Native Scottish wood samples were investigated as potential, locally sourced, raw materials for biochar production. Screening experiments identified pure softwood as the preferable feedstock. Influence of operational parameters, i.e. activating gas flow rate (CO2), heating ramp rate and contact time on final biochar characteristics, was investigated using design of experiments. Surface area and biochar yield were selected as response variables. Minitab was used to define experimental run conditions and suggested an optimal output at 60 min contact time and 15 °C/min ramp rate for maximum responses. The highest surface area (764 m2/g) was achieved at 850 °C from softwood, albeit with a low yield of 15%. Under optimised conditions, the observed surface area was 613 m2/g with ~ 18% yield. Pareto charts suggested no influence of gas flow rate on chosen responses, which correlated well with experimental data. Pore structure was a combination of micro- and mesopores with average pore widths of 3–5 nm and an average point of zero charge of 7.40 ± 0.02. Proximate analysis showed an increase in fixed carbon content from 20%, in the feedstock, to 80%, in the optimised biochar. Morphological analysis showed a layered carbon structure in the biochars. The results show the significance of the selected feedstock as a potential source of biochar material and the relevance of interplay of operational variables in biochar development and their final characteristics.
Biochar production from sustainable materials through pyrolysis remains a key area of research, where additional value can be gained by understanding the influence of initial operating parameters to create optimised carbon products with different characteristics. In this study, native Scottish wood samples were used to produce biochars. Softwood and hardwood samples were investigated to determine feedstock importance, with a focus on the influence of process conditions on the final characteristics of biochars. Screening experiments helped to determine that the softwood feedstock resulted in enhanced product characteristics and identified the optimal pyrolysis temperature. A design of experiments approach was used to scope process variables for softwood feedstock: contact time with activating agent, gas flowrate, and influence of ramp rate during pyrolysis were studied. The response variables were product yield and biochar surface area. As expected, product yield decreased with increasing pyrolysis temperature, and increased ramp rates decreased biochar yield. Pore structure was a combination of micro- and mesopores, and high gas flowrate and pyrolysis temperature produced biochars with the greatest surface areas, while morphological analysis suggests a layered carbon structure. Contact angle analysis suggested hydrophilicity, suggesting compatibility with aqueous media, while a neutral surface charge demonstrates easy application in drinking water treatment systems. The results show the potential of parameter optimisation and insight into the interplay of these variables in biochar development, with characteristics that can be tailored to a range of applications.
Cr(VI) is toxic and carcinogenic, which fuels discussions on reducing existing standards for maximum Cr concentrations in drinking water. Fe(II) reductive precipitation is a common and economical method for achieving very low Cr(tot) concentrations (<5 µg/L). While Cr(VI) is reduced to Cr(III), Fe(II) is oxidized to Fe(III). The resulting Cr(III) and Fe(III) have low solubilities at neutral pH, precipitate as hydroxides, and can be removed by conventional media filtration. The presence of natural organic matter (NOM) in the raw water source can, depending on pH, concentration, type of NOM, and contact time, affect this process in various ways, from promoting Cr(VI) reduction, to re-reducing Fe(III), to forming stable complexes with Cr and Fe, thus, impairing chromium removal. The presented data showed that NOM, whether dominated by terrestrial humic acid, or of aquatic origin, could substantially impair chromium removal at neutral pH conditions. In particular, the ultimate removal of Cr(III) was affected. Soluble complexes and/or colloids of Cr(III), Fe(III) and NOM in the size range of 10 kDa–0.1 µm were formed, that could not be removed by conventional media filtration. Presence of iron sludge (>50 mg/L Fe(III)) mitigated the negative impacts of NOM on Cr(VI) reduction and Cr(III) removal. However, even 100 mg/L Fe(III), the highest applied sludge concentration, did not lead to a decrease in Fe(II) dosing requirements under the given conditions. A molar ratio higher than the given stochiometric ratio of [Fe(II)]:[Cr(VI)] = 3 was necessary for sufficient Cr(VI) removal.
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