1995
DOI: 10.1515/hfsg.1995.49.4.332
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Alkaline Pulping of Hemp Woody Core: Kinetic Modelling of Lignin, Xylan and Cellulose Extraction and Degradation

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Cited by 44 publications
(41 citation statements)
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“…They studies were concerned with the processing of hemp raw materials (stalks, woody-core or bast) into soda pulps (Van der Werf et al 1994;De Groot et al 1995Dutt et al 2005;Fišerova et al 2013), organosolv pulps (Zomers et al 1995;Barberà et al 2011), thermomechanical pulp (TMP), cold caustic soda (CCS) pulp (Lisson 2001), alkaline peroxide extrusion pulp (APXP; DeJong et al 1999), enzymatic-mechanical pulp (Ekblad et al 2005), chemithermomechanical pulp (CTMP), sulphite pulps (Bączyńska et al 1993;Stupińska and Madaj 1996;Stupińska et al 2005;Dutt et al 2005) and kraft pulps Surma-Ś lusarska 2010a, 2011;Dutt et al 2005). Also studied were the kinetics of the delignification of hemp stalks and hemp woody-core (Abdul-Karim et al 1995;Dang and Nguyen 2006) and properties of bleached pulps from hemp roots (Miao et al 2014).…”
Section: Introductionmentioning
confidence: 99%
“…They studies were concerned with the processing of hemp raw materials (stalks, woody-core or bast) into soda pulps (Van der Werf et al 1994;De Groot et al 1995Dutt et al 2005;Fišerova et al 2013), organosolv pulps (Zomers et al 1995;Barberà et al 2011), thermomechanical pulp (TMP), cold caustic soda (CCS) pulp (Lisson 2001), alkaline peroxide extrusion pulp (APXP; DeJong et al 1999), enzymatic-mechanical pulp (Ekblad et al 2005), chemithermomechanical pulp (CTMP), sulphite pulps (Bączyńska et al 1993;Stupińska and Madaj 1996;Stupińska et al 2005;Dutt et al 2005) and kraft pulps Surma-Ś lusarska 2010a, 2011;Dutt et al 2005). Also studied were the kinetics of the delignification of hemp stalks and hemp woody-core (Abdul-Karim et al 1995;Dang and Nguyen 2006) and properties of bleached pulps from hemp roots (Miao et al 2014).…”
Section: Introductionmentioning
confidence: 99%
“…Pulping of thin hemp woody core was conducted in flow-through reactors (De Groot et al 1995). The hemp cores were impregnated at room temperature and then delignified isothermally at various sodium hydroxide concentrations (0.25 -2.0 M) and various temperatures 150 -180°C in flow-through reactors with a liquor-towood ratio of 30:1.…”
Section: Pulping Conditionsmentioning
confidence: 99%
“…It is anticipated that this model can also characterise the delignification kinetics of other lignocellulosic materials because the heterogeneous nature of the relevant reactions are similar. In this study this Nuclei Growth model will be tested against published data which were obtained from alkaline delignification of thin hemp woody core in isothermal flow-through reactors (De Groot et al 1995), ethanol-alkali organosolv delignification of fibre crop giant reed (Shatalov and Pereira 2005), acid-catalysed organosolv fractionation of wheat straw (Siridas and Koukios 2004), organosolv delignification of cottonwood in batch and flowthrough reactors (Tirtowidjojo et al 1988), kraft delignification of bamboo (Vu et al 2004) and alkaline delignification of flax fibres (Petrova et al 2004). We will attempt to identify the model parameters taking into account the effects of the type of lignocellulosic material and pulping processes.…”
Section: Introductionmentioning
confidence: 99%
“…During the chemical pulping process at high-temperature and high-pressure, degradation of lignin occurs and dissolves into the spent liquor. The delignification reactions involved the cleavage of non-phenolic β-O-4 linkage, phenolic α-O-4 linkage and releasing from the associated by the polysaccharide 8,9 .…”
Section: Introductionmentioning
confidence: 99%