Development of Zirconium-Stabilized Calcium Oxide Absorbent for Cyclic High-Temperature CO2 Capture

2012 ◽  
Vol 51 (31) ◽  
pp. 10390-10398 ◽  
Author(s):  
Hamid R. Radfarnia ◽  
Maria C. Iliuta
2010 ◽  
Vol 183 (1-3) ◽  
pp. 759-765 ◽  
Author(s):  
Binlin Dou ◽  
Yongchen Song ◽  
Yingguang Liu ◽  
Cong Feng

2021 ◽  
Author(s):  
Matthew T. Dunstan ◽  
Felix Donat ◽  
Alexander H. Bork ◽  
Clare P. Grey ◽  
Christoph R. Müller

2012 ◽  
Vol 6 ◽  
pp. 164-170 ◽  
Author(s):  
Firas N. Ridha ◽  
Vasilije Manovic ◽  
Arturo Macchi ◽  
Edward J. Anthony
Keyword(s):  

2022 ◽  
Vol 429 ◽  
pp. 132236
Author(s):  
Shuzhen Chen ◽  
Jinze Dai ◽  
Changlei Qin ◽  
Weiyang Yuan ◽  
Vasilije Manovic

RSC Advances ◽  
2016 ◽  
Vol 6 (100) ◽  
pp. 97739-97748 ◽  
Author(s):  
Kun Qin ◽  
TsingHai Wang ◽  
Jin-Chiang Huang ◽  
Chih-Hung Huang ◽  
Yi-Kong Hsieh ◽  
...  

Plasma treatment induces a thin CaZrO3 overlayer while the furnace treatment allows CaZrO3 as a wedge between CaO particles.


2013 ◽  
Author(s):  
Saeed Danaei Kenarsari ◽  
Yuan Zheng

A lab-scale CO2 capture system is designed, fabricated, and tested for performing CO2 capture via carbonation of very fine calcium oxide (CaO) with particle size in micrometers. This system includes a fixed-bed reactor made of stainless steel (12.7 mm in diameter and 76.2 mm long) packed with calcium oxide particles dispersed in sand particles; heated and maintained at a certain temperature (500–550°C) during each experiment. The pressure along the reactor can be kept constant using a back pressure regulator. The conditions of the tests are relevant to separation of CO2 from combustion/gasification flue gases and in-situ CO2 capture process. The inlet flow, 1% CO2 and 99% N2, goes through the reactor at the flow rate of 150 mL/min (at standard conditions). The CO2 percentage of the outlet gas is monitored and recorded by a portable CO2 analyzer. Using the outlet composition, the conversion of calcium oxide is figured and employed to develop the kinetics model. The results indicate that the rates of carbonation reactions considerably increase with raising the temperature from 500°C to 550°C. The conversion rates of CaO-carbonation are well fitted to a shrinking core model which combines chemical reaction controlled and diffusion controlled models.


Fuel ◽  
2021 ◽  
pp. 121687
Author(s):  
Fu Li ◽  
Yaoping Wang ◽  
Kai Liu ◽  
Yu Wu ◽  
Jiajia Ai ◽  
...  

2020 ◽  
Vol 59 (19) ◽  
pp. 8937-8945 ◽  
Author(s):  
Cameron Halliday ◽  
Takuya Harada ◽  
T. Alan Hatton

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