2020
DOI: 10.1002/jctb.6458
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Liquefaction of corn husks and properties of biodegradable biopolyol blends

Abstract: BACKGROUND: A valorization route of corn husks from agrarian practices was performed by liquefaction using glycerol as liquefaction solvent to obtain biopolyols used as bioadditives in starch blends with the aim to find a useful industrial application in polymer processing. RESULTS: Low-molecular-weight liquefied products obtained from a practically total conversion reaction can be used for composite formulations (OH number, 310 mg KOH g −1 ; viscosity, 3.4 Pa s; molecular weight, 549 g mol −1). Concurrently, … Show more

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Cited by 9 publications
(4 citation statements)
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“…Furthermore, the fact that after synthesis, the polyol was neutralized with NaOH in powder state might have also influenced this parameter. In any case, these values were lower than those presented by other authors [ 50 , 56 ]. This represented an advantage in the later production of polyurethanes in terms of processability.…”
Section: Resultscontrasting
confidence: 83%
“…Furthermore, the fact that after synthesis, the polyol was neutralized with NaOH in powder state might have also influenced this parameter. In any case, these values were lower than those presented by other authors [ 50 , 56 ]. This represented an advantage in the later production of polyurethanes in terms of processability.…”
Section: Resultscontrasting
confidence: 83%
“…The first stage occurred between 100 and 300 °C due to the evaporation of water and low-molecular-weight compounds, and the defragmentation and degradation of the liquefied products [ 77 ]. The second stage took place at around 300–450 °C, where the liquefied products introduced by lignin and cellulose underwent further thermal decomposition [ 77 ]. Two main degradation peaks were observed for CLW and PLW, as shown in Table 4 .…”
Section: Resultsmentioning
confidence: 99%
“…3 Hydrothermal liquefaction (HTL) processing involves conversion of moisture-rich biomass feedstock at a high pressure range of 5-25 MPa and low-to-moderate temperature range of 280-375 °C in water to produce liquid product (biocrude), solid product (biochar) and gases. [4][5][6] Thereafter, the liquid product is separated by organic solvents having like polarity to desirable compounds expected in biocrude due to the insoluble nature of char in organic solvents. 7 The literature suggests that using water as well as organic solvents for liquefaction to obtain desirable biocrude is in increasing demand.…”
Section: Introductionmentioning
confidence: 99%