Abstract

This work deals with solid–vapor equilibria and solid–liquid–vapor equilibria of carbon dioxide in mixtures of interest for natural gas purification and biogas upgrading. Experimental data available in the literature are reviewed and an algorithm for solving an isobaric–isothermal flash coupled to a phase stability analysis is presented, which does not require a-priori knowledge of the number and type of phases existing at equilibrium. The good agreement between calculation results, also performed with a tool that makes use of Gibbs free energy minimization, and experimental data suggests that the proposed approach can be used for determining suitable operating conditions for processes aimed at separating CO2 out of a gas by freezing it. This work points out that more experimental studies should be performed on phase equilibria in the presence of solid CO2 for multicomponent mixtures containing species other than methane (e.g., nitrogen and oxygen), which are representative of gaseous streams from which CO2 needs to be removed, such as natural gas, biogas, and flue gas from power plants. Such data are important for a proper calibration of thermodynamic models that must be selected for reliable process simulations.

Highlights

  • In the process industry field, one of the biggest concerns has always been the sweetening of acid gaseous streams

  • This work deals with phase equilibria in the presence of solid CO2 for mixtures of interest in the fields of natural gas purification and biogas/landfill gas upgrading

  • Experimental data for solid−vapor equilibria and solid−liquid−vapor equilibria available in the literature are first reviewed, reporting the type of measurements to which they refer for the CO2− CH4 binary mixture, the CO2−CH4−N2 ternary mixture, and the CO2−CH4−N2−O2 quaternary mixture

Read more

Summary

Introduction

In the process industry field, one of the biggest concerns has always been the sweetening of acid gaseous streams. The presence of high CO2 contents in natural gas results in a reduction of the calorific value of the gas and causes corrosion of the pipeline and equipment, along with many other operational problems.[1] Among the established CO2 separation strategies, recently CO2 capture using low-temperature/cryogenic technologies has received increasing attention. Previous works have demonstrated they have lower energy consumptions than conventional amine scrubbing if applied both to natural gas purification[2] and to biogas upgrading.[3] Another advantage these technologies offer is that pure CO2 is separated as a liquid under pressure rather than in the gaseous state at near ambient pressure, making it relatively easy to pump underground for storage or to be used for enhanced oil recovery (EOR) applications.[4]

Objectives
Results
Conclusion
Full Text
Published version (Free)

Talk to us

Join us for a 30 min session where you can share your feedback and ask us any queries you have

Schedule a call