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氧化吸收工艺尾气焚烧炉中SO_(3)生成动力学北大核心CSCD
引用本文:赵西,谢武君,李金金,常宏岗,陈世明,丁桐.氧化吸收工艺尾气焚烧炉中SO_(3)生成动力学北大核心CSCD[J].石油与天然气化工,2023,52(4):1-8.
作者姓名:赵西  谢武君  李金金  常宏岗  陈世明  丁桐
作者单位:中国石油西南油气田公司天然气研究院;国家能源高含硫气藏开采研发中心;中国石油西南油气田公司开发处
基金项目:中国石油西南油气田公司博士后项目“克劳斯尾气氧化吸收工艺焚烧炉中硫化物燃烧动力学研究”(B202120);中国石油天然气股份有限公司科学研究与技术开发项目“含硫天然气硫磺回收及氧化吸收尾气处理关键技术研究(2021DJ2603)
摘    要:目的研究采用氧化吸收工艺的硫磺回收装置尾气焚烧炉操作参数和气体条件变化对SO_(3)生成的影响,以减少尾气焚烧炉中SO_(3)的生成。方法在实验室中利用管式炉模拟尾气焚烧炉研究SO_(3)的生成,采用控制冷凝法测定反应管出口气体中SO_(3)含量。仅在气相条件下研究不同工况和气质条件对SO_(3)生成的影响。结果SO_(2)和O_(2)体积分数增加会增加SO_(3)体积分数,SO_(3)体积分数与反应气体停留时间呈线性关系,在反应体系中引入CS2也能明显提高SO_(3)体积分数,但对SO_(3)生成率无明显影响;反应体系中引入少量CH4也会明显提高体系中SO_(3)体积分数,并提高SO_(3)生成率。结论明确了SO_(3)生成情况与尾气焚烧炉操作参数和气质条件的关系。SO_(3)生成对反应物SO_(2)和O_(2)的反应级数分别为0.87和0.45,SO_(2)氧化过程的表观活化能为69.04 kJ/mol。

关 键 词:含硫尾气  氧化吸收  尾气焚烧  SO_(3)  控制冷凝法
收稿时间:2023/3/22 0:00:00

Kinetics of SO3 formation in the tail gas incinerator of oxidized absorption technology
Zhao Xi,Xie Wujun,Li Jinjin,Chang Honggang,Chen Shiming,Ding Tong.Kinetics of SO3 formation in the tail gas incinerator of oxidized absorption technology[J].Chemical Engineering of Oil and Gas,2023,52(4):1-8.
Authors:Zhao Xi  Xie Wujun  Li Jinjin  Chang Honggang  Chen Shiming  Ding Tong
Affiliation:Research Institute of Natural Gas Technology, PetroChina Southwest Oil & Gasfield Company, Chengdu, Sichuan, China;National Energy R&D Center of High Sulfur Gas Exploitation, Chengdu, Sichuan, China;Gas Field Development and Management Department, PetroChina Southwest Oil & Gasfield Company, Chengdu, Sichuan, China
Abstract:ObjectiveThe aim is to reduce the formation of SO3 in the tail gas incinerator by analyzing the effects of operating parameters and gas conditions on the formation of sulfur trioxide(SO3) in the tail gas incinerator of sulfur recovery unit using oxidation absorption process. Methods In the laboratory, the formation of SO3 was studied by using tube furnace to simulate tail gas incinerator, and the content of SO3 in the outlet gas of reaction tube was determined by controlled condensation method. The effects of different working conditions and gas conditions on SO3 formation were studied only under gas phase conditions. ResultsThe increase of SO2 and O2 volume fraction would increase the SO3 volume fraction, and the SO3 volume fraction had a linear relationship with the residence time of the reaction gas. The introduction of CS2 in the reaction system could also significantly increase the SO3 volume fraction, but had no significant effect on the SO3 formation rate. A tiny proportion of CH4 in the gas had significant effect on the SO3 volume fraction in the system and increase the SO3 formation rate. ConclusionsIt is clarified the relationship between SO3 formation and operating parameters and gas quality conditions of tail gas incinerator. The reaction orders of SO3 formation to SO2 and O2 were 0.87 and 0.45, respectively. The apparent activation energy of SO2 oxidation process was 69.04 kJ/mol.
Keywords:sulfur-containing tail gas  oxidation absorption  tail gas incineration  sulfur trioxide  controlled condensation method
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