Abstract

The calcium looping (CaL) process, based on the calcination/carbonation of CaCO3 at high temperatures, has emerged in the last years as a potentially low cost technology for CO2 capture. In this work, we show that the application of high intensity sound waves to granular beds of limestone and dolomite in a CaL reactor enhances significantly their multicycle CO2 capture capacity. Sound waves are applied either during the calcination stage of each CaL cycle or in the carbonation stage. The effect of sound is to intensify the transfer of heat, mass and momentum and is more marked when sound is applied during calcination by promoting CaO regeneration. The application of sound would allow reducing the calcination temperature thereby mitigating the decay of capture capacity with the number of cycles and reducing the energy penalty of the technology.

Highlights

  • The calcium looping (CaL) process is a second generation technology to capture CO2 by means of cyclic carbonation and calcination of CaO [1,2,3,4,5]

  • The application of sound would allow reducing the calcination temperature thereby mitigating the decay of capture capacity with the number of cycles and reducing the energy penalty of the technology

  • We investigate the effect of high intensity low frequency sound on the multicycle capture performance of fixed limestone and dolomite beds operated at CaL conditions

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Summary

Introduction

The calcium looping (CaL) process is a second generation technology to capture CO2 by means of cyclic carbonation and calcination of CaO [1,2,3,4,5] In this process, the gas is passed through a bed of CaO particles at atmospheric pressure in a carbonator reactor operated at around 650 0 C. The gas is passed through a bed of CaO particles at atmospheric pressure in a carbonator reactor operated at around 650 0 C At this temperature, the kinetics of carbonation is fast enough as required by industrial applications whereas the equilibrium CO2 concentration is low (around 1% vol.), which allows for a high CO2 capture efficiency [6]. Pre-combustion capture conditions require either fixed or bubbling beds operated at low gas velocities (∼ 1-10 cm/s)

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