KAJIAN TEKNO EKONOMI PRODUKSI BAHAN PROPILENA GLIKOL BERBASIS BIOMASSA VIA HIDROGENOLISIS GLISEROL

Galuh Wirama Murti, A. Darmawan, Nesha Adelia, Nilasari, Dorit Bayu Islam Nuswantoro
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Abstract

Governmental policies that promote biofuels such as biodiesel have led to the generation a largeamounts of glycerol waste as a low-cost raw material. The purpose of this paper is to present a technoeconomic study on the production of biomass-based propylene glycol via glycerol hydrogenolysis,considering hydrogen feeds that partially or fully utilize renewable sources. For analysis andcalculation, computer simulations are carried out using the Aspen Hysys V11 simulator. The technoeconomic analysis is performed by modelling the propylene glycol synthesis process from glycerol,which is then used to calculate the facility capital cost and estimate operating costs to obtain an annualreturn on investment. Sensitivity analysis is also conducted for several parameters on a 36,000ton/year propylene glycol plant. The results showed the production cost was 0.76 USD/kg or 10,802IDR/kg when the hydrogen is generated from the natural gas steam-methane reforming (SMR)process. If the hydrogen is produced from the glycerol steam reforming process, which is fullyrenewable, the plant is not feasible, as indicated by a negative net present value (NPV).
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这是一项经济技术,通过水原甘油生产生物质素乙二醇
政府推广生物燃料(如生物柴油)的政策导致了作为低成本原材料的甘油废料的大量产生。本文的目的是在考虑部分或全部利用可再生能源的氢原料的情况下,通过甘油氢解生产生物质基丙二醇的技术经济研究。为了进行分析和计算,使用Aspen Hysys V11模拟器进行了计算机模拟。技术经济分析是通过模拟甘油合成丙二醇的过程来进行的,然后用于计算设施的资本成本和估计运营成本,以获得年度投资回报。并对36000吨/年丙二醇装置的几个参数进行了敏感性分析。结果表明,天然气蒸汽-甲烷重整制氢的生产成本为0.76美元/kg (10802 idr /kg)。如果氢气是由甘油蒸汽重整过程产生的,这是完全可再生的,那么工厂是不可行的,正如负净现值(NPV)所表明的那样。
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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