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1. Introduction - Firenze University Press

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Abstract:<br />

PROCEEDINGS OF ECOS 2012 - THE 25 TH INTERNATIONAL CONFERENCE ON<br />

EFFICIENCY, COST, OPTIMIZATION, SIMULATION AND ENVIRONMENTAL IMPACT OF ENERGY SYSTEMS<br />

JUNE 26-29, 2012, PERUGIA, ITALY<br />

Carbon dioxide storage by mineralisation applied<br />

to a lime kiln<br />

Inês Romão a,b , Matias Eriksson c,d , Experience Nduagu a , Johan Fagerlund a ,<br />

Licínio M. Gando-Ferreira b and Ron Zevenhoven a<br />

a Åbo Akademi <strong>University</strong>, Dept. of Chemical Engineering, Åbo / Turku, Finland,<br />

iromao@abo.fi (CA)<br />

b <strong>University</strong> of Coimbra, Dept. of Chemical Engineering, Coimbra, Portugal<br />

c Nordkalk Corporation, Pargas / Parainen, Finland<br />

d Umeå <strong>University</strong>, Sweden<br />

This paper describes a design, for a pilot-scale application, of a two-staged process that is under study at<br />

Åbo Akademi <strong>University</strong> (ÅA), for Carbon dioxide Storage by Mineralisation (CSM). The ÅA route implies the<br />

production of brucite (besides Ca- and Fe- based by-products) from a magnesium/calcium silicate rock,<br />

using recoverable ammonium sulphate (AS), followed by carbonation of the Mg(OH)2 in a pressurised<br />

fluidised bed at ~ 500°C, 20-30 bar CO2 partial pressure. An assessment is reported for operating the CSM<br />

process on waste heat from a limekiln (lime production: 210 t/day) in Pargas, Southwest Finland, i.e. without<br />

external energy input apart from what is needed for crushing the rock to the required particle size (a few % of<br />

the overall CSM process energy requirement) and compressing the flue gas to be treated. Part of the off-gas<br />

from the limekiln (CO2 content ~21%-vol) will be processed without a CO2 separation step. The feature of<br />

operating without CO2 separation makes CSM an attractive and cost-competitive option when compared to<br />

conventional CCS involving underground storage of CO2. An exergy analysis is used to optimise process<br />

layout and energy efficiency, and at the same time maximise the amount of CO2 that can be bound to<br />

MgCO3 given the amount of waste heat available from the kiln. Also, experimental results are reported for<br />

producing Mg(OH)2 (and Fe,Ca(OH)2) from local rock material.<br />

Keywords:<br />

CO2 mineral sequestration, Scale-up, Lime kiln.<br />

<strong>1.</strong> <strong>Introduction</strong><br />

<strong>1.</strong>1 CO2 mineralisation<br />

For Finland, carbon dioxide storage by mineralisation (CSM) was identified as the only option for<br />

CCS (carbon dioxide capture and storage) application. It is a permanent storage option and has an<br />

estimated storage potential that is much larger than underground storage as pressurized CO2 [1-2],<br />

the currently most intensively studied option for CO2 disposal. The purpose of CSM is to promote<br />

CO2 fixation by metal oxides into thermodynamically stable carbonates while benefiting of the<br />

exothermicity of the carbonation reaction:<br />

(Ca,Mg)*ySiO2*zH2O (s) + CO2 (g) → (Ca,Mg)CO3 (s) + ySiO2 (s) + z H2O (g) + HEAT (R1)<br />

Magnesium in particular is abundant in the earth’s crust, as silicates such as serpentinite and<br />

olivine. These reactions occur in nature over geological timescales (hundreds of thousands of<br />

years). Research has focused on improving the reaction rates by treating the mineral rock by<br />

thermal, mechanical or chemical means [1-4]. Due to the exceptionally large scale of CCS<br />

processes, all additives must be recovered, and the energy input minimised.<br />

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