Impact of sludge density and viscosity on continuous stirred tank reactor performance in wastewater treatment by numerical modelling

IF 6.3 3区 工程技术 Q1 ENGINEERING, CHEMICAL Journal of the Taiwan Institute of Chemical Engineers Pub Date : 2025-01-01 DOI:10.1016/j.jtice.2024.105368
Praveenkumar T R , Tahani Awad Alahmadi , Saleh H. Salmen , Tikendra Nath Verma , K.K. Gupta , Beata Gavurová , Mangandan Sekar
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Abstract

Background

Wastewater treatment is crucial for maintaining a sustainable environment and managing water resources. Unprocessed wastewater contains pollutants that damage ecosystems and trigger eutrophication. The continuous stirred tank reactor plays a pivotal role in wastewater treatment due to its effective mixing, stability, and versatility. In this study, a multiphase CSTR model was developed using a numerical scheme.

Methods

The Reynolds-Averaged Navier-Stokes model was utilized for turbulence, considering two phases: water-liquid as the primary phase (Phase-1) and sludge as the secondary phase (Phase-2). Computational fluid dynamics facilitated the creation of an Eulerian model using a dispersed particle distribution approach. Four CSTR variations were explored by altering sludge density, ranging from 1200 kg/m³ to 1400 kg/m³.

Significant Findings

Adaptive mesh refinement improved result reliability and sludge dispersion near the tank walls. Mesh refinement near to the impeller is high to capture the vortices magnitude and the turbulence kinetic energy. The study highlights the pivotal role of the relationship between wastewater and microorganisms in effective treatment. Optimizing sludge density and viscosity enhances CSTR mixing efficiency. High sludge density contributes to dead zone formation within the CSTR, while increased viscosity affects overall performance. Increasing the sludge density affects the turbulent viscosity of the operating fluids. Added to above, there is significant change in the velocity distribution for the phase 2. Insights from this research contribute to understanding CSTR performance linked to impeller speed, sludge density, and viscosity for sludge of the wastewater.

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通过数值模拟研究污泥密度和粘度对污水处理中连续搅拌罐反应器性能的影响
废水处理对于维持可持续环境和管理水资源至关重要。未经处理的废水含有破坏生态系统并引发富营养化的污染物。连续搅拌槽式反应器以其有效的混合、稳定性和通用性在污水处理中起着举足轻重的作用。本文采用数值格式建立了多相CSTR模型。方法采用reynolds - average Navier-Stokes模型,考虑两相:水-液为初级相(phase 1),污泥为次级相(phase 2)。计算流体动力学促进了使用分散粒子分布方法的欧拉模型的创建。通过改变污泥密度,探索了四种CSTR变化,范围从1200 kg/m³到1400 kg/m³。重要发现:自适应网格细化提高了结果的可靠性和污泥在罐壁附近的分散。靠近叶轮的网格精密度较高,可以捕捉到旋涡大小和湍流动能。该研究强调了废水与微生物之间的关系在有效处理中的关键作用。优化污泥密度和粘度,提高CSTR混合效率。高污泥密度有助于CSTR内死区形成,而增加的粘度影响整体性能。污泥密度的增加会影响操作流体的湍流粘度。此外,阶段2的速度分布也发生了显著变化。本研究的见解有助于理解CSTR性能与叶轮转速、污泥密度和废水污泥粘度的关系。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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来源期刊
CiteScore
9.10
自引率
14.00%
发文量
362
审稿时长
35 days
期刊介绍: Journal of the Taiwan Institute of Chemical Engineers (formerly known as Journal of the Chinese Institute of Chemical Engineers) publishes original works, from fundamental principles to practical applications, in the broad field of chemical engineering with special focus on three aspects: Chemical and Biomolecular Science and Technology, Energy and Environmental Science and Technology, and Materials Science and Technology. Authors should choose for their manuscript an appropriate aspect section and a few related classifications when submitting to the journal online.
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