Rücker Theresa, Pettersen Torbjørn, Graute Hannah, Wittgens Bernd, Graßl Tobias, Waldvogel Siegfried R
Process Technology, SINTEF Industry, Trondheim, Trøndelag NO-7465, Norway.
Max Planck Institute for Chemical Energy Conversion, Stiftstraße 34-36, 45470 Mülheim an der Ruhr, Germany.
ACS Sustain Chem Eng. 2024 Jul 18;12(30):11283-11296. doi: 10.1021/acssuschemeng.4c02898. eCollection 2024 Jul 29.
A pilot scale plant at Technology Readiness Level (TRL) 6 comprising an electrochemical ex-cell continuous production of sodium peroxodicarbonate and a thermal depolymerization plug flow reactor for kraft lignin conversion is established. Due to the labile nature of the "green" oxidizer peroxodicarbonate, special attention must be paid to the production parameters in order to optimize its use. A simplified design model describing steady-state and transient operations is formulated and finally validated against experimental data from the electrolysis setup. Design trade-offs are visualized, and their impact on specific energy consumption is evaluated. The pilot plant was operated for a 20-month period for more than 1200 h on-stream. Optimized process conditions result in vanillin yields of 8 wt % and thus prove the successful scale-up.
建立了一个处于技术就绪水平(TRL)6的中试工厂,该工厂包括用于连续电化学生产过氧二碳酸钠的外部电池以及用于木质素转化的热解聚活塞流反应器。由于“绿色”氧化剂过氧二碳酸钠的性质不稳定,必须特别关注生产参数以优化其使用。制定了一个描述稳态和瞬态操作的简化设计模型,并最终根据来自电解装置的实验数据进行了验证。可视化了设计权衡,并评估了它们对特定能耗的影响。中试工厂运行了20个月,连续运行超过1200小时。优化的工艺条件使香草醛产率达到8 wt%,从而证明了成功的放大。