کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
10274873 | 461768 | 2005 | 37 صفحه PDF | دانلود رایگان |
عنوان انگلیسی مقاله ISI
Review-calcination and carbonation of limestone during thermal cycling for CO2 sequestration
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کلمات کلیدی
موضوعات مرتبط
مهندسی و علوم پایه
مهندسی شیمی
مهندسی شیمی (عمومی)
پیش نمایش صفحه اول مقاله
![عکس صفحه اول مقاله: Review-calcination and carbonation of limestone during thermal cycling for CO2 sequestration Review-calcination and carbonation of limestone during thermal cycling for CO2 sequestration](/preview/png/10274873.png)
چکیده انگلیسی
Some aspects of using lime from limestone to sequester CO2 from combustion systems are examined in this review of the literature. A typical sequestration technology would consist of two circulating fluidised beds, one operated in the temperature range 600-700 °C and acting as a carbonator, and the other in the temperature range 750-950 °C acting as a cracker. The processes involved in calcination, sintering, and carbonation are summarised, including the relative rates of reaction. The physical properties of the calcined products after sintering and reaction are reviewed. The loss of active calcium due to the competitive formation of sulphates and other calcium compounds is noted. Prolonged residence times in fluidised bed systems will lead to extensive loss of surface area and porosity in the particles. The likely extent of particle fragmentation is discussed, and some cost figures for avoided CO2 emissions from power generation systems are presented. The need for a realistic model of the processes taking place in the particles is emphasised.
ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Fuel Processing Technology - Volume 86, Issue 16, November 2005, Pages 1707-1743
Journal: Fuel Processing Technology - Volume 86, Issue 16, November 2005, Pages 1707-1743
نویسندگان
B.R. Stanmore, P. Gilot,