Shell and tube heat exchanger design for production graphene oxide nanoparticles from agricultural waste

Diah Indriati, A. Nandiyanto, M. Fiandini, R. Ragadhita, Teguh Kurniawan
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Abstract

Heat exchangers are used to transferring energy (heat), using fluids or gases, both hot and cold, from one area to another due to temperature differences. Almost all agricultural wastes serve as carbon products which are essential to produce graphene oxide, it is very possible to get graphene oxide by synthesizing it from agricultural waste which is expected to reduce the amount of waste on the earth. After carrying out the synthesis, it is necessary to test the characterization of the resulting product. The characterization stage requires a sintering process (20oC to 98oC) until the product is completely solidified. This research aims to design a heat exchanger that is highly effective in assisting the sintering process. For the design to be well-directed, several things must be done, such as calculating the main components (shell and tube) and designing a heat exchanger. Based on the TEMA standard and the use of simple calculations that refer to the attached calculation formula using Ms. Excel, hot and cold fluids used in this heat exchanger design are ethylene glycol and water. The length of the shell and tube as a whole is 5 m, the inner and outer shell diameters are 254 mm and 279.4 mm; the inner and outer tube diameters are respectively 22.09 mm and 25.40 mm. The calculation results show an excellent design effectiveness value of 86.14%. Continuous innovation in the design and materials of the heat exchanger can increase the effectiveness value to close to 100% so that it can help the graphene oxide synthesis process to make it cheaper and more efficient.
壳管式热交换器设计用于从农业废弃物中生产氧化石墨烯纳米颗粒
热交换器是用来传递能量(热),使用流体或气体,热的和冷的,从一个区域到另一个由于温差。几乎所有的农业废弃物都是生产氧化石墨烯所必需的碳产品,利用农业废弃物合成氧化石墨烯是很有可能的,有望减少地球上的废物量。在进行合成后,有必要对所得产物的表征进行测试。表征阶段需要烧结过程(20℃至98℃),直到产品完全固化。本研究旨在设计一种高效辅助烧结过程的热交换器。为了使设计有针对性,必须做几件事,例如计算主要部件(壳和管)和设计换热器。根据TEMA标准,并使用Ms. Excel进行简单计算,参考附件中的计算公式,本换热器设计中使用的热流体和冷流体为乙二醇和水。管壳整体长度为5m,内外壳直径分别为254 mm和279.4 mm;内径22.09 mm,外径25.40 mm。计算结果表明,设计有效性值为86.14%。换热器在设计和材料上的不断创新,可以将有效性值提高到接近100%,从而帮助氧化石墨烯合成工艺使其更便宜,更高效。
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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