在微波-可见光辐照连续搅拌浆料反应器中利用预处理甘蔗渣连续生产滴入式生物燃料:反应动力学和技术-环境-经济可持续性分析

Sourav Barman and Rajat Chakraborty
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引用次数: 0

摘要

本研究利用创新的微波-可见光辐照连续搅拌淤浆反应器(MWVIS-CSSR),从预处理甘蔗渣(PSCB)中以生态友好和具有成本效益的方式连续生产滴入型生物燃料,即乙酰丙酸乙酯(EL)。此外,考虑到在磁性 Ni0.5Zn0.5Fe2O4(NZF)光催化剂与草酸-氯化胆碱基酸性深共晶溶剂(DES2)的作用下,MWVIS 可通过平行非催化和均相-异相催化途径强化 EL 的生产,该研究还制定并验证了一个新的现实动力学模型(R2 adj. ≥ 0.95)。在优化条件下(温度:100°C;NZF 负载:6 wt.% 的 PSCB;搅拌速度:500 rpm),进料流速为 35 ml/min,5 升体积的 MWVIS-CSSR 可产生最高 54.7 mol% 的 EL 收率(选择性:97.85%)。值得注意的是,与单独的 MW(29.45 摩尔%)和 VIS(20.1 摩尔%)体系相比,MW 和 VIS 辐照的协同作用大大提高了 EL 的产量(54.7 摩尔%)。与参考混合物(B10 和 B20)相比,优化生产的 EL 与 B10 和 B20(10% 和 20%的生物柴油-柴油混合物)混合 5 Vol%时,除了能减少 21-22% 的 HC 和 7.5-20% 的 CO 发动机废气排放外,还能提高断裂热效率(1-2%)。值得注意的是,基于 MW 的渗透深度以及 NZF 和 DES2 的 VIS 能量进行的反应器放大研究表明,5 升 MWVIS-CSSR 有可能放大到 1 立方米的容积,而甘蔗渣到 EL 的转化过程可放大到 2000 公斤/小时的处理能力。此外,在 Aspen Plus 软件中进行的工艺模拟,利用基于 COSMO 的属性估计和 DFT 计算,以及技术经济分析,显示出 54.25% 的稳健内部收益率和 8.22E+05 美元的净现值,投资回收期为 4.91 年。此外,对 MWVIS-CSSR 可持续电解质生产工艺的环境影响分析研究表明,与单独的 MW-CSSR 和 VIS-CSSR 反应器系统相比,海洋生态毒性降低了 40-60%,人体毒性降低了 39-61%。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Continuous drop-in-biofuel production from pretreated sugarcane bagasse in a microwave-visible irradiated continuous stirred slurry reactor: reaction kinetics & techno-enviro-economic sustainability analyses†

Continuous drop-in-biofuel production from pretreated sugarcane bagasse in a microwave-visible irradiated continuous stirred slurry reactor: reaction kinetics & techno-enviro-economic sustainability analyses†

This work utilizes an innovative microwave-visible irradiated continuous stirred slurry reactor (MWVIS-CSSR) for sustainable continuous production of a drop-in biofuel, namely, ethyl levulinate (EL), from pretreated sugarcane bagasse (PSCB). Besides, a novel realistic kinetic model, considering MWVIS intensified EL production through parallel non-catalytic and homogeneous–heterogeneous catalytic pathways in the presence of a magnetic Ni0.5Zn0.5Fe2O4 (NZF) photocatalyst in conjunction with an oxalic acid–choline chloride based acidic deep eutectic solvent (DES2), was also formulated and validated (R2 adj. ≥ 0.95). The 5 liter volume MWVIS-CSSR could render maximum 54.7 mol% EL yield (selectivity: 97.85%) at a feed flow rate of 35 ml min−1 under optimized conditions (temperature: 100 °C, NZF loading: 6 wt% PSCB, stirring speed: 500 rpm). Remarkably, the synergistic impact of MW and VIS irradiation substantially elevated the EL yield (54.7 mol%) compared to those of the individual MW (29.45 mol%) and VIS (20.1 mol%) systems. The optimally produced EL when blended at 5 vol% with B10 and B20 (10% and 20% biodiesel–diesel blends) could enhance the brake thermal efficiency (1–2%) besides mitigating 21–22% HC and 7.5–20% CO engine exhaust emissions in comparison with reference blends (B10 and B20). Notably, the reactor scale-up study based on the penetration depth of the MW and VIS energy of NZF and DES2 showcased the potential to upscale the 5 liter MWVIS-CSSR to a 1 m3 volume, allowing EL production to reach 689 kg h−1 with a sugarcane bagasse processing capacity of 2000 kg h−1. Moreover, the process simulation conducted in Aspen Plus software, utilizing COSMO-based property estimation with DFT calculations, alongside the techno-economic analysis, revealed a robust internal rate of return (IRR) of 54.25% and a net present value (NPV) of 8.22 × 105 US$ with a payback period of 4.91 years. Additionally, the environmental impact analysis study for the scaled-up EL production process in the MWVIS-CSSR revealed a reduction of 40–60% in marine ecotoxicity and 39–61% in human toxicity compared to the separate MW-CSSR and VIS-CSSR systems.

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