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1.河南能源集团研究总院有限公司,河南 郑州 450046
2.郑州市绿色低碳化工能源材料工程技术研究中心,河南 郑州 450046
3.贵州黔希化工有限责任公司,贵州 毕节 551500
4.河南龙宇煤化工有限公司,河南 永城 476600
5.河南省中原大化集团有限责任公司,河南 濮阳 457000
6.山西沃能化工科技有限公司,山西 临汾 041000
赵立红(1981—),博士,高级工程师,研究方向为C1化学、精细化学品合成,E-mail:hncczhaolihong@163.com。
梁旭(1981—),博士,正高级工程师,研究方向为工业催化、催化材料及膜分离技术研发,E-mail:hnecliangxu@126.com;
蒋元力(1968—),博士,教授,研究方向为化学工程、精细化学品合成,E-mail:jyl@zzu.edu.cn。
收稿日期:2025-02-25,
修回日期:2025-03-31,
纸质出版日期:2025-07-25
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赵立红,梁旭,蒋元力等.H2S对Pd/α-Al2O3催化剂催化草酸二甲酯合成反应性能的影响[J].低碳化学与化工,2025,50(7):51-57.
ZHAO Lihong,LIANG Xu,JIANG Yuanli,et al.Effect of H2S on catalytic performance of Pd/α-Al2O3 catalyst for synthesis of dimethyl oxalate[J].Low-Carbon Chemistry and Chemical Engineering,2025,50(7):51-57.
赵立红,梁旭,蒋元力等.H2S对Pd/α-Al2O3催化剂催化草酸二甲酯合成反应性能的影响[J].低碳化学与化工,2025,50(7):51-57. DOI: 10.12434/j.issn.2097-2547.20250071.
ZHAO Lihong,LIANG Xu,JIANG Yuanli,et al.Effect of H2S on catalytic performance of Pd/α-Al2O3 catalyst for synthesis of dimethyl oxalate[J].Low-Carbon Chemistry and Chemical Engineering,2025,50(7):51-57. DOI: 10.12434/j.issn.2097-2547.20250071.
草酸二甲酯(DMO)是合成气制乙二醇的中间产品,工业上通常采用CO和亚硝酸甲酯(MN)在Pd/
α
-Al
2
O
3
催化剂作用下制备DMO,但是在以含CO工业尾气为原料生产DMO的过程中无法避免负荷大范围波动的问题,会出现H
2
S等毒物含量超标情况,因此探究H
2
S对催化剂的毒害影响具有重要意义。采用固定床微反装置考察了H
2
S对利用CO和MN合成DMO的Pd/
α
-Al
2
O
3
催化剂催化性能的影响。在反应温度为120 ℃、常压、
n
(CO)/
n
(MN)为2.0以及空速为3000 h
-1
条件下,H
2
S毒化处理催化剂后,其MN转化率由83%降低至64%左右。对中毒处理后的催化剂进行H
2
还原处理,发现催化剂活性进一步降低,MN转化率稳定在51%左右。采用XRD、FT-IR、HRTEM和XPS等对新鲜催化剂、中毒处理后催化剂及H
2
还原处理后催化剂进行了表征分析。结果表明,H
2
S优先与催化剂表面Pd活性物种反应生成PdSO
4
、PdO
x
-S和PdO
x
-SO
x
等惰性物种,Pd颗粒内部仍保持Pd
0
状态。H
2
还原处理会脱除掉部分表面硫,部分氧化态Pd物种重新被还原为Pd
0
,但是还原处理造成Pd
0
颗粒团聚长大。表面PdSO
4
、PdO
x
-S和PdO
x
-SO
x
等惰性物种占据并覆盖活性中心及Pd
0
团聚长大是造成催化剂催化活性下降的主要原因。
Dimethyl oxalate (DMO) is an intermediate product of syngas to ethylene glycol. In industry
DMO is typically produced via the reaction of CO and methyl nitrite (MN) over Pd/
α
-Al
2
O
3
catalyst. However
during the production of DMO using industrial tail gas
significant load fluctuations are unavoidable
and the concentration of toxic substances such as H
2
S may exceed permissible limits. Therefore
investigating the toxic effects of H
2
S on the catalyst is of critical importance. The impact of H
2
S on catalytic performance of the Pd/
α
-Al
2
O
3
catalyst for synthesis of DMO from CO and MN was examined using a fixed-bed microreactor. Under the temperature of 120 ℃
normal pressure
n
(CO)/
n
(MN) of 2.0
and the space velocity of 300
0 h
-1
after exposure to H
2
S poisoning
the conversion rate of MN decreases from 83% to about 64%. After H
2
reduction treatment on the poisoned catalyst
the MN conversion rate further decreases to about 51%. The structures of catalysts were characterized by XRD
FT-IR
HRTEM and XPS
etc. The results indicate that H
2
S preferentially reacts with palladium active species on the catalyst surface to form inert compounds such as PdSO
4
PdO
x
-S
and PdO
x
-SO
x
while the palladium particles retain Pd
0
state internally. H
2
reduction treatment removes some surface sulfur species and some oxidized Pd species are reduced back to Pd
0
. However
this reduction process induces the aggregation of Pd
0
particles. The occupation and coverage of active sites by inert species such as PdSO
4
PdO
x
-S
and PdO
x
-SO
x
along with the aggregation of Pd
0
are the main reasons for the decrease of cataltic activity of catalyst.
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