Sulfurization- Desulfurization of Iron-Calcium Oxygen Carriers during Chemical Looping Combustion of Syngas
Chemical looping combustion of SO 2 -containing syngas with various fabricated iron-calcium oxygen carriers was studied to comprehend the sulfurization and desulfurization of oxygen carriers during combustion. Experimental results indicated calcium-iron oxygen carriers fabricated with CaO:Fe 2 O 3 w...
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Published in | Aerosol and air quality research Vol. 24; no. 2; pp. 220398 - 11 |
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Main Authors | , , |
Format | Journal Article |
Language | English |
Published |
Cham
Springer International Publishing
01.02.2024
Springer |
Subjects | |
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Abstract | Chemical looping combustion of SO
2
-containing syngas with various fabricated iron-calcium oxygen carriers was studied to comprehend the sulfurization and desulfurization of oxygen carriers during combustion. Experimental results indicated calcium-iron oxygen carriers fabricated with CaO:Fe
2
O
3
weight ratio of 3:7 and calcined at 800°C (CaFe-378) was suitable for chemical looping combustion of syngas. CaFe
2
O
4
was noticed to be the dominant crystalline phase in CaFe-378 even after 10 redox operations. Reduction kinetics for chemical looping combustion of both H
2
or CO in syngas with CaFe-378 were adequately described by the 2-dimension diffusion model. The activation energies of H
2
and CO with CaFe-378 were determined to be 35.4 kJ mol
−1
and 46.0 kJ mol
−1
, respectively. Calcium sulfide (CaS) was generated during the chemical looping combustion of SO
2
-containing syngas with CaFe-378. CaS was further oxidized to CaSO
4
on the surface of CaFe-378 during air regeneration, which might inhibit the complete regeneration of iron oxides. Satisfactory regeneration of sulfurized oxygen carriers was accomplished by introducing hydrogen after the air-regeneration because of the reduction of calcium sulfate to calcium oxide. |
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AbstractList | Abstract Chemical looping combustion of SO2-containing syngas with various fabricated iron-calcium oxygen carriers was studied to comprehend the sulfurization and desulfurization of oxygen carriers during combustion. Experimental results indicated calcium-iron oxygen carriers fabricated with CaO:Fe2O3 weight ratio of 3:7 and calcined at 800°C (CaFe-378) was suitable for chemical looping combustion of syngas. CaFe2O4 was noticed to be the dominant crystalline phase in CaFe-378 even after 10 redox operations. Reduction kinetics for chemical looping combustion of both H2 or CO in syngas with CaFe-378 were adequately described by the 2-dimension diffusion model. The activation energies of H2 and CO with CaFe-378 were determined to be 35.4 kJ mol−1 and 46.0 kJ mol−1, respectively. Calcium sulfide (CaS) was generated during the chemical looping combustion of SO2-containing syngas with CaFe-378. CaS was further oxidized to CaSO4 on the surface of CaFe-378 during air regeneration, which might inhibit the complete regeneration of iron oxides. Satisfactory regeneration of sulfurized oxygen carriers was accomplished by introducing hydrogen after the air-regeneration because of the reduction of calcium sulfate to calcium oxide. Chemical looping combustion of SO 2 -containing syngas with various fabricated iron-calcium oxygen carriers was studied to comprehend the sulfurization and desulfurization of oxygen carriers during combustion. Experimental results indicated calcium-iron oxygen carriers fabricated with CaO:Fe 2 O 3 weight ratio of 3:7 and calcined at 800°C (CaFe-378) was suitable for chemical looping combustion of syngas. CaFe 2 O 4 was noticed to be the dominant crystalline phase in CaFe-378 even after 10 redox operations. Reduction kinetics for chemical looping combustion of both H 2 or CO in syngas with CaFe-378 were adequately described by the 2-dimension diffusion model. The activation energies of H 2 and CO with CaFe-378 were determined to be 35.4 kJ mol −1 and 46.0 kJ mol −1 , respectively. Calcium sulfide (CaS) was generated during the chemical looping combustion of SO 2 -containing syngas with CaFe-378. CaS was further oxidized to CaSO 4 on the surface of CaFe-378 during air regeneration, which might inhibit the complete regeneration of iron oxides. Satisfactory regeneration of sulfurized oxygen carriers was accomplished by introducing hydrogen after the air-regeneration because of the reduction of calcium sulfate to calcium oxide. |
Author | Chang, Ya-Chun Ku, Young Chen, Yu-Lun |
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Snippet | Chemical looping combustion of SO
2
-containing syngas with various fabricated iron-calcium oxygen carriers was studied to comprehend the sulfurization and... Abstract Chemical looping combustion of SO2-containing syngas with various fabricated iron-calcium oxygen carriers was studied to comprehend the sulfurization... |
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StartPage | 220398 |
SubjectTerms | Atmospheric Protection/Air Quality Control/Air Pollution CaO/Fe2O3 oxygen carrier Chemical looping combustion Climate Change/Climate Change Impacts Environment Environmental Health Original Research Sulfurization desulfurization |
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Title | Sulfurization- Desulfurization of Iron-Calcium Oxygen Carriers during Chemical Looping Combustion of Syngas |
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