Volume 45, Issue 4 pp. 5165-5176
RESEARCH ARTICLE

Alkali metal modified iron-nickel oxygen carrier to produce hydrogen-rich synthesis gas by chemical looping gasification with pine sawdust

Pengcheng Wang

Pengcheng Wang

Key Laboratory of Low-Grade Energy Utilization Technologies and Systems, Ministry of Education, Chongqing University, Chongqing, China

School of Energy and Power Engineering, Chongqing University, Chongqing, China

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Ge Pu

Corresponding Author

Ge Pu

Key Laboratory of Low-Grade Energy Utilization Technologies and Systems, Ministry of Education, Chongqing University, Chongqing, China

School of Energy and Power Engineering, Chongqing University, Chongqing, China

Correspondence

Ge Pu, Key Laboratory of Low-Grade Energy Utilization Technologies and Systems, Ministry of Education, School of Energy and Power Engineering, Chongqing University, Chongqing 400044, China.

Email: [email protected]

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Qiwen Liu

Qiwen Liu

Key Laboratory of Low-Grade Energy Utilization Technologies and Systems, Ministry of Education, Chongqing University, Chongqing, China

School of Energy and Power Engineering, Chongqing University, Chongqing, China

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Weicheng Xiong

Weicheng Xiong

Key Laboratory of Low-Grade Energy Utilization Technologies and Systems, Ministry of Education, Chongqing University, Chongqing, China

School of Energy and Power Engineering, Chongqing University, Chongqing, China

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First published: 23 October 2020
Citations: 16

Summary

In the research of biomass chemical looping gasification technology, the production of hydrogen-rich synthesis gas has received increasing attention. In this paper, iron-nickel oxygen carriers were prepared by the mechanical and impregnation method. Chemical looping gasification experiments were performed with pine sawdust in a self-built fixed-bed reactor to prepare hydrogen-rich synthesis gas. Experimental results showed that for the iron-nickel oxygen carrier with a loading ratio of 3% NiO under reaction conditions of 800°C, ratio of steam content to biomass (S/B) of 1.25, and ratio of lattice oxygen to biomass (O/B) of 0.2, the volume fraction of hydrogen in the synthesized gas reached 43.06%; correspondingly, the carbon conversion rate was 78.22%, the low calorific value of syngas was 7.49 MJ/Nm3, and the gas production rate was 1.25 Nm3/kg. After modification of the iron-nickel oxygen carrier with a mass ratio of 5% K2CO3, the volume fraction of hydrogen in the prepared synthesis gas increased to 47.83%, the corresponding carbon conversion rate was 85.44%, and the low-level calorific value was 7.95 MJ/Nm3. The gas production rate was 1.49 Nm3/kg.

DATA AVAILABILITY STATEMENT

The data that support the findings of this study are available from the corresponding author upon reasonable request.

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