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1.四川大学 新能源与低碳技术研究院,四川 成都 610207
2.四川大学 碳中和未来技术学院,四川 成都 610207
钟涵琪(2001—),硕士研究生,研究方向为能源环境工程,E-mail:zhongh7@126.com。
岑望来(1981—),博士,副研究员,博士研究生导师,研究方向为能源环境材料计算模拟,E-mail:cenwanglai@scu.edu.cn;
肖 鑫(1993—),博士,助理研究员,研究方向为二氧化碳及生物质转化,E-mail:xiaoxin93@scu.edu.cn。
收稿日期:2025-01-07,
修回日期:2025-03-03,
纸质出版日期:2025-05-25
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钟涵琪,岑望来,肖鑫.基于钢渣元素的铁钙基双功能材料吸附增强水气变换制氢[J].低碳化学与化工,2025,50(5):155-162.
ZHONG Hanqi,CEN Wanglai,XIAO Xin.Adsorption enhancement of water-gas shift to produce hydrogen of iron-calcium-based dual-functional materials based on steel slag[J].Low-Carbon Chemistry and Chemical Engineering,2025,50(5):155-162.
钟涵琪,岑望来,肖鑫.基于钢渣元素的铁钙基双功能材料吸附增强水气变换制氢[J].低碳化学与化工,2025,50(5):155-162. DOI: 10.12434/j.issn.2097-2547.20250006.
ZHONG Hanqi,CEN Wanglai,XIAO Xin.Adsorption enhancement of water-gas shift to produce hydrogen of iron-calcium-based dual-functional materials based on steel slag[J].Low-Carbon Chemistry and Chemical Engineering,2025,50(5):155-162. DOI: 10.12434/j.issn.2097-2547.20250006.
为应对水气变换制氢过程中CO
2
大量排放的问题,可利用铁钙基吸附/催化双功能材料原位吸附CO
2
,提高水气变换反应的制氢脱碳效率。以钢渣所含元素作为材料组成元素,采用共沉淀法制备了Fe
x
/CaO-MAM样品(
x
=
n
(Ca)/
n
(Fe))。通过XRD、N
2
物理吸/脱附、CO
2
-TPD和TG等对样品的物相组成、织构性质、碱度、碱性位点数量和CO
2
吸附性能进行了表征,并利用固定床反应器研究了样品在水气变换中的吸附/催化性能。结果表明,Fe
5
/CaO-MAM的碱性位点最多,CO
2
吸附容量最大(0.105 g/g),且10次循环后CO
2
吸附容量仅下降23%。在温度600 ℃、常压、
n
(H
2
O)/
n
(CO) = 6、混合气流量100 mL/min(
φ
(CO) = 4%,
φ
(N
2
) = 46%,
φ
(Ar) = 50%)条件下反应2 h,Fe
5
/CaO-MAM表现出最优的吸附/催化性能,其CO平均转化率和H
2
平均产率均达到84.24%,H
2
选择性为100%,产物气中CO
2
平均占比(体积分数)为18.05%,预穿透阶段持续时长达2 h。
In order to address the i
ssue of significant CO
2
emissions during the water-gas shift to produce hydrogen
iron-calcium-based dual-functional materials can be utilized for in situ CO
2
adsorption
enhancing the efficiency of hydrogen production and decarbonization in water-gas shift reaction. Fe
x
/CaO-MAM samples (
x
=
n
(Ca)/
n
(Fe)) with elements derived from steel slag were prepared by co-precipitation method. The phase compositions
textural properties
alkalinities
numbers of alkaline sites and CO
2
adsorption properties of the samples were characterized by XRD
N
2
physical adsorption/desorption
CO
2
-TPD
TG and so on. The adsorption/catalysis performances of the samples in water-gas shift were studied by a fixed-bed reactor. The results show that Fe
5
/CaO-MAM exhibits the most alkaline sites and the highest CO
2
adsorption capacity (0.105 g/g)
and the CO
2
adsorption capacity only decreases by 23% after ten cycles. Under the temperature of 600 ℃
atmospheric pressure
n
(H
2
O)/
n
(CO) = 6 and the mixed gas (
φ
(CO) = 4%
φ
(N
2
) = 46% and
φ
(Ar) = 50%) flow rate of 100 mL/min
Fe
5
/CaO-MAM shows the best adsorption/catalysis performance after reaction for 2 h
with CO average conversion rate and H
2
average yield both reaching 84.24% and H
2
average selectivity of 100%. The average proportion (volume fraction) of CO
2
in the product gas is 18.05%
and the pre-penetration stage lasts up to 2 h.
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