Preliminary reactor design for gold nanoparticle production by the Turkevich method on an industrial scale

Thyta Medina Salsabila Erlangga, A. Nandiyanto, R. Ragadhita
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Abstract

This study aims to design and analyze the design of a batch-type reactor to optimize the production of gold nanoparticles on an industrial scale. The method used in the design of this reactor is the computational analysis of the reactor calculations, including stirring and mass balance as initial calculations using the Microsoft Excel application manually. The calculation results show that the designed reactor specifications have a reactor volume of 21.7335 ft3, cylinder height of 13.4612 in, a height of solution in the cylinder of 8.9046 in, vessel diameter of 73.2984 in, design pressure of 9.9978 psig, impeller length of 9.1840 in, shaft length of 10.5418 in, with stirring power 62.5228 Hp. Reactor design analysis is an important stage in the design of production processes on an industrial scale, where the specification results from the designed reactor can be used not only to adjust the reactor to the product but also to be used as a reference for production costs. The results of computational analysis and calculations performed on the reactor design in this study can be used as a reference and can be applied in the design of reactor performance analysis as a learning media, including operating mechanisms in the production process.
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工业规模上Turkevich法生产金纳米颗粒的初步反应器设计
本研究旨在设计和分析间歇式反应器的设计,以优化工业规模的金纳米颗粒生产。本反应器设计采用的方法是对反应器计算进行计算分析,包括搅拌和质量平衡作为初始计算,使用Microsoft Excel应用程序手动进行。计算结果表明,设计反应器规格反应器体积为21.7335 ft3,筒体高度为13.4612 in,筒体内溶液高度为8.9046 in,容器直径为73.2984 in,设计压力为9.9978 psig,叶轮长度为9.1840 in,轴长为10.5418 in,搅拌功率为62.5228 Hp。反应器设计分析是工业规模生产工艺设计的一个重要阶段,设计出的反应器规格不仅可以用于调整反应器以适应产品,还可以作为生产成本的参考。本研究对反应器设计进行的计算分析和计算结果可作为参考,可作为学习媒介应用于反应器性能分析的设计,包括生产过程中的操作机制。
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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