Hydrochar, a solid residue generated from the hydrothermal liquefaction (HTL), presents both challenges and opportunities in biomass valorization. While HTL is a competitive technology aimed at producing crude bio-oil, the major limiting its economic viability and technical scalability is the safe disposal of generated by-products, which include nearly 25 wt% to 50 wt% post-hydrothermal aqueous phase (HTL-AP) and 5 wt% to 20 wt% solid hydrochar residues. Existing HTL studies have extensively characterized crude bio-oils, but hydrochar has received less attention, primarily focusing on yield and ultimate analysis.
Hydrochars (HCs), produced from HTL with carbon as the main component, can serve as low-cost adsorbents. However, their porosity and BET surface area remain relatively low due to the formation and condensation of hydrocarbons on the surface, which clogs pores. To improve this, chemical activation can be employed, where HCs are impregnated with agents acting as oxidants and then pyrolyzed. This process aromatizes the HCs carbon skeleton, introduces oxygen-containing functional groups, and develops a porous structure.

๐’๐ญ๐ž๐ฉ 1: ๐…๐ซ๐จ๐ฆ ๐–๐ก๐ž๐š๐ญ ๐’๐ญ๐ž๐ฆ ๐ญ๐จ ๐‡๐ฒ๐๐ซ๐จ๐œ๐ก๐š๐ซ๐ฌ ๐ฏ๐ข๐š ๐‡๐“๐‹
Wheat stems (WS) were subjected to HTL, transforming into HCs. Scanning electron microscopy (๐˜š๐˜Œ๐˜” ๐˜ช๐˜ฎ๐˜ข๐˜จ๐˜ฆ๐˜ด ๐Ÿ‘‡) reveals changes in the dense structure of WS, attributed to its carbohydrate composition. This transformation creates mesoporous cavities (Dp of 12.79 to 33.58 nm) and results in low BET surface areas (5.46โ€“26.06 mยฒ/g).


๐’๐ญ๐ž๐ฉ 2: ๐…๐ซ๐จ๐ฆ ๐‡๐ฒ๐๐ซ๐จ๐œ๐ก๐š๐ซ๐ฌ ๐ญ๐จ Activated Carbons (๐€๐‚๐ฌ) ๐ฏ๐ข๐š ๐‚๐ก๐ž๐ฆ๐ข๐œ๐š๐ฅ ๐€๐œ๐ญ๐ข๐ฏ๐š๐ญ๐ข๐จ๐ง
Through activation, the porous structure and adsorption capacity of HCs were enhanced. This process widens existing pores and introduces new pores (1.75 to 6.61 nm), resulting in ACs with BET surface areas 100.22โ€“1612.04 mยฒ/g. The transformation occurs through reactions between activating agents and the carbon structure in HCs at 800 ยฐC, which leads to carbon weight loss and yields decrease from 14.49% to 38.07%.

Integrating activated hydrochars as an alternative and low-cost adsorbents holds great promise for effectively removing organic and nutrient compounds from HTL-AP. Our research article titled โ€œ๐˜‰๐˜ช๐˜ฐ-๐˜ค๐˜ณ๐˜ถ๐˜ฅ๐˜ฆ ๐˜–๐˜ช๐˜ญ๐˜ด ๐˜—๐˜ณ๐˜ฐ๐˜ฅ๐˜ถ๐˜ค๐˜ต๐˜ช๐˜ฐ๐˜ฏ ๐˜ง๐˜ณ๐˜ฐ๐˜ฎ ๐˜ž๐˜ฉ๐˜ฆ๐˜ข๐˜ต ๐˜š๐˜ต๐˜ฆ๐˜ฎ ๐˜ถ๐˜ฏ๐˜ฅ๐˜ฆ๐˜ณ ๐˜š๐˜ถ๐˜ฃ๐˜ค๐˜ณ๐˜ช๐˜ต๐˜ช๐˜ค๐˜ข๐˜ญ ๐˜ž๐˜ข๐˜ต๐˜ฆ๐˜ณ ๐˜Š๐˜ฐ๐˜ฏ๐˜ฅ๐˜ช๐˜ต๐˜ช๐˜ฐ๐˜ฏ๐˜ด ๐˜ข๐˜ฏ๐˜ฅ ๐˜‰๐˜ข๐˜ต๐˜ค๐˜ฉ ๐˜ˆ๐˜ฅ๐˜ด๐˜ฐ๐˜ณ๐˜ฑ๐˜ต๐˜ช๐˜ฐ๐˜ฏ ๐˜ฐ๐˜ง ๐˜—๐˜ฐ๐˜ด๐˜ต-๐˜๐˜บ๐˜ฅ๐˜ณ๐˜ฐ๐˜ต๐˜ฉ๐˜ฆ๐˜ณ๐˜ฎ๐˜ข๐˜ญ ๐˜“๐˜ช๐˜ฒ๐˜ถ๐˜ฆ๐˜ง๐˜ข๐˜ค๐˜ต๐˜ช๐˜ฐ๐˜ฏ ๐˜ˆ๐˜ฒ๐˜ถ๐˜ฆ๐˜ฐ๐˜ถ๐˜ด ๐˜—๐˜ฉ๐˜ข๐˜ด๐˜ฆ ๐˜ฐ๐˜ฏ๐˜ต๐˜ฐ ๐˜ˆ๐˜ค๐˜ต๐˜ช๐˜ท๐˜ข๐˜ต๐˜ฆ๐˜ฅ ๐˜๐˜บ๐˜ฅ๐˜ณ๐˜ฐ๐˜ค๐˜ฉ๐˜ข๐˜ณ๐˜ดโ€ published in the Chemical Engineering Journal (CEJ) Engineering Journal, delves into this potential.

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