Design of heat exchanger for producing nickel ferrite (NiFe2O4) nanoparticles using coprecipitation method

Sifa Aulia Rahma, A. Nandiyanto, Teguh Kurniawan
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Abstract

This study examines the design of a heat exchanger (HE) in the production process of nickel ferrite (NiFe2O4) nanoparticles using the coprecipitation method by determining the shell and tube heat exchanger. The Microsoft Excel application is used as a manual calculating machine to facilitate the analysis of heat exchanger (HE) data calculations. The research flowchart starts with a literature study, preparation of tools and materials for design, calculation of the main shell and tube components, and then fabrication. Based on the calculation results, the design specification data for a shell and tube heat exchanger has a shell diameter of 0.032 m, a shell length of 4.267 mm, a thickness of 0.002 m with an initial heat transfer rate (Q) of 460130 W resulting in a heat transfer efficiency of 95.706% and an NTU of 6.165. The high effectiveness value makes the design of the one shell and tube type turbulent flow heat exchanger (HE) considered to have met the standards of high effectiveness and good performance. The design and design process is complete if the device functions properly. This study can be used as a reference for researchers in designing heat exchangers during production to make them more effective, reliable, and economical.
共沉淀法制备纳米铁酸镍(NiFe2O4)的换热器设计
本研究通过确定管壳式换热器,考察了采用共沉淀法生产铁酸镍纳米颗粒(NiFe2O4)过程中换热器的设计。使用Microsoft Excel应用程序作为人工计算机器,方便对换热器(HE)数据进行分析计算。研究流程从文献研究开始,准备设计工具和材料,计算主要壳管部件,然后制造。计算结果表明,管壳式换热器的设计规范数据为:管壳直径为0.032 m,管壳长度为4.267 mm,管壳厚度为0.002 m,初始换热率Q为460130 W,换热效率为95.706%,NTU为6.165。高的效率值使得单管壳式紊流换热器的设计达到了高效、高性能的标准。如果设备功能正常,则表示设计和设计过程已经完成。研究结果可为生产过程中换热器的设计提供参考,使换热器更加高效、可靠、经济。
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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