Experimental study on SO2 recovery using a sodium-zinc sorbent based flue gas desulfurization technology
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Experimental study on SO2 recovery using a sodium-zinc sorbent based flue gas desulfurization technology
Experimental study on SO2 recovery using a sodium-zinc sorbent based flue gas desulfurization technology
中国化学工程学报(英文版)2015年23卷第1期 页码:241-246
Affiliations:
2 National Engineering Laboratory of Coal-Fired Pollution Reduction, School of Energy and Power Engineering, Shandong University,Jinan,China,250061
Author bio:
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DOI:
中图分类号:
纸质出版:2015
Accepted:
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Yang Zhang, Tao Wang, Hairui Yang, 等. Experimental study on SO2 recovery using a sodium-zinc sorbent based flue gas desulfurization technology[J]. 中国化学工程学报(英文版), 2015,23(1):241-246.
recovery using a sodium-zinc sorbent based flue gas desulfurization technology[J]. Chinese Journal of Chemical Engineering, 2015, 23(1): 241-246.
Yang Zhang, Tao Wang, Hairui Yang, 等. Experimental study on SO2 recovery using a sodium-zinc sorbent based flue gas desulfurization technology[J]. 中国化学工程学报(英文版), 2015,23(1):241-246.DOI:
recovery using a sodium-zinc sorbent based flue gas desulfurization technology[J]. Chinese Journal of Chemical Engineering, 2015, 23(1): 241-246.DOI:
Experimental study on SO2 recovery using a sodium-zinc sorbent based flue gas desulfurization technology
A sodium-zinc sorbent based flue gas desulfurization technology (Na-Zn-FGD) was proposed based on the experiments and analyses of the thermal decomposition characteristics of CaSO
3
and ZnSO
3
·2.5H
2
O
the waste products of calcium-based semi-dry and zinc-based flue gas desulfurization (Ca-SD-FGD and Zn-SD-FGD) technologies
respectively. Itwas found that ZnSO
3
·2.5H
2
O first lost crystal H
2
O at 100 ℃ and then decomposed into SO
2
and solid ZnO at 260 ℃ in the air
while CaSO
3
is oxidized at 450 ℃ before it decomposed in the air. The experimental results confirm that Zn-SD-FGD technology is good for SO
2
removal and recycling
but with problem in clogging and high operational cost. The proposed Na-Zn-FGD is clogging proof
and more cost-effective. In the newprocess
Na
2
CO
3
is used to generate Na
2
CO
3
for SO
2
absorption
and the intermediate product NaHSO
3
reacts with ZnO powders
producing ZnSO
3
·2.5H
2
O precipitate and Na
2
CO
3
solution. The Na
2
CO
3
solution is clogging proof
which is re-used for SO
2
absorption. By thermal decomposition of ZnSO
3
·2.5H
2
O
ZnO is re-generated and SO
2
with high purity is co-produced as well. The cycle consumes some amount of raw material Na
2
CO
3
and a small amount of ZnO only. The newly proposed FGD technology could be a substitute of the traditional semi-dry FGD technologies.
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