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捕获水泥生产中使用的碳酸钙煅烧产生的二氧化碳的方法。

Process for capturing CO2 arising from the calcination of the CaCO3 used in cement manufacture.

作者信息

Rodríguez N, Alonso M, Grasa G, Abanades J Carlos

机构信息

Institution Nacional del Carbón, INCAR-CSIC, Francisco Pintado Fe, 26, Oviedo 33011, Spain.

出版信息

Environ Sci Technol. 2008 Sep 15;42(18):6980-4. doi: 10.1021/es800507c.

Abstract

This paper outlines a new CaCO3 calcination method for producing a stream of CO2 (suitable for permanent geological storage after purification and compression). The process is based on the use of very hot CaO particles (T >1000 degrees C) to transfer heat from a circulating fluidized bed combustor (CFBC) to a calciner (fluidized with CO2 and/or steam). Since the fluidized bed combustor and calciner have separate atmospheres, the CO2 resulting from the decomposition of CaCO3 can be captured, while the CO2 generated in the combustion of the fuel in air is emitted to the atmosphere. We demonstrate that with this system it is possible to reduce the CO2 emissions of a cement plant by around 60%. Furthermore, since the key pieces of equipment are similar to the commercial CFBCs used in power generation plants, it is possible to establish the additional investment required for the system and to estimate the cost per ton of CO2 avoided for this process to be about 19 $/tCO2 avoided.

摘要

本文概述了一种新的碳酸钙煅烧方法,用于产生一股二氧化碳流(经净化和压缩后适合永久地质封存)。该工艺基于使用非常热的氧化钙颗粒(温度>1000摄氏度)将热量从循环流化床燃烧器(CFBC)传递到煅烧炉(用二氧化碳和/或蒸汽流化)。由于流化床燃烧器和煅烧炉有独立的气氛,碳酸钙分解产生的二氧化碳可以被捕获,而燃料在空气中燃烧产生的二氧化碳则排放到大气中。我们证明,使用该系统可将水泥厂的二氧化碳排放量减少约60%。此外,由于关键设备与发电厂使用的商业循环流化床燃烧器相似,因此可以确定该系统所需的额外投资,并估计该工艺避免每吨二氧化碳的成本约为19美元/tCO2避免。

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