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Retrofit design of a pharmaceutical batch process improving green process chemistry engineering principles

机译:改造制药批处理工艺设计改善绿色工艺化学和工程原则

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Rapid globalization during the last decades and increasing regulatory efforts from governments forced the chemical industry to meet up the rising concern about sustainability aspects of chemical process design. Besides these non-monetary issues, the economic performance is still a very crucial aspect of design. Therefore, considering the capital intensive nature of chemical industry, redesign of existing production plants has been recently regarded as a key strategic decision. This retrofitting task has been extensively performed in continuous processes for the production of bulk chemicals, however in the case of batch processes and specialty chemicals only few studies address the importance of retrofitting, especially including multi-criteria sustainability assessment. The objective of this paper is to address retrofitting actions to enhance both monetary and non-monetary aspects of chemical process design. This is done using a systematic Path Flow Decomposition (PFD) method, multi-dimensional process assessment indicators, heuristics, and model based methodologies for generation of design alternatives. In this study a set of Environmental, Health, and Safety (EHS) hazard assessment and Life Cycle Impact Assessment (LC1A) indicators is newly introduced in the PFD method and evaluated in parallel with previously developed indicators. This set of indicators has been associated with a set of heuristics based on hazard and life cycle impact assessment rules and established principles of green chemistry and engineering. The developed methodology is applied to an existent batch production plant from pharmaceutical industry by addressing three process flowsheet structural alternatives for waste solvent management, pressure swing distillation, extractive distillation, and extraction for the separation of the THF/Water azeotrope. It is found that the suggested structural alternatives result in improved EHS, LCIA, and cost metrics compared to the base case of solvent incineration.
机译:在过去几十年中,快速全球化以及增加政府的监管努力迫使化学工业促进了化学工艺设计可持续发展方面的上升担忧。除了这些非货币问题之外,经济绩效仍然是一个非常重要的设计方面。因此,考虑到化学工业的资本密集型性质,最近被视为一个关键的战略决策。这种改造任务已经广泛地在连续生产散装化学物质的过程中进行,然而,在批处理过程中,特种化学品只有很少的研究解决了改造的重要性,特别是包括多标准可持续性评估。本文的目的是解决改造行动,以提高化学过程设计的货币和非货币方面。这是使用系统路径流分解(PFD)方法,多维过程评估指标,启发式和基于模型的设计方法来完成的。在本研究中,在PFD方法中新引入了一套环境,健康和安全(EHS)危险评估和生命周期影响评估(LC1A)指标,并与先前开发的指标并行评估。这套指标与基于危险和生命周期影响评估规则的一套启发式有关,并建立了绿色化学与工程的原则。通过寻址用于废物溶剂管理,压力蒸馏,萃取蒸馏和分离的三种工艺流程结构替代品,将开发方法应用于制药工业的存在的批量生产厂,用于分离THF /水共沸物的分离。结果发现,与溶剂焚烧的基本情况相比,建议的结构替代方案导致改善的EHS,LCIA和成本度量。

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