972 resultados para KRAFT LIGNIN


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Epoxidization is an interesting way to develop a new application of lignin and therefore to improve its application potential. In this work, kraft lignin-based epoxy resins were obtained by the epoxidization reaction, using the kraft lignin recovered directly from pulping liquor and modified by a methylolation reaction. The methylolated lignins were obtained by the reaction of original kraft lignin with formaldehyde and glyoxal, which is a less volatile and less toxic aldehyde. 1H-NMR spectroscopy showed that methylolated kraft lignin has more hydroxymethyl groups than glyoxalated kraft lignin. For the epoxidization reaction we studied the influence of the lignin:NaOH (w/w) ratio, temperature, and time of the reaction on the properties of the prepared epoxidized lignins. The structures of lignin-based epoxy resins were followed by epoxy index test and FTIR spectroscopy. Optimal conditions were obtained for lignin-based epoxy resin produced at lignin/NaOH = 1/3 at 70 ºC for 3h. Thermogravimetry analysis (TGA) revealed that the epoxidization enhances the thermal stability of lignins and may allow a wider temperature range for applications with lignin epoxy-PF blends

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La vanillina è un’aldeide aromatica importante da un punto di vista industriale, in quanto viene ampiamente utilizzata dall’industria alimentare, cosmetica e farmaceutica. Attualmente, la vanillina da biomasse viene ottenuta attraverso l’ossidazione catalitica della lignina. Un’alternativa è rappresentata dall’ossidazione elettro-catalitica, un processo che sta riscuotendo un notevole interesse, perché permette di lavorare in condizioni blande. L’obiettivo di questo lavoro è stato quello di sintetizzare elettro-catalizzatori che favoriscano la depolimerizzazione della lignina Kraft per ottenere selettivamente vanillina. Sono state utilizzate schiume di Ni a cella aperta, tal quali e elettro-depositate con idrossidi di Ni-Co e Co. La formazione degli osso-idrossidi dei metalli, sulla superficie delle schiume, e la OER contribuiscono all’elettro-ossidazione della lignina, mentre la resa di vanillina dipende sia dal catalizzatore che dalle condizioni di reazione (potenziale applicato e tempo di reazione). La resa maggiore di vanillina è stata ottenuta applicando 0.6 V vs SCE con un tempo di reazione di un’ora e utilizzando la schiuma di Ni bare come catalizzatore. Indipendentemente dal tipo di catalizzatore usato, aumentando il tempo di reazione la resa di vanillina diminuisce, probabilmente a causa delle reazioni di ri-condensazione e ossidazione successiva dei prodotti che coinvolgono la vanillina stessa. La presenza di idrossidi di Ni-Co e Co sulla schiuma di Ni non ne migliora l’attività catalitica. La schiuma Co/Ni esibisce un’elevata carica accumulata e un’alta conversione, probabilmente dovuto alle reazioni parassite che sfavoriscono l’accumulo di vanillina. Le schiume Ni-Co/Ni invece, presentando sia una resa in vanillina intermedia tra le altre due ma associata ad una carica accumulata molto bassa. Un risultato incoraggiante per possibili sviluppi futuri.

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One of the most important scientific and environmental issues is reducing global dependence on fossil sources and one of the solutions is to use biomass as feedstock. In particular, the use of lignocellulosic biomass to obtain molecules with considerable commercial importance is gaining more and more interest. Lignin, the most recalcitrant part of lignocellulosic biomass, is a valuable source of sustainable and renewable aromatic molecules, currently produced from petrochemical processes. Vanillin, one of the most important aromatic aldehydes on an industrial level, can be obtained through catalytic lignin oxidation. An alternative to the conventional catalytic oxidation process is the electro-catalytic process, which can be carried out at ambient temperature and pressure, using water as solvent, and it can be considered as a renewable energy storage. In this thesis, the electrocatalytic oxidation of Kraft and Dealkaline lignin in NaOH was investigated over Ni foam catalysts. The effect of the reaction parameters (i.e. time, applied potential, lignin concentration, NaOH concentration, and temperature) on the yields of vanillin and other valuable products was evaluated. After the screening of the reaction conditions, a systematic study of the contribution of the homogeneous reaction (lignin depolymerization due to the basic solvent) to the yield of the product was accomplished. Finally, considering the obtained results, an alternative reaction procedure was proposed.

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Different types of activated carbon were prepared by chemical activation of brewer`s spent grain (BSG) lignin using H(3)PO(4) at various acid/lignin ratios (1, 2, or 3 g/g) and carbonization temperatures (300, 450, or 600 degrees C), according to a 2(2) full-factorial design. The resulting materials were characterized with regard to their surface area, pore volume, and pore size distribution, and used for detoxification of BSG hemicellulosic hydrolysate (a mixture of sugars, phenolic compounds, metallic ions, among other compounds). BSG carbons presented BET surface areas between 33 and 692 m(2)/g, and micro- and mesopores with volumes between 0.058 and 0.453 cm(3)/g. The carbons showed high capacity for adsorption of metallic ions, mainly nickel, iron, chromium, and silicon. The concentration of phenolic compounds and color were also reduced by these sorbents. These results suggest that activated carbons with characteristics similar to those commercially found and high adsorption capacity can be produced from BSG lignin. (C) 2009 Elsevier Ltd. All rights reserved.

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Organosolv and kraft lignins were treated with ozone both in basic and acid media and the reaction was studied kinetically. In contrast to reported studies, ozone was more efective in basic medium. Kraft lignin was degraded faster than organosolv lignin in both media but in the basic medium the rate of reaction was very much faster than in the acid one: for kraft lignin, the observed degradation was 93% for 2 min of reaction in the basic medium and 56% for 10 min of reaction in the acid medium; for organosolv lignin, 47% and 25%, respectively, in the same times. Higher phenolic hydroxyl groups contents increase the reaction rate.

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Lignin was used as a natural adhesive to manufacture Vitis vinifera fiberboards. The fiberboards were produced at laboratory scale by adding powdered lignin to material that had previously been steam-exploded under optimized pretreatment and pressing conditions. The kraft lignin used was washed several times with an acidic solution to eliminate any contaminants and low molecular weight compounds. This research studied the effects of amounts of lignin ranging from 5% to 20% on the properties of Vitis vinifera fiberboards. The fiberboard properties evaluated were density, water resistance in terms of thickness swelling, water absorption, and the mechanical properties in terms of modulus of rupture, modulus of elasticity, and internal bond. Results showed that fiberboards made from Vitis vinifera without lignin addition had weaker mechanical properties. However, the fiberboards obtained using acid-washed kraft lignin as a natural adhesive had good mechanical and water resistance properties that fully satisfied the relevant standard specifications

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Diplomityön tarkoituksena oli puhdistaa kraft ligniiniä. Raaka-aineena käytettiin pääasiassa Lignoboost -menetelmän kaltaisella menetelmällä havupuu- mustalipeästä saostettua ligniiniä. Diplomityön ensimmäisenä tavoitteena oli löytää menetelmä, jolla voidaan poistaa kraft ligniinistä tuhkaa. Työssä raaka-aineena käytetyn saostetun ligniinin tuhkapitoisuus oli noin 3 %. Tarkoituksena oli saada laskettua tuhkapitoisuutta uudelleenlieton, suodatuksen ja pesun avulla. Työn toisena tavoitteena oli hiilihydraattien poisto kraft ligniinistä. Hiilihydraatit, pääosin hemiselluloosaa, ovat kiinnittyneet ligniiniin vahvoin kovalenttisin sidoksin. Aiempien kokemusten perusteella hemiselluloosat eivät irtoa ligniinistä vesipesun yhteydessä, vaan niiden irrottaminen vaatii onnistuakseen happo-, entsyymi- tai mikrobikäsittelyn, mikäli halutaan säilyttää ligniinin rakenne muuttumattomana. Tässä työssä käytetyt kraft ligniinin puhdistusmenetelmät olivat lietto, happohydrolyysi ja entsymaattinen hydrolyysi, joista kumpikin sisälsi ligniinin uudelleenlieton, suodatuksen ja muodostuneen kakun pesun vedellä.

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The purpose of this study is to investigate whether commercial Kraft lignin can be treated with pulsed corona discharge apparatus so that it becomes active. Active lignin refers to the kind of lignin that can be precipitated on the surface of a fiber by lowering the pH. A secondary agenda here is to remove the pungent smell of kraft lignin, which is caused by organically bound sulfur. It is expected that the study will identify mild processing conditions and parameters for achievement of the desired outcome. In the literature review, the properties of lignin are explained, as is their impact on any further processing. In addition, a number of processes are described for the oxidation of lignin in a variety of applications. In the experimental part of the study, test runs were conducted to determine the effects of oxygen supply and pulse frequency on oxidation results, where the purpose is to produce reactive lignin and to find a process that is feasible at an industrial scale. Based on the reported experiments, lignin could not be made active or precipitated to the surface of the fiber. Actual changes in the structure of lignin were not observed, but the pungent smell of lignin was removed. The exact reason for this change could not be established because sulfur NMR analysis did not work for the lignin samples.

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A kraft lignin derivative (KLD) obtained by reaction with p-aminobenzoic acid/phthalic anhydride was blended with poly(vinyl alcohol) (PVA) by solution casting from DMSO. PVA and PVA/KLD films were exposed to ultraviolet radiation (24, 48, and 96 h) and analyzed by thermogravimetry (TG), differential scanning calorimetry (DSC), infrared spectroscopy (FTIR), hydrogen nuclear magnetic resonance (H-1 NMR) spectroscopy, and scanning electron microscopy (SEM). PVA films show a loss of thermal stability due to irradiation. PVA/KLD reveals greater thermal stability than PVA and an increase in thermal stability after irradiation. These results suggest that the incorporation of KLD into PVA provides a gain in thermal and photochemical stability. FTIR, H-1 NMR, DSC, and TG results obtained for the blends suggest that intermolecular interactions between PVA and KLD chains are present. SEM micrographs revealed blend miscibility for a KLD blend content of up to 15 wt%, as observed at magnification of 1000 times. (c) 2005 Elsevier Ltd. All rights reserved.

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Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

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Besides polyurethanes and polyesters, phenolic and epoxy resins are the most prominent applications for technical lignins in thermosetting materials. To evaluate the potential application of lignin raw materials in phenol formaldehyde and epoxy resins, three types of alkaline lignins were characterized in terms of their structures and thermal properties. The lignin samples analyzed were kraft lignin (LIG-1), soda–rice straw lignin (LIG-2), and soda-wheat straw lignin (LIG-3). FTIR and 1H-NMR methods were used to determine their structure. Gel permeation chromatography (GPC) was used to determine the molecular weight distribution (MWD). Differential scanning calorimetry (DSC) was used to measure the glass transition temperature (Tg), and thermogravimetric analysis (TGA) to determine the thermal stability of lignin samples. Results showed that kraft lignin (LIG-1) has moderate hydroxyl-group content, is rich in G-type units, and has good thermal stability. These properties make it more suitable for direct use in phenol formaldehyde resins, and it is therefore a good raw material for this purpose. The alkaline soda-rice straw lignin (LIG-2) with a high hydroxyl-group content and excellent thermal stability is most suited to preparing lignin-based epoxy resin

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Kirjallisuusosassa tarkastellaan ligniiniä luonnon polymeerinä sekä sen kemiallisia perustietoja. Aiheena on myös sen tuotanto ja käyttö uusiutuvana raaka-ainelähteenä energian-, materiaali- ja kemikaalituotantoon sekä niiden mahdolliset tulevaisuudennäkymät. Mekaanisten prosessien osalta keskitytään kiintoaineen hienontamiseen. Lisäksi perehdytään planeettamyllyn toiminnan teoriaan sekä tuoreimpiin tutkimuksiin planeettamyllyjauhatukseen liittyen. Työn kokeellisen osan tarkoituksena oli tutkia ligniinin jauhautuvuutta, sillä partikkelien pienentämisellä voidaan kasvattaa ligniininijauheen ominaisalaa ja tasoittaa sen kokojakaumaa. Jauhautuvuuden avulla voidaan esimerkiksi arvioida ligniinille tehtävän hienojauhatuksen kannattavuutta jatkoprosesseja varten. Tutkimuskysymyksinä oli ”kuinka hyvin ligniini jauhautuu planeettamyllyllä?”, ”onko kylmäkäsittelyllä vaikutusta jauhatustulokseen?”, ”miten eri parametrit (jauhatusaika, kuulakoko ja kierrosnopeus) vaikuttavat jauhatustulokseen?” sekä ”muuttaako hienojauhatus ligniinin kemiallista koostumusta?”. Tutkittavana materiaalina oli kaupallinen kraft-ligniini ja koelaitteena käytettiin planeettamyllyä. Syötölle ja kaikille jauhatustuotteille suoritettiin partikkelikokoanalyysi, ja lisäksi syötölle ja erittäin hienoksi jauhetulle tuotteelle suoritettiin FTIR-analyysi. Kokeiden mukaan ligniini oli hyvin jauhautuvaa, eikä kylmäkäsittelyllä ollut merkittävää vaikutusta jauhatukseen. Kuulakoon pienentäminen sekä jauhatusajan ja kierrosnopeuden kasvattaminen alensivat ligniininjauheen partikkelikokoa. Lisäksi hienojauhatuksen ei todettu muuttaneen ligniinin kemiallista koostumusta.

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This work mainly arises from the necessity to support the rapid introduction of different biobased polymers that the industrial sector has been facing lately. Indeed, while considerable efforts are being made to find environmentally and economically sustainable materials, less attention is paid to their need to be properly compounded to fulfil increasingly rigorous technical and quality requirements. Therefore, there is a strong demand for the development of a novel generation of compatible additives able to improve the properties of biobased polymers while respecting sustainability. With this in mind, a new class of biobased plasticizers is herein proposed. Five different ketal-diesters were selectively synthesized starting from levulinic acid, a promising renewable chemical platform. These molecules were added to poly(vinyl chloride) as model polymer to test their plasticizing effectiveness. Complete morphological, thermal and viscoelastic characterizations showed a clear correlation between the structural features of the ketal-esters and the properties of the material. In addition, no significant leaching was found in both hydrophilic and lipophilic environments. Importantly, the proposed ketal-diesters performed comparably and, in some cases, even better than commercial plasticizers. The same molecules were then added to bacterial poly(3-hydroxybutyrate), a semicrystalline polyester characterized by poor thermal and mechanical properties. Morphology assessments showed no phase separation and the plasticizing effectiveness was confirmed by thermal and viscoelastic analyses, while leaching tests showed low extraction values. Readily usable fractions with controlled structure and tailored properties were obtained from highly heterogeneous industrial grade Kraft lignin. These fractions were then added to poly(vinyl alcohol). Promising preliminary results in terms of compatibility were achieved, with thermograms showing only one glass transition temperature. Finally, a fully biobased glycerol-trilevulinate was successfully synthesized by means of a mild and solvent-free route. Its plasticizing effectiveness was evaluated on poly(vinyl chloride), showing a significant decrease of the glass transition temperature of the material.

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Eucalyptus globulus sapwood and heartwood showed no differences in lignin content (23.0% vs. 23.7%) and composition: syringyl-lignin (17.9% vs. 18.0%) and guaiacyl-lignin (4.8% vs. 5.2%). Delignification kinetics of S- and G-units in heartwood and sapwood was investigated by Py-GC–MS/FID at 130, 150 and 170 °C and modeled as double first-order reactions. Reactivity differences between S and G-units were small during the main pulping phase and the higher reactivity of S over G units was better expressed in the later pulping stage. The residual lignin composition in pulps was different from wood or from samples in the initial delignification stages, with more G and H-units. S/G ratio ranged from 3 to 4.5 when pulp residual lignin was higher than 10%, decreasing rapidly to less than 1. The S/H was initially around 20 (until 15% residual lignin), decreasing to 4 when residual lignin was about 3%.

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Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)