Integrated techno-economic and life cycle assessment of hydroformylation in microemulsion systems

Johannes Wunderlich, Philipp Kretzschmar, Reinhard Schomäcker
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Abstract

This paper presents the first integrated techno-economic and life cycle assessment of microemulsion systems being applied for rhodium-catalyzed hydroformylation of long-chain alkenes at industrial scale. The case study describes a projected 150 kt/a production of tridecanal (US gulf coast, 2019). The industrial success of the hydroformylation of short-chain alkenes lies in the continuous recycling of the rhodium-containing water phase. Microemulsion systems can be applied to transfer this concept to long-chain alkenes by overcoming the miscibility gap between the aqueous catalyst phase and the unipolar alkene phase and, moreover, by generating a temperature-induced multi-phase system enabling the immobilization of the catalyst and its continuous recycling, as demonstrated in miniplant operations with dodecene and rhodium/SulfoXantPhos. Customizable simulation models have been developed for scale-up and assessment of the miniplant data. Surprisingly, a profitability-driven sensitivity study indicates a base case optimum at low residence time with low alkene conversion leading to large throughput streams and high raw material purge rates. The comparison to the industrial cobalt-based benchmark system shows an economic advantage regarding net present value (Rh: 68 M$; Co: 62 M$), while about half of the environmental indicators are in favor or equivalent. In a best-case scenario considering zero leaching of expensive rhodium the net present value increases by almost 40% accompanied by a shift to overall lower environmental impacts than the benchmark. In conclusion, the investigated miniplant data suggest microemulsion systems to be competitive when applied in continuous processes at a large scale.
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微乳液系统中加氢甲酰化的综合技术经济和生命周期评估
本文首次对应用于工业规模长链烯烃铑催化加氢甲酰化的微乳液系统进行了综合技术经济和生命周期评估。案例研究描述了预计年产量为 150 kt/a 的十三醛生产(美国海湾沿岸,2019 年)。短链烯烃加氢甲酰化的工业成功在于含铑水相的持续循环利用。微乳液系统可以克服水相催化剂和单极烯烃相之间的混溶性差距,而且还可以生成温度诱导的多相系统,从而实现催化剂的固定化和连续循环,正如十二烯和铑/SulfoXantPhos 的微型装置操作所证明的那样,微乳液系统可以将这一概念应用于长链烯烃。为扩大规模和评估微型工厂数据,开发了可定制的模拟模型。令人惊讶的是,盈利能力驱动的敏感性研究表明,在低停留时间、低烯烃转化率的基本情况下,会产生大吞吐量流和高原料净化率,从而达到最佳效果。与以钴为基础的工业基准系统相比,该系统在净现值方面具有经济优势(Rh:6,800 万美元;Co:6,200 万美元),而大约一半的环境指标处于有利或相当的水平。在最佳情况下,考虑到昂贵铑的零浸出,净现值增加了近 40%,同时对环境的总体影响也低于基准系统。总之,所调查的微型工厂数据表明,微乳液系统在大规模应用于连续工艺时具有竞争力。
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