Patent Application
20240360034
This application claims the benefit of priority from Chinese Patent Application No. 202410204516.1, filed on Feb. 24, 2024. The content of the aforementioned application, including any intervening amendments made thereto, is incorporated herein by reference in its entirety.
This application relates to cement-type building materials, and more particularly to a method for preparing a general-purpose cement.
The rapid development of economy brings more and more bulk solid wastes. The storage of the bulk solid wastes not only occupies a large amount of land, but also leads to serious geological disaster risks and pollution to the environment including soil, water system and air. At present, the main method for effectively utilizing the bulk solid wastes is to prepare building materials, including general-purpose cement. The existing general-purpose cement is made of Portland cement clinker mixed with a small amount of gypsum and other mixed materials. Most of the bulk solid wastes are aluminosilicates mainly composed of SiO2 and Al2O3. However, due to its chemical composition of high calcium and low silicon and aluminum, Portland cement has a high carbon emission, and dispose of aluminosilicate wastes with a low mixing content. Moreover, the aluminosilicate wastes containing excessive amounts of alkali metal oxides and MgO cannot be used to prepare Portland cement.
The research and development of low-carbon and environmentally friendly general-purpose cement with high aluminosilicate wastes disposal capacity to replace Portland cement has been the direction of the cement industry. Alkali-activated cement has outstanding advantages such as early strength, corrosion resistance and excellent freeze-thaw resistance. It can make use of a large amount of solid wastes, leading to low carbon emission, energy saving and environmental protection, and is one of the new cements most likely to replace Portland cement. Traditional alkali-activated cement is a two-component cement that is hardened by using strong alkali to activate active amorphous (calcium) aluminosilicates, which still has many shortcomings. 1) Kaolinite resources are scarce, and other main raw materials such as fly ash and blast furnace slag have risen in price due to their large-scale use as admixtures of Portland cement. 2) The addition of a large amount of industrial alkali activator (3-14 wt % in terms of Na2O) also leads to high cost and easy efflorescence, thereby affecting durability. 3) Processing methodologies and properties for AACs derived from solid waste precursors are difficult to standardize due to variations in chemical composition and properties.
The reduction and elimination of the use of alkali activators can effectively reduce the cost of alkali-activated cement. Chinese patent publication No. 110451827A disclosed preparation and use of a steam-curing alkali-activated cement, and Chinese patent publication No. 110372240A disclosed preparation and use of a room temperature-curing alkali-activated cement. A small amount of industrial alkali was mixed with potassium sodium aluminosilicate and calcium raw materials, ground and calcined at 1250-1300° C. before rapidly cooled to obtain a clinker. The clinker was ground and evenly mixed with sodium water glass to obtain the cement. The 28-day compressive strengths of the resulting cement pastes exceed 80 MPa and 110 MPa respectively. The above alkali-activated cements have a lower dosage of the alkali activator compared to the commonly used two-component alkali-activated cement, but still failed to completely eliminate the alkali activator.
An object of the disclosure is to provide a method for preparing a general-purpose cement, which can significantly reduce cement carbon emission and save non-renewable high-quality limestone resources, and requires little or no alkali for activation.
In order to achieve the above object, the following technical solutions are adopted.
This application provides a method for preparing a general-purpose cement, comprising:
In some embodiments, in the clinker, a weight ratio of CaO+MgO to SiO2+Al2O3 is 0.6-1.0:1.
In some embodiments, in the clinker, a weight ratio of SiO2 to Al2O3 is 2.0-7.0:1.
In some embodiments, in the clinker, a weight ratio of MgO to CaO is 0.03-0.66:1.
In some embodiments, in step (2), the cooling is performed by air blast cooling or water quenching.
In some embodiments, in step (3), a weight percentage of a sieve residue of the general-purpose cement is no more than 5% after passing through a 75-μm square hole sieve; and a weight percentage of a sieve residue of the clinker powder is no more than 5% after passing through the 75-μm square hole sieve.
In some embodiments, after hydration, the general-purpose cement is subjected to steam curing at room temperature for no less than 7 days and then subjected to water curing.
Compared with the prior art, this application has the following beneficial effects.
The present disclosure will be further described below in conjunction with the embodiments, but the scope of the present disclosure is not limited thereto.
According to the difference in chemical composition, raw materials of raw meal including 12 types of potassium sodium aluminosilicate, kaolinite, analytical pure sodium carbonate, calcium carbonate, silicon dioxide (quartz), iron oxide and natural dolomite listed in Table 1 were prepared. The above raw materials were dried at 105° C. to constant weight and subjected to chemical composition detection, with the detection results listed in Table 1. In Examples 1-14, the raw materials of each raw meal were mixed according to formulas shown in Table 2, and ground to obtain a raw meal powder. A weight percentage of a sieve residue of raw meal powder was no more than 10% after passing through a 75-μm square hole sieve. The raw meal powder was placed in a corundum crucible, calcinated under heating in a silicon carbide muffle furnace with a heating rate of 10° C./min, and kept at a constant temperature for 1, 2 and 3 h at 1210-1350° C., respectively. After the temperature keeping was completed, the corundum crucible was immediately taken out of the silicon carbide muffle furnace and rapidly cooled by air blast cooling or water quenching to obtain a clinker predominated by a glass phase. The clinker was ground to obtain a clinker powder. A weight percentage of a sieve residue of the clinker powder was no more than 5% after passing through the 75-μm square hole sieve. By means of a powder X-ray diffraction method, it was found that when a temperature keeping time of the same raw material at a highest calcination temperature was changed, the phase characteristics of clinker samples kept at the constant temperature for 2 h and 3 h were the same, while there were some differences in clinker samples kept at the constant temperature for 1 h. Therefore, the temperature keeping time at the highest temperature during clinker calcination was determined as 2 h. A total weight percentage of SiO2, Al2O3, Fe2O3, CaO, MgO, Na2O and K2O in the clinker powder was no less than 93%, and in every 100 parts (by mass) of SiO2+Al2O3+Fe2O3+CaO+MgO+Na2O+K2O, a mass parts distribution is: SiO2 31.5˜44.8, Al2O3 6.1˜19.9, Fe2O3 0˜6.2, CaO 22.5˜45.0, MgO 1.2˜16.0, Na2O+K2O 1.0˜8.3, and a weight ratio of CaO+MgO to SiO2+Al2O3 was 0.6-1.0:1, a weight ratio of SiO2 to Al2O3 was 2.0-7.0:1, and a weight ratio of MgO to CaO was 0.03-0.66:1 (see Table 3 for details).
athe percentage of individual oxides when a sum of SiO2, Al2O3, Fe2O3, CaO, MgO, Na2O and K2O is 100%, and “Others” refer to a content of other chemical components in the clinker.
Analytically-pure NaOH and/or KOH was/were dissolved in as little water as possible and cooled to room temperature. NaOH, KOH or a combination thereof was added such that a weight ratio of NaOH+0.713KOH to the clinker was 0-0.03:1. The clinker powder was added in the alkaline solution and stirred for 2-5 min to obtain a slurry. Water was added in the slurry during stirring to reduce the slurry consistency such that the slurry was liquefied during subsequent vibration. The slurry was placed in a 40×40×40 cubic steel mold and vibrated to compact. The slurry as well as the mold was placed into a standard cement curing box and cured at 20° C. and ≥90% humidity for 1 day followed by demolding to obtain a cement paste test block. In a case where a strength of the slurry did not meet a demolding requirement after 1 day of curing, the demolding was delayed, and the slurry was cured in moisture for 7 days and then soaked in water for 28 days. An unconfined compressive strength of the test block at 3 days, 7 days and 28 days was tested respectively. The ingredients and compressive strength of the cement paste were shown in Table 4. It can be seen from Table 4 that the resulting clinker powder exhibits a certain self-gelling property, that is, it can be solidified by only adding water and has excellent compressive strength. Moreover, the strength of cement increases with the increase of the alkali content. A maximum compressive strength of the cement paste after 28 days reaches 106.0 MPa.
| Number | Date | Country | Kind |
|---|---|---|---|
| 202410204516.1 | Feb 2024 | CN | national |
