Solid-liquid separation of lignocellulosic sugars from biomass by rotating ceramic disc filtration

• Published in: Green chemistry : an international journal and green chemistry resource : GC 2024-11, Vol.26 (23), p.11587-11599
• Main Authors: Saboe, Patrick O, Li, Yudong, Tomashek, Emily G, Tan, Eric C. D, Chen, Xiaowen, Chirban, Louis A, Chen, Yian, Schell, Daniel J, Karp, Eric M, Beckham, Gregg T
• Format: Article
• Language: English
• Subjects: Biomass; Biomass energy production; bioseparations; Computational fluid dynamics; Cross flow; dynamic filtration; Energy consumption; Energy demand; Energy efficiency; Filtration; Fluid dynamics; Fluid filters; Hydrodynamics; INORGANIC, ORGANIC, PHYSICAL, AND ANALYTICAL CHEMISTRY; Lignocellulose; Membranes; Modules; Operating costs; Recovery; rotating ceramic disc; Rotating liquids; Rotation; Separation; Shear rate; Slurries; solid-liquid separation; Solids; Sugar; techno-economic analysis; Vacuum filtration
• ISSN: 1463-9262; 1463-9270
• DOI: 10.1039/d4gc04533e

In many biomass conversion processes, the separation of cellulosic sugars from residual, lignin-rich solids is a critical step, and achieving high recovery yields of sugars by conventional tangential crossflow and vacuum filtration is challenged by the presence of biomass solids, which rapidly foul filters, resulting in decreased throughput. Considering the performance limitations of traditional filtration methods, dynamic filtration, which generates high shear at the membrane surface to decrease fouling, is emerging as a viable alternative for demanding solid-liquid separations. For high solids separations, there is little available information regarding the performance, limitations, and energy consumption of dynamic filtration. To that end, here we characterized the performance of a dynamic filtration module, specifically a rotating ceramic disc (RCD) filter, for the aseptic recovery of cellulosic sugars from biomass solids following pretreatment and enzymatic hydrolysis. We show how RCD rotational velocity and percent biomass solids impact the filter throughput. Additionally, we used computational fluid dynamics (CFD) simulations to estimate the shear rate at the membrane surface and to visualize hydrodynamic profiles within the module. With the combined CFD simulations and experimental results, we estimated the energy demand and operating expenses for a viable dynamic filtration system operating with a lignocellulosic feed slurry. Our results indicate that an RCD filter can achieve ≥95% recovery of sugars and produce a retentate slurry containing 12 wt% insoluble solids with low energy consumption (a 2.2-fold improvement over cross-flow filtration) and low operating costs ($0.06 per kg sugars). These results show a viable path towards operationally reliable, energy efficient, and cost-effective separations of sterilized cellulosic sugars from biomass solids and highlight the potential of dynamic filtration systems for challenging solid-liquid separations. A simple, low energy, and productive filtration method to clarify biomass hydrolysate to enable biochemical and thermochemical pathways to biofuels and biochemicals.