Dynamic analysis of the temperature and the concentration profiles of an industrial rotary kiln used in clinker production

dc.creatorDiulia C. Q. Rodrigues
dc.creatorAtílio P. Soares Junior
dc.creatorEsly F. Costa Junior
dc.creatorAndréa Oliveira Souza da Costa
dc.date.accessioned2023-07-28T17:57:44Z
dc.date.accessioned2025-09-08T23:13:38Z
dc.date.available2023-07-28T17:57:44Z
dc.date.issued2017
dc.format.mimetypepdf
dc.identifier.doihttps://doi.org/10.1590/0001-3765201720160661
dc.identifier.issn0001-3765
dc.identifier.urihttps://hdl.handle.net/1843/57133
dc.languageeng
dc.publisherUniversidade Federal de Minas Gerais
dc.relation.ispartofAnais da Academia Brasileira de Ciências
dc.rightsAcesso Aberto
dc.subjectEngenharia Mecânica
dc.subjectAnálise matemática
dc.subjectTemperatura
dc.subject.otherClinker
dc.subject.otherDynamic Analysis
dc.subject.otherMathematical Modelling
dc.subject.otherRotary Kiln
dc.titleDynamic analysis of the temperature and the concentration profiles of an industrial rotary kiln used in clinker production
dc.typeArtigo de periódico
local.citation.epage3136
local.citation.issue4
local.citation.spage3123
local.citation.volume89
local.description.resumoCement is one of the most used building materials in the world. The process of cement production involves numerous and complex reactions that occur under different temperatures. Thus, there is great interest in the optimization of cement manufacturing. Clinker production is one of the main steps of cement production and it occurs inside the kiln. In this paper, the dry process of clinker production is analysed in a rotary kiln that operates in counter flow. The main phenomena involved in clinker production is as follows: free residual water evaporation of raw material, decomposition of magnesium carbonate, decarbonation, formation of C3A and C4AF, formation of dicalcium silicate, and formation of tricalcium silicate. The main objective of this study was to propose a mathematical model that realistically describes the temperature profile and the concentration of clinker components in a real rotary kiln. In addition, the influence of different speeds of inlet gas and solids in the system was analysed. The mathematical model is composed of partial differential equations. The model was implemented in Mathcad (available at CCA/UFES) and solved using industrial input data. The proposal model is satisfactory to describe the temperature and concentration profiles of a real rotary kiln.
local.identifier.orcidhttps://orcid.org/0000-0002-6763-9752
local.publisher.countryBrasil
local.publisher.departmentENG - DEPARTAMENTO DE ENGENHARIA QUÍMICA
local.publisher.departmentENGENHARIA - ESCOLA DE ENGENHARIA
local.publisher.initialsUFMG
local.url.externahttps://www.scielo.br/j/aabc/a/WzPw7PVyWYvDC6phTZv8MRj/?lang=en

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