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This study presents the design, fabrication, and performance evaluation of a batch reactor for the hydrothermal valorization of coffee and peapod waste biomass. The reactor, designed using Inventor 2023 and analyzed using ANSYS 2023, is capable of operating at elevated temperatures to facilitate the breakdown of lignocellulosic structures and promote the extraction of valuable platform chemicals. Based on the design, the reactor was manufactured, and a set of experiments was performed to test it at different temperatures ranging from 120 to 180 °C, at different times (1–4 h) and with different types of biomass (peapods and coffee cherry waste). The results demonstrate the effectiveness of the reactor in optimizing the conversion of agricultural waste into key compounds such as hydroxymethylfurfural (HMF) and furfural. For peapod biomass, optimal conditions were identified at temperatures between 150 °C and 180 °C, with a reaction time of approximately 1 h yielding up to 72.17%wt total platform chemicals. Coffee cherry biomass showed a different yield profile, with total platform chemical yields reaching 23.56%wt at 180 °C after 4 h of treatment, highlighting the importance of feedstock-specific optimization. The reactor’s performance indicates its potential for broader applications in the conversion of various lignocellulosic feedstocks into high-value chemicals, contributing to a more sustainable and circular economy. The presented design and analysis demonstrate the reactor’s compliance with necessary characteristics such as temperature, deformation, and stress, ensuring its suitability for the experiments. This study showcases the importance of innovative reactor design in advancing sustainable chemical production from biomass waste, making it a valuable contribution to the field of waste-to-value conversion technologies.

Hydrothermal processing has emerged as a promising clean technology for managing the substantial amounts of agro-industrial waste generated worldwide. This study aims to introduce a clean technology approach to biomass valorization processes by exploring the hydrothermal conversion of two distinct biomass feedstocks, peapods and coffee cherries, into valuable platform chemicals through the use of homogeneous acid catalysts. The hydrothermal valorization experiments were conducted in a 500 mL reactor at 180 °C for 1 h with a 1:20 biomass–acid solution ratio, utilizing a set of organic and inorganic acids as catalysts. The chemical compositions of the biomass feedstocks were analyzed, revealing significant differences in their cellulose (20.2 wt% in peapods; 27.6 wt% in coffee cherries), hemicellulose (17.4 wt% in peapods; 12.5 wt% in coffee cherries), and lignin (5.0 wt% in peapods; 13.7 wt% in coffee cherries) contents. Without the use of catalysts, peapods yielded 45.128 wt% platform chemicals, outperforming coffee cherries, which produced 32.598 wt%. The introduction of various acid catalysts influenced the yields and selectivity of platform chemicals. Sulfuric acid enhanced sugar production, yielding 62.936 wt% from peapods and 51.236 wt% from coffee cherries. Hydrochloric acid selectively favored sugar production but resulted in decreased overall yields. Nitric acid facilitated the conversion of both biomass types, yielding 35.223 wt% from coffee cherries and 40.315 wt% from peapods. Adipic acid achieved the highest overall yields, with 53.668 wt% for coffee cherries and 65.165 wt% for peapods, while also increasing levulinic acid production. Acetic acid significantly increased sugar yields, which reached 50.427 wt% with peapods. The findings highlight the potential of hydrothermal valorization as a clean technology for biomass conversion and underscores the importance of tailoring catalyst selection and process conditions to optimize the valorization of biomass feedstocks.

The management of coffee and peapod waste presents significant environmental challenges, with millions of tons generated annually, leading to disposal issues and resource inefficiencies. Hydrothermal processes offer a promising valorization method, though biomass characteristics significantly influence the resulting products. Biomass characterization revealed distinct profiles for coffee cherry waste (moisture: 10.94%, ashes: 7.79%, volatile matter: 79.91%, fixed carbon: 1.36%, cellulose: 27.6%, hemicellulose: 12.5%, and lignin: 13.7%) and peapods (moisture: 7.77%, ashes: 4.22%, volatile matter: 74.18%, fixed carbon: 13.0%, cellulose: 20.2%, hemicellulose: 17.4%, and lignin: 5.0%). Experiments were conducted in 100 mL and 500 mL hydrothermal reactors with varying conditions for temperature (120–260 °C), time (1–4 h), stirring (none and at 5000 and 8000 rpm), biomass/water ratio (1:5, 1:10, 1:20, and 1:40), particle size (0.5–5 mm), and catalysts (acids and bases). The results showed that peapods produced over 30 times more platform chemicals than coffee. High temperatures (over 180 °C) degraded peapods, whereas coffee yields increased. Both biomasses were influenced similarly by reaction conditions: lower biomass/water ratios, smaller particle sizes, acid catalysts, and no stirring increased yields. Peapods consistently had higher yields than coffee in all conditions. Biochar analysis revealed anthracite from coffee and coal from peapods.