content is less than 5%, grind and pass through a 75 μm sieve to obtain clay powder;
(5)将粘土粉末与压缩空气混合,从立式管式炉顶部喷入,粘土粉末以悬浮状态分散,炉内温度设置为850℃,煅烧0.5s,即得闪烧粘土。(5) Mix the clay powder with compressed air and spray it in from the top of the vertical tube furnace. The clay powder is dispersed in a suspended state. The temperature in the furnace is set at 850°C and calcined for 0.5s to obtain the flash fired clay.
实施例3Example 3
本实施例提供一种辅助胶凝材料闪烧粘土的制备方法,具体步骤如下:This embodiment provides a method for preparing auxiliary cementitious material flash-fired clay, and the specific steps are as follows:
(1)将已风干的泥饼与水以1:50的质量比混合均匀,制得颗粒物充分分散的泥浆;(1) Mix the air-dried mud cake and water evenly at a mass ratio of 1:50 to obtain a slurry in which the particles are fully dispersed;
(2)将泥浆通过孔径为25μm的筛网进行过滤,得到滤液;(2) filter the mud through a sieve with an aperture of 25 μm to obtain a filtrate;
(3)将滤液在离心机中以1000g的重力加速度离心10分钟,排出上层清液,得到细颗粒物沉淀;(3) The filtrate is centrifuged for 10 minutes with a gravitational acceleration of 1000g in a centrifuge, and the supernatant is discharged to obtain fine particle precipitation;
(4)将细颗粒物沉淀在自然条件下风干至含水率小于5%,粉磨并通过75μm的筛网,得到粘土粉末;(4) Air-dry the fine particles precipitated under natural conditions until the water content is less than 5%, grind and pass through a 75 μm sieve to obtain clay powder;
(5)将粘土粉末与压缩空气混合,从立式管式炉顶部喷入,粘土粉末以悬浮状态分散,炉内温度设置为950℃,煅烧1.5s,即得闪烧粘土。(5) Mix the clay powder with compressed air and spray it in from the top of the vertical tube furnace. The clay powder is dispersed in a suspended state. The temperature in the furnace is set at 950°C and calcined for 1.5s to obtain the flash fired clay.
实施例4Example 4
本实施例提供一种辅助胶凝材料矿化再生微粉的制备方法,具体步骤如下:This embodiment provides a preparation method of auxiliary gelling material mineralization regenerated micropowder, the specific steps are as follows:
(1)将经75μm的筛网筛分获得的再生微粉在不锈钢托盘中摊平,粉末厚度为1mm;(1) Flatten the regenerated micropowder obtained by sieving through a 75 μm sieve in a stainless steel tray, and the powder thickness is 1mm;
(2)将4g/L的氢氧化钠水溶液按照固液质量比0.05:1的比例均匀喷洒在已平摊开的再生微粉表面使其润湿;(2) Spray 4g/L sodium hydroxide aqueous solution evenly on the surface of the regenerated micropowder that has been spread out to make it wet according to the ratio of solid to liquid mass ratio of 0.05:1;
(3)将润湿后的再生微粉置于二氧化碳浓度为20%,温度为25℃,相对湿度为90%RH的环境中反应2小时;(3) Place the wetted regenerated micropowder in an environment where the carbon dioxide concentration is 20%, the temperature is 25° C., and the relative humidity is 90% RH, and reacts for 2 hours;
(4)将反应完毕的再生微粉在自然条件下风干至含水率小于5%,研磨并通过75μm的筛网,得矿化再生微粉。(4) Air-dry the reacted regenerated micropowder under natural conditions until the moisture content is less than 5%, grind and pass through a 75 μm sieve to obtain mineralized regenerated micropowder.
实施例5Example 5
本实施例提供一种辅助胶凝材料矿化再生微粉的制备方法,具体步骤如下:This embodiment provides a preparation method of auxiliary gelling material mineralization regenerated micropowder, the specific steps are as follows:
(1)将经75μm的筛网筛分获得的再生微粉在不锈钢托盘中摊平,粉末厚度为0.8mm;(1) Flatten the regenerated micropowder obtained by sieving through a 75 μm sieve in a stainless steel tray, and the powder thickness is 0.8mm;
(2)将3g/L的氢氧化钠水溶液按照固液质量比0.01:1的比例均匀喷洒在已平摊开的再生微粉表面使其润湿;(2) Spray 3g/L sodium hydroxide aqueous solution evenly on the surface of the regenerated micropowder that has been spread out to make it wet according to the ratio of solid to liquid mass ratio of 0.01:1;
(3)将润湿后的再生微粉置于二氧化碳浓度为10%,温度为20℃,相对湿度为80%RH的环境中反应1小时;(3) Place the wetted regenerated micropowder in an environment with a carbon dioxide concentration of 10%, a temperature of 20° C., and a relative humidity of 80% RH for 1 hour;
(4)将反应完毕的再生微粉在自然条件下风干至含水率小于5%,研磨并通过75μm的筛网,得矿化再生微粉。(4) Air-dry the reacted regenerated micropowder under natural conditions until the moisture content is less than 5%, grind and pass through a 75 μm sieve to obtain mineralized regenerated micropowder.
实施例6Example 6
本实施例提供一种辅助胶凝材料矿化再生微粉的制备方法,具体步骤如下:This embodiment provides a preparation method of auxiliary gelling material mineralization regenerated micropowder, the specific steps are as follows:
(1)将经75μm的筛网筛分获得的再生微粉在不锈钢托盘中摊平,粉末厚度为1.0mm;(1) Flatten the regenerated micropowder obtained by sieving through a 75 μm sieve in a stainless steel tray, and the powder thickness is 1.0mm;
(2)将5g/L的氢氧化钠水溶液按照固液质量比0.1:1的比例均匀喷洒在已平摊开的再生微粉表面使其润湿;(2) Spray 5g/L sodium hydroxide aqueous solution evenly on the surface of the regenerated micropowder that has been spread out to make it wet according to the ratio of solid to liquid mass ratio of 0.1:1;
(3)将润湿后的再生微粉置于二氧化碳浓度为30%,温度为30℃,相对湿度为100%RH的环境中反应3小时;(3) Place the wetted regenerated micropowder in an environment where the carbon dioxide concentration is 30%, the temperature is 30° C., and the relative humidity is 100% RH, and reacts for 3 hours;
(4)将反应完毕的再生微粉在自然条件下风干至含水率小于5%,研磨并通过75μm的筛网,得矿化再生微粉。(4) Air-dry the reacted regenerated micropowder under natural conditions until the moisture content is less than 5%, grind and pass through a 75 μm sieve to obtain mineralized regenerated micropowder.
实施例7Example 7
本实施例提供一种由实施例1制得的闪烧粘土和实施例4制得的矿化再生微粉组成的辅助胶凝材料及其在胶凝材料中的应用,辅助胶凝材料和胶凝材料的组分配比如表1所示。This embodiment provides an auxiliary gelling material composed of the flash fired clay prepared in Example 1 and the mineralized regenerated micropowder prepared in Example 4 and its application in gelling materials, auxiliary gelling material and gelling The composition ratio of the materials is shown in Table 1.
实施例8Example 8
本实施例提供一种由实施例2制得的闪烧粘土和实施例5制得的矿化再生微粉组成的辅助胶凝材料及其在胶凝材料中的应用,辅助胶凝材料和胶凝材料的组分配比如表1所示。This embodiment provides an auxiliary gelling material composed of the flash-fired clay obtained in Example 2 and the mineralized regenerated micropowder prepared in Example 5 and its application in gelling materials, auxiliary gelling material and gelling The composition ratio of the materials is shown in Table 1.
实施例9Example 9
本实施例提供一种由实施例3制得的闪烧粘土和实施例6制得的矿化再生微粉组成的辅助胶凝材料及其在胶凝材料中的应用,辅助胶凝材料和胶凝材料的组分配比如表1所示。This embodiment provides an auxiliary gelling material composed of the flash-fired clay prepared in Example 3 and the mineralized regenerated micropowder prepared in Example 6 and its application in gelling materials, auxiliary gelling material and gelling The composition ratio of the materials is shown in Table 1.
实施例10~12Examples 10-12
本实施例提供一种由实施例1制得的闪烧粘土和实施例4制得的矿化再生微粉组成的辅助胶凝材料及其在胶凝材料中的应用,辅助胶凝材料和胶凝材料的组分配比如表1所示。This embodiment provides an auxiliary gelling material composed of the flash fired clay prepared in Example 1 and the mineralized regenerated micropowder prepared in Example 4 and its application in gelling materials, auxiliary gelling material and gelling The composition ratio of the materials is shown in Table 1.
对比例1Comparative example 1
本对比例提供一种闪烧粘土的制备方法,具体步骤与实施例1相似,区别仅在于粘土粉末的煅烧条件为在800℃下煅烧2小时。This comparative example provides a method for preparing flash-fired clay. The specific steps are similar to those in Example 1, except that the clay powder is calcined at 800° C. for 2 hours.
对比例2Comparative example 2
本对比例提供一种干法矿化再生微粉的制备方法,具体步骤如下:将再生微粉在不锈钢托盘中摊平,粉末厚度为1.0mm,将其置于二氧化碳浓度为20%,温度为25℃,相对湿度为60%RH的环境中反应2小时,得干法矿化再生微粉。This comparative example provides a preparation method of dry mineralized regenerated micropowder. The specific steps are as follows: flatten the regenerated micropowder in a stainless steel tray, the thickness of the powder is 1.0mm, and place it in a place where the concentration of carbon dioxide is 20% and the temperature is 25°C. , react in an environment with a relative humidity of 60% RH for 2 hours to obtain dry mineralized regenerated micropowder.
对比例3Comparative example 3
本对比例提供一种半干法矿化再生微粉的制备方法,具体步骤与实施例4相似,区别仅在于将氢氧化钠溶液替换为纯水进行喷洒,得半干法矿化再生微粉(喷水)。This comparative example provides a kind of preparation method of semi-dry method mineralized regenerated micropowder, and concrete steps are similar to embodiment 4, difference only is that sodium hydroxide solution is replaced by pure water and sprayed, obtain semidry method mineralized regenerated micropowder (spray water).
对比例4~7Comparative example 4~7
对比例4~7提供4种胶凝材料,其中对比例5所用的煅烧粘土由对比例1制得,对比例6所用的煅烧粘土和干法矿化再生微粉分别由对比例1和对比例2制得,对比例7所用的半干法矿化再生微粉(喷水)和闪烧粘土分别由对比例3和实施例2制得。对比例4~7中胶凝材料的组分配比如表1所示。Comparative Examples 4-7 provide 4 kinds of cementitious materials, wherein the calcined clay used in Comparative Example 5 is prepared from Comparative Example 1, and the calcined clay and dry mineralized regenerated micropowder used in Comparative Example 6 are prepared from Comparative Example 1 and Comparative Example 2 respectively. Prepared, semi-dry method mineralized regenerated micropowder (water spray) and flash fire clay used in Comparative Example 7 were prepared by Comparative Example 3 and Example 2 respectively. The composition ratio of the gelling material in Comparative Examples 4-7 is shown in Table 1.
表1实施例7~12和对比例4~7中胶凝材料的组分配比The component distribution ratio of the cementitious material in Table 1 embodiment 7~12 and comparative example 4~7
。 .
检验例1Test case 1
分别对实施例1~3制得的闪烧粘土和对比例1制得的煅烧粘土采取内掺20%氧化锌粉末的方式进行X射线衍射分析,结果如表2所示。X-ray diffraction analysis was carried out on the flashed clay prepared in Examples 1-3 and the calcined clay prepared in Comparative Example 1 by adding 20% zinc oxide powder, and the results are shown in Table 2.
表2实施例1~3和对比例1的X射线衍射结果The X-ray diffraction result of table 2 embodiment 1~3 and comparative example 1
。.
由表2测试结果可知,实施例1~3采用闪烧的方式,虽然由于煅烧时间短,尚不能将高岭石完全转化为偏高岭土,但闪烧的效率及能耗仍较普通煅烧有巨大优势。与实施例2相比,实施例3中的无定形物含量大幅提升,表明在一定温度和时间范围内,更高温度、更长煅烧时间有利于高岭石转化为偏高岭土。From the test results in Table 2, it can be seen that Examples 1 to 3 adopt the method of flash calcination. Although the kaolinite cannot be completely converted into metakaolin due to the short calcination time, the efficiency and energy consumption of flash calcination are still significantly higher than those of ordinary calcination. Advantage. Compared with Example 2, the amorphous content in Example 3 is greatly increased, indicating that within a certain temperature and time range, higher temperature and longer calcination time are conducive to the transformation of kaolinite into metakaolin.
检验例2Test case 2
分别对实施例4~6制得的矿化再生微粉、对比例2制得的干法矿化再生微粉和对比例3制得的半干法矿化再生微粉(喷水)进行热失重分析,结果如表3所示。Carry out thermogravimetric analysis to the mineralization regeneration micropowder that embodiment 4~6 makes, the dry mineralization regeneration micropowder that comparative example 2 makes and the semi-dry method mineralization regeneration micropowder (water spray) that comparative example 3 makes respectively, The results are shown in Table 3.
表3实施例4~6和对比例2~3的热失重结果The thermogravity result of table 3 embodiment 4~6 and comparative example 2~3
。 .
由表3测试结果可知,实施例4~6采用半干法矿化的矿化效率比对比例2采用干法矿化的矿化效率相比大幅提高,比对比例3采用纯水润湿再生微粉的半干法矿化效率也有提高,说明喷洒一定浓度的氢氧化钠溶液对再生微粉进行半干法矿化所固化的二氧化碳更多。From the test results in Table 3, it can be seen that the mineralization efficiency of Examples 4-6 using semi-dry mineralization is significantly higher than that of Comparative Example 2 using dry mineralization, and Comparative Example 3 uses pure water for wet regeneration The semi-dry mineralization efficiency of the micropowder also increased, indicating that spraying a certain concentration of sodium hydroxide solution on the regenerated micropowder for semi-dry mineralization would solidify more carbon dioxide.
与实施例5相比,实施例6中的碳酸钙含量提升,表明在一定湿度范围和矿化时间内,更高湿度、更长矿化时间有利于水泥石中的物相转变为碳酸钙。Compared with Example 5, the calcium carbonate content in Example 6 is improved, indicating that within a certain humidity range and mineralization time, higher humidity and longer mineralization time are conducive to the phase transformation of cement stones into calcium carbonate.
检验例3Test case 3
分别将实施例7~12和对比例4~7提供的胶凝材料按照水胶质量比0.35的比例与水混合制备水泥净浆,并加入占胶凝材料重量0.5%的减水剂,并分别对所得水泥净浆的力学强度进行测试,结果如表4所示。The cementitious materials provided in Examples 7-12 and Comparative Examples 4-7 were mixed with water according to the water gel mass ratio of 0.35 to prepare cement paste, and 0.5% of the cementitious material weight water reducer was added, and respectively The mechanical strength of the obtained cement slurry was tested, and the results are shown in Table 4.
表4实施例7~12和对比例4~7的凝胶材料对应的水泥净浆的力学性能The mechanical properties of the cement slurry corresponding to the gel material of Table 4 Examples 7-12 and Comparative Examples 4-7
。 .
由表4中的数据可知,实施例7~9中随着辅助胶凝材料中有效成分的提升,净浆力学性能有小幅提升。尽管如此,辅助胶凝材料的颗粒填充效应仍对强度有着较大贡献。与实施例7相比,虽然实施例10与实施例12中的水泥在胶凝材料中的比例降低导致净浆强度有所降低,但是降低了水泥的用量,而且得到的净浆强度仍可满足使用要求;实施例11的辅助胶凝材料中闪烧粘土比例的降低使净浆早期强度有所下降,表明闪烧粘土-矿化再生微粉的比例关系对其协同作用有影响。From the data in Table 4, it can be seen that in Examples 7-9, with the increase of the active ingredients in the auxiliary gelling material, the mechanical properties of the clean pulp are slightly improved. Nevertheless, the particle filling effect of auxiliary cementitious materials still has a large contribution to the strength. Compared with Example 7, although the proportion of cement in the cementitious material in Example 10 and Example 12 reduces and causes the clean slurry strength to reduce to some extent, the consumption of cement is reduced, and the clean slurry strength obtained can still satisfy Requirements for use: The reduction in the proportion of flash-fired clay in the auxiliary cementitious material of Example 11 reduces the early strength of the clean slurry, indicating that the ratio of flash-fired clay-mineralized regenerated micropowder has an impact on its synergistic effect.
另外,除实施例10以外,其余实施例与对比例4中的纯硅酸盐水泥净浆的力学性能无显著差异或略微提升,表明辅助胶凝材料制备的复合水泥在性能上与纯硅酸盐水泥相当;与对比例5的石灰石煅烧粘土水泥相比,尽管强度无显著差异,但矿化再生微粉取代了天然原材料,且制备过程固化了二氧化碳,在减少胶凝材料碳足迹方面具有优势;对比例6与对比例5相比,由于干法矿化再生微粉中有效成分较低,与煅烧粘土产生的协同效应较弱,对净浆早期强度产生较大影响;对比例7中辅助胶凝材料包含半干法矿化再生微粉(喷水),由于有效成分含量相对较低,与实施例8相比净浆早期强度有所降低。In addition, except for Example 10, the mechanical properties of the other examples and the pure Portland cement slurry in Comparative Example 4 have no significant difference or are slightly improved, indicating that the composite cement prepared by the auxiliary cementitious material is comparable in performance to that of pure silicate cement. Salt cement is equivalent; compared with the limestone calcined clay cement of Comparative Example 5, although there is no significant difference in strength, the mineralized recycled micropowder replaces the natural raw material, and the preparation process solidifies carbon dioxide, which has advantages in reducing the carbon footprint of cementitious materials; Compared with Comparative Example 6 and Comparative Example 5, due to the low active ingredient in the regenerated micropowder of dry mineralization, the synergistic effect with calcined clay is weak, which has a greater impact on the early strength of the clean slurry; in Comparative Example 7, the auxiliary gelling The material contains semi-dry mineralized regenerated micropowder (sprayed with water). Compared with Example 8, the early strength of the clean slurry is reduced due to the relatively low content of active ingredients.
经上述分析可知,本发明提供的辅助胶凝材料与水泥复合制得的胶凝材料的力学性能与以纯硅酸盐水泥作为胶凝材料的力学性能相当,说明该发明提供的辅助胶凝材料可大比例替换普通硅酸盐水泥的使用。Through the above-mentioned analysis, it can be known that the mechanical properties of the cementitious material prepared by compounding the auxiliary cementitious material provided by the present invention and cement are equivalent to the mechanical properties of the cementitious material with pure Portland cement, indicating that the auxiliary cementitious material provided by the invention can be A large proportion replaces the use of ordinary Portland cement.
以上所述的,仅为本发明较佳的具体实施方式,但本发明的保护范围并不局限于此,任何熟悉本技术领域的技术人员在本发明揭露的技术范围内,根据本发明的技术方案及其发明构思加以等同替换或改变,都应涵盖在本发明的保护范围之内。The above is only a preferred embodiment of the present invention, but the scope of protection of the present invention is not limited thereto, any person familiar with the technical field within the technical scope disclosed in the present invention, according to the technology of the present invention Any equivalent replacement or change of the scheme and its inventive concepts shall fall within the protection scope of the present invention.
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