In the past years, the employment of carbon dioxide as an alternative is becoming significant. Its compatibility with synthetic compressor lubricants is still a problem far from a solution. In the literature, only a few data on the mutual solubility of the carbon dioxide-lubricant systems are present, although it is one of the main properties affecting the selection of the proper lubricant. At our laboratories, a systematic study on the solubility of carbon dioxide in lubricants has been started, trying to identify its dependence on pressure, temperature, and oil chemical structure. In this work, experimental solubility data of carbon dioxide in pentaerythritol tetra-2-methylbutyrate, i.e., a precursor of polyol ester oil, are presented in the temperature range of (243 to 343) K and pressure up to 10 MPa. The experimental data were correlated by means of the Peng-Robinson equation of state with the Huron Vidal mixing rules in which the excess Gibbs energy at infinite pressure was represented by the UNIQUAC equation assuming a temperature dependence of the fitted parameters.

Solubility temperature dependence and data Correlation of carbon dioxide in pentaerythritol tetra-2-methylbutyrate

Laura Fedele;Sergio Bobbo;
2009

Abstract

In the past years, the employment of carbon dioxide as an alternative is becoming significant. Its compatibility with synthetic compressor lubricants is still a problem far from a solution. In the literature, only a few data on the mutual solubility of the carbon dioxide-lubricant systems are present, although it is one of the main properties affecting the selection of the proper lubricant. At our laboratories, a systematic study on the solubility of carbon dioxide in lubricants has been started, trying to identify its dependence on pressure, temperature, and oil chemical structure. In this work, experimental solubility data of carbon dioxide in pentaerythritol tetra-2-methylbutyrate, i.e., a precursor of polyol ester oil, are presented in the temperature range of (243 to 343) K and pressure up to 10 MPa. The experimental data were correlated by means of the Peng-Robinson equation of state with the Huron Vidal mixing rules in which the excess Gibbs energy at infinite pressure was represented by the UNIQUAC equation assuming a temperature dependence of the fitted parameters.
2009
Istituto per le Tecnologie della Costruzione - ITC
Equations of state
Esters
Lubricants
Solubility
Temperature distribution
File in questo prodotto:
Non ci sono file associati a questo prodotto.

I documenti in IRIS sono protetti da copyright e tutti i diritti sono riservati, salvo diversa indicazione.

Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/20.500.14243/27459
Citazioni
  • ???jsp.display-item.citation.pmc??? ND
  • Scopus 11
  • ???jsp.display-item.citation.isi??? 12
social impact