Zeolite-Y-catalyst production from locally sourced Meta-kaolin: Computer-Aided scale-up process design and economic analysis with Monte-Carlo-Simulation

Emmanue Olusola Oke , Kazeem Kolapo Salam , Titilayo Deborah Oluwole , Aru Eze Okere , Nnabodo Darlington , Kehinde Ayoola Babatunde , Yahya Umar , Suliyat Omolara Ibrahim
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Abstract

Production of zeolite-Y catalyst from natural substrate has been a research trend in the scientific community. Published articles revealed that zeolite-Y recovery from locally sourced metakaolin is confined to laboratory practice. Scale-up process design and its economic feasibility for zeolite-Y catalyst recovery are rarely found in the scientific bibliography. Therefore, this study presented conceptual scale-up process design, base-case techno-economics and Monte-Carlo simulation of zeolite Y recovery from Nigerian metakaoline. ASPEN Base Case Simulation (ABCS), scale-up design and economics were accomplished using inherent design and costing algorithms in ASPEN Batch Process Developer (ABPD) V10. Process economic parameters: Net Present Value (NPV), Internal Rate of Return (IRR), Return on Investment (ROI) and Payback Time (PBT), were modelled and optimized using Design Expert V13 software; while zeolite Unit Production Cost (UPC), Annual Production Cost (APC), Total Capital Investment (TCI) and interest/discount rate were considered as model inputs. Monte-Carlo Simulation (MCS) in Crystal Ball Oracle software was used to perform the sensitivity and uncertainty analyses. The base-case techno-economic results of process design of 600,000 kg/year zeolite production gave batch size 5000 kg/batch with 104 batches/year, batch time (4149 min), TCI ($15,930,306), APC ($147,145), NPV ($41,983,375), ROI (38.13 %) and PBT (2.14 years). The coefficient of determination (R2) of the economic models were 0.9978, 0.9989 and 0.9986 for NPV, ROI and IRR respectively. The optimum economic variables that maximized synthesis of 5000 kg/batch zeolite Y are UPC ($11.68), APC ($100,033) and TPC ($15,930,200). MCS uncertainty for NPV, IRR and ROI are negligible. Therefore, this study demonstrated that scale-up zeolite-Y production from the local substrate is economically feasible.

Abstract Image

利用本地 Meta-kaolin 生产沸石-Y 催化剂:计算机辅助放大工艺设计和蒙特卡洛模拟经济分析
利用天然基质生产沸石-Y 催化剂一直是科学界的研究趋势。已发表的文章显示,从本地来源的偏高岭土中回收沸石-Y 仅局限于实验室实践。沸石-Y 催化剂回收的放大工艺设计及其经济可行性在科学文献中很少见。因此,本研究介绍了从尼日利亚偏高岭土中回收沸石 Y 的概念性放大工艺设计、基础案例技术经济学和蒙特卡洛模拟。利用 ASPEN Batch Process Developer (ABPD) V10 中固有的设计和成本计算算法,完成了 ASPEN Base Case Simulation (ABCS)、放大设计和经济学分析。工艺经济参数使用 Design Expert V13 软件对净现值 (NPV)、内部收益率 (IRR)、投资回报率 (ROI) 和投资回收期 (PBT) 进行建模和优化;同时将沸石单位生产成本 (UPC)、年生产成本 (APC)、总资本投资 (TCI) 和利息/贴现率作为模型输入。Crystal Ball Oracle 软件中的蒙特卡洛模拟(MCS)用于进行敏感性和不确定性分析。年产 600,000 公斤沸石的工艺设计的基础案例技术经济结果为:批量 5000 公斤/批,104 批/年,批次时间(4149 分钟),TCI(15,930,306 美元),APC(147,145 美元),NPV(41,983,375 美元),投资回报率(38.13%)和 PBT(2.14 年)。经济模型的净现值、投资回报率和内部收益率的决定系数(R2)分别为 0.9978、0.9989 和 0.9986。能最大化合成 5000 公斤/批次沸石 Y 的最佳经济变量是 UPC(11.68 美元)、APC(100,033 美元)和 TPC(15,930,200 美元)。净现值、内部收益率和投资回报率的 MCS 不确定性可忽略不计。因此,本研究表明,利用当地基质扩大沸石-Y 的生产规模在经济上是可行的。
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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