Zhang Guangwen, Zheng Yi, Dong Yong Zhao
State Key Laboratory of Chemicals Safety, Qingdao 266071, P. R. China.
SINOPEC Research Institute of Safety Engineering Company, Limited Qingdao 266071, P. R. China.
ACS Omega. 2024 May 1;9(19):21260-21269. doi: 10.1021/acsomega.4c01346. eCollection 2024 May 14.
Natural gas generates varying concentrations of HS during natural formation and extraction, and HS leak accidents are frequent, posing a significant threat to the safety of human life and the environment. Conventional treatment technology equipment is large and does not meet the emergency requirements of the complex topographical gas field. This study aimed to design a pilot-scale method coupling the venturi and bubbling reactors to reduce equipment size and improve emergency capabilities for the absorption of leaked HS. It found that the ring system self-priming venturi reactor, which was suitable only for the coarse treatment of toxic gases, maintained an absorption efficiency of around 50% under most operating conditions, with substantial variations due to changes in process parameters, but that redundancy of the bubbling reactor was high. With the synergistic effect of venturi and bubbling, the coupling process had an extremely high absorption efficiency, basically more than 95%. The experiments also showed that the HS concentration at the outlet of the venturi-bubbling reactor increased with increasing inlet gas concentration and gas volume. The absorption performance improved significantly on increasing Fe concentration; it increased first and then remained constant, and the optimum Fe concentration for the absorption of leaked HS was 21 000 mg/m. The absorption performance decreased with increasing submergence height and then remained stable after the size of the inlet approached 600 mm, whereas the overall absorption efficiency of the venturi-bubbling reactor remained constant. The optimum operating temperature range was 10 °C-50 °C. The experimental system kept the outlet concentration below the emergency discharge standard for a continuous period of 48 h following practical use in the gas field and resulting in significant enhancement in mass transfer performance, fully satisfying the emergency requirements.
天然气在自然形成和开采过程中会产生不同浓度的硫化氢,硫化氢泄漏事故频发,对人类生命安全和环境构成重大威胁。传统处理技术设备体积庞大,无法满足复杂地形气田的应急需求。本研究旨在设计一种将文丘里反应器和鼓泡反应器耦合的中试规模方法,以减小设备尺寸并提高对泄漏硫化氢的吸收应急能力。研究发现,仅适用于有毒气体粗处理的环形系统自吸式文丘里反应器在大多数运行条件下保持约50%的吸收效率,因工艺参数变化而有较大波动,但鼓泡反应器的冗余度较高。在文丘里和鼓泡的协同作用下,耦合工艺具有极高的吸收效率,基本超过95%。实验还表明,文丘里-鼓泡反应器出口处的硫化氢浓度随进气浓度和气体体积的增加而增加。随着铁浓度的增加,吸收性能显著提高;先增加后保持恒定,吸收泄漏硫化氢的最佳铁浓度为21000mg/m。吸收性能随淹没高度的增加而降低,在入口尺寸接近600mm后保持稳定,而文丘里-鼓泡反应器的整体吸收效率保持不变。最佳运行温度范围为10℃-50℃。该实验系统在气田实际应用后连续48小时将出口浓度保持在应急排放标准以下,传质性能显著增强,完全满足应急需求。