喷流式加压管状微气泡发生器的气体溶解性能和气泡生成特性研究

IF 8.1 1区 工程技术 Q1 ENGINEERING, CHEMICAL Separation and Purification Technology Pub Date : 2024-09-25 DOI:10.1016/j.seppur.2024.129886
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引用次数: 0

摘要

目前,海上油田采出水气浮处理装置的性能不稳定,而微气泡生成技术有望显著提高其分离效率。在这项研究中,我们开发了一种射流式加压管状微气泡发生器,由一个射流溶解气体管(JDGT)和一个标准球阀组成。JDGT 的设计原理是通过射流喷嘴强化气泡破裂,并通过上下循环涡流加强气体溶解。我们提出了一种创新的计算流体动力学(CFD)模型,利用用户定义函数(UDF)来预测管内的流动模式和溶解氧(DO)分布。数值模拟与实验结果之间的相对误差为 5.25%。在相同的操作条件下,JDGT 可以在 3.5 秒内高效地产生气溶水,溶气效率达到 80.24%,而水力停留时间为 30 秒的传统垂直喷射容器的溶气效率为 58.31%。氧气体积传质系数随进水流速、气液体积比和溶解压力的增加而增加。随着进水流量的增加,萨特平均气泡直径最初会增大,然后减小。气液体积比和溶解气体压力与萨特平均气泡直径呈指数关系。处理能力为 35 立方米/小时的工程原型在南海的一个平台上成功进行了现场测试。试验结果表明,当微气泡发生器连接到带有 10% 回流流量系统的垂直气浮装置时,装置出口处的平均油类浓度为 13 mg/L。计算得出的平均除油效率为 72.38%,比不使用管式微气泡发生器时的除油效率高 12.8%。
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Study on the gas dissolution performance and bubble generation characteristics of a jet flow type pressurized tubular microbubble generator
Microbubble generation technology has the potential to significantly enhance the separation efficiency of offshore oilfield produced water flotation treatment devices, which currently display unstable performance. In this study, we developed a jet flow type pressurized tubular microbubble generator, comprising a jet-dissolved gas tube (JDGT) and a standard ball valve. The JDGT was designed based on the principle of intensifying bubble breakup through jet nozzles and enhancing gas dissolution via up-down circulation vortex. We proposed an innovative Computational Fluid Dynamics (CFD) model that utilizes User Defined Functions (UDF) to predict the flow pattern and dissolved oxygen (DO) distribution within the tube. The relative error between numerical simulations and experimental results was 5.25 %. Under identical operating conditions, the JDGT can efficiently produce gas-dissolved water in 3.5 s, achieving a dissolved gas efficiency of 80.24 %, compared to 58.31 % for a conventional jet vertical vessel with a hydraulic retention time of 30 s. High-quality microbubbles can be generated through decompression via a standard ball valve. The oxygen volumetric mass transfer coefficient increases with the inlet water flow rate, the gas–liquid volume ratio, and increased dissolved pressure. As the inlet water flow rate increases, the Sauter mean bubble diameter initially increases before decreasing. Both the gas–liquid volume ratio and dissolved gas pressure are exponentially related to the Sauter mean bubble diameter. An engineering prototype with a treatment capacity of 35 m3/h was successfully field-tested on a platform in the South China Sea. The test results indicated that when the microbubble generator was connected to a vertical air flotation unit with a 10 % reflux flow system, the average oil concentration at the unit’s outlet was 13 mg/L. The calculated average oil removal efficiency was 72.38 %, which is 12.8 % higher than that achieved without a tubular microbubble generator.
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来源期刊
Separation and Purification Technology
Separation and Purification Technology 工程技术-工程:化工
CiteScore
14.00
自引率
12.80%
发文量
2347
审稿时长
43 days
期刊介绍: Separation and Purification Technology is a premier journal committed to sharing innovative methods for separation and purification in chemical and environmental engineering, encompassing both homogeneous solutions and heterogeneous mixtures. Our scope includes the separation and/or purification of liquids, vapors, and gases, as well as carbon capture and separation techniques. However, it's important to note that methods solely intended for analytical purposes are not within the scope of the journal. Additionally, disciplines such as soil science, polymer science, and metallurgy fall outside the purview of Separation and Purification Technology. Join us in advancing the field of separation and purification methods for sustainable solutions in chemical and environmental engineering.
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