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 inAerosol and air quality research Vol. 24; no. 2; pp. 220398 - 11
Main Authors Chen, Yu-Lun, Ku, Young, Chang, Ya-Chun
Format Journal Article
LanguageEnglish
Published Cham Springer International Publishing 01.02.2024
Springer
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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.
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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Keywords oxygen carrier
Sulfurization desulfurization
CaO/Fe
Chemical looping combustion
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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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