2020
DOI: 10.31080/asmi.2020.03.0555
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Separation of Lignocellulosic Biomass Components by Alkali Pretreatment

Abstract: Traditional pretreatment methods have several disadvantages, including lower efficiency in terms of cellulose purity, high cost and incomplete separation of biomass components. Considering this, we compared different pretreatment processes and studied their effect on separation of biomass components. Effective delignification was achieved by alkali pretreatment with sodium hydroxide and ammonia. Among alkalis, sodium hydroxide treatment requires less severe process condition like lower concentration, temperatu… Show more

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Cited by 3 publications
(2 citation statements)
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“…A weak peak at 776 cm -1 in WRMA (Figure 2(a)), due to C-H out-of-plane deformation of lignin, was not found in the XRD patterns of LCNF-1h and LCNF-3h, indicating the hydrolysis of lignin with the NaOH treatment. The lignin wavenumber showed at 3343, 2891, 1600-1500, 1421, 1365, 1161 cm -1 in Figure 2 (a, b)-the data supported by Pereira et al [35].…”
Section: Characterization Of Wrma and Lcnfssupporting
confidence: 82%
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“…A weak peak at 776 cm -1 in WRMA (Figure 2(a)), due to C-H out-of-plane deformation of lignin, was not found in the XRD patterns of LCNF-1h and LCNF-3h, indicating the hydrolysis of lignin with the NaOH treatment. The lignin wavenumber showed at 3343, 2891, 1600-1500, 1421, 1365, 1161 cm -1 in Figure 2 (a, b)-the data supported by Pereira et al [35].…”
Section: Characterization Of Wrma and Lcnfssupporting
confidence: 82%
“…These advantages render NaOH more environmentally friendly and highly valuable for biomass pre-treatment. It is advantageous due to its low-energy extraction, dilute concentrations, and normal air pressure[35].…”
mentioning
confidence: 99%