Environmental impact of incineration of calorific industrial waste: Rotary kiln vs. cement kiln

2012 ◽  
Vol 32 (10) ◽  
pp. 1853-1863 ◽  
Author(s):  
Isabel Vermeulen ◽  
Jo Van Caneghem ◽  
Chantal Block ◽  
Wim Dewulf ◽  
Carlo Vandecasteele
2014 ◽  
Vol 2014 ◽  
pp. 1-8 ◽  
Author(s):  
Shamsad Ahmad ◽  
Ibrahim Hakeem ◽  
Mohammed Maslehuddin

In the exploratory study presented in this paper, an attempt was made to develop different mixtures of ultrahigh performance concrete (UHPC) using various locally available natural and industrial waste materials as partial replacements of silica fume and sand. Materials such as natural pozzolana (NP), fly ash (FA), limestone powder (LSP), cement kiln dust (CKD), and pulverized steel slag (PSS), all of which are abundantly available in Saudi Arabia at little or no cost, were employed in the development of the UHPC mixtures. A base mixture of UHPC without replacement of silica fume or sand was selected and a total of 24 trial mixtures of UHPC were prepared using different percentages of NP, FA, LSP, CKD, and PSS, partially replacing the silica fume and sand. Flow and 28-d compressive strength of each UHPC mixture were determined to finally select those mixtures, which satisfied the minimum flow and strength criteria of UHPC. The test results showed that the utilization of NP, FA, LSP, CKD, and PSS in production of UHPC is possible with acceptable flow and strength. A total of 10 UHPC mixtures were identified with flow and strength equal to or more than the minimum required.


Author(s):  
Atinder Pal Singh ◽  
P.S. Ghoshdastidar

Abstract The paper presents computer simulation of heat transfer in alumina and cement rotary kilns. The model incorporates radiation exchange among solids, wall and gas, convective heat transfer from the gas to the wall and the solids, contact heat transfer between the covered wall and the solids, and heat loss to the surroundings as well as chemical reactions. The mass and energy balances of gas and solids have been performed in each axial segment of the kilns. The energy equation for the wall is solved numerically by the finite-difference method. The dust entrainment in the gas is also accounted for. The solution marches from the solids inlet to the solids outlet. The kiln length predicted by the present model of the alumina kiln is 77.5 m as compared to 80 m of the actual kiln of Manitius et al. (1974, Manitius, A., Kurcyusz, E., and Kawecki, W., “Mathematical Model of an Aluminium Oxide Rotary Kiln,” Ind. Eng. Chem. Process Des. Dev., 13 (2), pp. 132-142). In the second part, heat transfer in a dry process cement rotary kiln is modelled. The melting of the solids and coating formation on the inner wall of the kiln are also taken into account. A detailed parametric study lent a good physical insight into axial solids and gas temperature distributions, and axial variation of chemical composition of the products in both the kilns. The effect of kiln rotational speed on the cement kiln wall temperature distribution is also reported.


2013 ◽  
Vol 30 (4) ◽  
pp. 297-303
Author(s):  
Ki-Heon Kim ◽  
◽  
Hae-Young Jung ◽  
Min-Young Kim ◽  
Jun-Ik Son ◽  
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2020 ◽  
Vol 12 (4) ◽  
pp. 24-30
Author(s):  
Alla Zvyaginceva ◽  
Svetlana Sazonova ◽  
V. Kul'neva

The environmental impact of the LLC «EVO» company in Voronezh was assessed and the process of processing mercury-containing waste was analyzed. The characteristics of storage devices for storage and storage of industrial waste are considered. Comprehensive environmental protection measures aimed at reducing the negative impact of mercury-containing wastes that emit mercury vapor on air and water are proposed.


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