Thermodynamic modelling of cements clinkering process as a tool for optimising the proportioning of raw meals containing alternative materials

被引:7
作者
Costa, Ana R. D. [1 ,2 ]
Coppe, Mateus V. [3 ]
Bielefeldt, Wagner V. [3 ]
Bernal, Susan A. [2 ]
Black, Leon [2 ]
Kirchheim, Ana Paula [4 ]
Goncalves, Jardel P. [1 ,5 ]
机构
[1] Fed Univ Bahia UFBA, Polytech Sch, Postgrad Program Civil Engn PPEC, BR-40210630 Salvador, Brazil
[2] Univ Leeds, Sch Civil Engn, Leeds LS2 9JT, England
[3] Fed Univ Rio Grande do Sul UFRGS, Dept Met, Postgrad Program Min Met & Mat Engn PPGE3M, Iron & Steelmaking Lab LASID, BR-91501970 Porto Alegre, Brazil
[4] Fed Univ Rio Grande do Sul UFRGS, Dept Civil Engn, Bldg Innovat Res Unit NORIE, BR-90035190 Porto Alegre, Brazil
[5] Fed Univ Bahia UFBA, Interdisciplinary Ctr Energy & Environm CIENAM, BR-40170115 Salvador, Brazil
基金
英国工程与自然科学研究理事会;
关键词
FLUID CATALYTIC CRACKING; SPENT CATALYSTS; HYDRATION; SYSTEM; PHASE; PERFORMANCE; MINERALS; ZEOLITE; MULLITE; REUSE;
D O I
10.1038/s41598-023-44078-7
中图分类号
O [数理科学和化学]; P [天文学、地球科学]; Q [生物科学]; N [自然科学总论];
学科分类号
07 ; 0710 ; 09 ;
摘要
The valorisation of waste or by-products in Portland clinker production is a promising alternative for developing sustainable cements. The complexity of the chemical reactions during clinkering demands an adequate dosing method that considers the effect of feedstock impurities to maximise the potential substitution of natural resources by waste or by-products, while guaranteeing the clinker reactivity requirements. This study proposes a raw meal proportioning methodology for optimising co-processing of natural feedstocks with alternative raw materials in clinker production, intending to reduce the content of natural raw materials needed, while promoting an optimal clinker reactivity. A thermodynamic modelling sequence was developed considering the variability of raw materials composition and heating temperatures. The model was then validated by comparing simulation outcomes with results reported in previous studies. An experimental case study was conducted for validation of the proposed method using a spent fluid catalytic cracking catalyst (SFCC), a by-product from the oil industry as an alternative alumina source during clinkering. The modelling simulations indicated that substitution of natural feedstocks by 15 wt% SFCC promotes the formation of reactive clinkers with more than 54% tricalcium silicate (C3S). Mixes with the potential to form the highest C3S were then produced, and heating microscopy fusibility testing was applied for evaluating the clinkers' stability. The main factors governing the reactivity and stability of the clinker phases were the melt phase content, alumina modulus, and formation of C3S and dicalcium silicate (C2S). The self-pulverisation of clinker during cooling was observed in selected mixes, and it is potentially associated with high viscosity and low Fe content in the melt phase. The proposed framework enables optimisation of the dosing of raw meals containing alternative alumina-rich feedstocks for clinker production and allows a deeper interpretation of limited sets of empirical data.
引用
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页数:19
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