Estudo do Comportamento de Fase e Volumétrico do Sistema Dióxido de Carbono + n-Hexadecano + n-Butil Ciclohexano a Altas Temperaturas e Pressões

Detalhes bibliográficos
Ano de defesa: 2022
Autor(a) principal: Silva, Maxwell Risseli Laurentino da
Orientador(a): Não Informado pela instituição
Banca de defesa: Não Informado pela instituição
Tipo de documento: Dissertação
Tipo de acesso: Acesso aberto
Idioma: por
Instituição de defesa: Não Informado pela instituição
Programa de Pós-Graduação: Não Informado pela instituição
Departamento: Não Informado pela instituição
País: Não Informado pela instituição
Palavras-chave em Português:
CO2
Link de acesso: http://www.repositorio.ufc.br/handle/riufc/65953
Resumo: This work reports carbon dioxide (CO2) + n-hexadecane (C16) + n-butyl cyclohexane (butyl) phase and volumetric behavior at pressure up to P = 13.30 MPa (for vapor-liquid equilibria - VLE) and P = 100.00 MPa (for volumetric analysis) and for temperature up to T = 403.15 K. VLE measurements were carried out using a variable volume cell to bubble pressure determination. Three different compositions were studied: i) alkane-rich phase; ii) equimolar; and, iii) butyl-rich phase, covering a molar fraction range of 0.15 – 0.57, 0.15 – 0.61, and 0.15 – 0.56, respectively. Bubble point pressure prediction capability of two different equations of state were tested, as follows: Peng-Robinson (PR), Soave-Redlich-Kwong (SRK) and their predictive forms (PSRK - predictive Soave-Redlich-Kwong and VTPR - volume translated Peng-Robinson). Best results were obtained for SRK equation of state for regressed binary interaction parameter (kij), with a total average absolute relative deviation (AARD) of 16.15% of for all phases. Density measurements were obtained by intermediate of a U-tube vibrating densimeter, for a gas mole fraction of 0.0, 0.40 and 0.62; 0.0, 0.46 and 0.59; and, 0.0, 0.45 and 0.60 for: i) alkane-rich phase; ii) equimolar; and, iii) butyl-rich phase, respectively. These data were correlated by using Tamman-Tait equation and the capacity of the four state equations (SRK, PSRK, PR and VTPR) were tested for liquid phase prediction. PR and its predictive form, VTPR, presented the best results of AARD.