Abstract
In order to elucidate the high-temperature reaction process of solid waste-based high belite sulphoaluminate cement containing residual gypsum in clinker (NHBSAC) and obtain the formation laws of each mineral in clinker, this article studied its high-temperature reaction kinetics. Through QXRD analysis and numerical fitting methods, the formation of C(4)A(3)S¯, β-C(2)S, and CaSO(4) in clinker under different calcination systems was quantitatively characterized, the corresponding high-temperature reaction kinetics models were established, and the reaction activation energies of each mineral were obtained. The results indicate that the content of C(4)A(3)S¯ and β-C(2)S increases with the prolongation of holding time and the increase in calcination temperature, while CaSO(4) is continuously consumed. Under the control mechanism of solid-state reaction, the formation and consumption of minerals follow the kinetic equation. C(4)A(3)S¯ and β-C(2)S satisfy the D(4) equation under diffusion mechanism control, and CaSO(4) satisfies the R(3) equation under interface chemical reaction mechanism control. The activation energy required for mineral formation varies with different temperature ranges. The activation energies required to form C(4)A(3)S¯ at 1200-1225 °C, 1225-1275 °C, and 1275-1300 °C are 166.28 kJ/mol, 83.14 kJ/mol, and 36.58 kJ/mol, respectively. The activation energies required to form β-C(2)S at 1200-1225 °C and 1225-1300 °C are 374.13 kJ/mol and 66.51 kJ/mol, respectively. This study is beneficial for achieving flexible control of the mineral composition of NHBSAC clinker, providing a theoretical basis and practical experience for the preparation of low-carbon cement and the optimization design of its mineral composition.