SwePub
Sök i SwePub databas

  Utökad sökning

Träfflista för sökning "WFRF:(Theliander Hans) "

Sökning: WFRF:(Theliander Hans)

  • Resultat 1-50 av 254
Sortera/gruppera träfflistan
   
NumreringReferensOmslagsbildHitta
1.
  • Kristiansen, Anna Vollo, et al. (författare)
  • Electro-assisted filtration of microfibrillated cellulose : the impact of the degree of fibrillation
  • 2023
  • Ingår i: Cellulose. - : Springer Nature. - 0969-0239 .- 1572-882X. ; 30:16, s. 10097-10116
  • Tidskriftsartikel (refereegranskat)abstract
    • Efficient dewatering is necessary to achieve an economically sustainable large-scale production of microfibrillated cellulose (MFC) because the low solids content of the final product (< 3 wt.%) results in high costs related to transportation and storage, and problems for products with water incompatibility. Mechanical dewatering is preferred to thermal drying due to its lower energy demand, but MFC has a very high filtration resistance, which implies that an excessive filter area is necessary. Thus, to improve the dewatering, electro-assisted filtration may be used. In this study a bench-scale dead-end filter press was modified and the electro-assisted filtration of MFC, with two degrees of fibrillation, was investigated. The impact of the degree of fibrillation was clear when either pressure or electric field were applied separately. It was more challenging to dewater MFC with a higher degree of fibrillation using conventional filtration due to a greater surface area being subjected to the liquid flow. The opposite was found when using an electric field alone: the more fibrillated material has a higher surface charge and thereby is impacted more by the electric field. A combination of pressure and electric field resulted in a greatly improved dewatering rate, but no significant difference could be observed between the two qualities. After dewatering, the water retention value was slightly decreased, but the material still showed a gel-like behaviour, although the network strength was slightly reduced, as seen by a reduction in yield stress, storage and loss moduli. This was plausibly due to a decrease in the surface area and/or deformed network.
  •  
2.
  • Magnusson, Hans, 1943- (författare)
  • From recovery boiler to integration of a textile fiber plant : Combination of mass balance analysis and chemical engineering
  • 2015
  • Licentiatavhandling (övrigt vetenskapligt/konstnärligt)abstract
    • Modern chemical technology is an efficient tool for solving problems, particularly within the complex environment of the pulp and paper industry, and the combination of experimental studies, mill data and mass balance calculations are of fundamental importance to the development of the industry. In this study various examples are presented, whereby chemical technology is of fundamental importance.It is well documented that under normal conditions the molten salt mixture from the kraft recovery boiler flows down into the dissolving tank without problems. However, in the case of  alternatives to the kraft recovery boiler, knowledge of more precise data of the molten salts is required for the design calculations. In this study the viscosity for the case of sodium carbonate and 30 mole% sulphide has been measured and is of the magnitude 2 – 3 cP at temperatures relevant for a recovery boiler, i.e. similar to water at room temperature.The presence of non-process elements (NPE) in a typical pulp mill has been investigated. The main input is with regards to the wood, and anticipated problems include; deposits in evaporators, high dead-load in liquor streams, plugging of the upper part of the recovery boiler and decreasing efficiency in the causticization department. Efficient green liquor clarification is of the greatest importance as an efficient kidney for many NPE. Mill data and calculations show that the magnesium added in the oxygen delignification does not form a closed loop.Integration of a prehydrolysis kraft pulp mill producing dissolving pulp with a plant producing viscose textile fiber could be highly beneficial. The prehydrolysis liquor will contain both sugars and acetic acid. It is however not possible to fully replace the sulphuric acid of the viscose spinning bath with acetic acid of own production. The sulphuric chemicals from the viscose plant can be partly taken care of in the kraft recovery area as well as the viscose plant which can be supplied with alkali and sulphuric acid. Zinc-containing effluents from the viscose plant can be treated with green liquor to precipitate zinc sulphide.
  •  
3.
  • Abdel Hady, Ahmed Wagih Abdallah, 1990, et al. (författare)
  • In situ microstructural evolution of spruce wood during soda pulping using synchrotron X-ray tomography
  • 2022
  • Ingår i: Holzforschung. - : Walter de Gruyter GmbH. - 1437-434X .- 0018-3830. ; 76:7, s. 611-621
  • Tidskriftsartikel (refereegranskat)abstract
    • A new laboratory reactor to perform in situ studies of structural changes in wood during soda pulping using synchrotron X-ray tomography is presented. The reactor is of recirculation type to provide stable reaction conditions and mimic the industrial situation. Experiments have been performed using this reactor in situ at a synchrotron microtomography beamline to provide sequences of 3D images from which measurement of wood cell wall thickness have been possible for the first time. The results showed that the cell wall thickness increased significantly in the early stage of pulping (<10 min), which is due to the transportation of cooking chemicals through the tracheids, resin channels and pits into the cell wall, which is swollen with the increased pH. Subsequently, the cell wall thickness reduces over the processing time up to 60 min with a high rate, which is inferred to be due to the dissolution and transport of lignin and hemicellulose from the secondary walls, allowing for better transportation of active chemicals deep through the cell wall layers. After 60 min processing, the cell wall thickness reduction rate reduced, as dissolution of lignin and hemicelluloses from the cell walls ceased, while the remaining dissolution occurs mainly at the middle lamella.
  •  
4.
  • Abdel Hady, Ahmed Wagih Abdallah, 1990, et al. (författare)
  • Micro/nano-structural evolution in spruce wood during soda pulping
  • 2021
  • Ingår i: Holzforschung. - : Walter de Gruyter GmbH. - 1437-434X .- 0018-3830. ; 75:8, s. 754-764
  • Tidskriftsartikel (refereegranskat)abstract
    • Alkaline delignification of wood tissue is the core of the global pulping technology and the most prominent large-scale separation of the main wood components. This work aims at improved understanding of the interplay between the topochemistry of alkaline pulping and the associated morphological changes. Morphology and chemical structure of partially soda-delignified wood chips were studied combining X-ray tomography (XRT), X-ray diffraction analysis and compositional characterization (lignin and carbohydrate content). The XRT studies of wet samples (providing 3D structural information without interfering drying effects), allowed observation of the cell wall separation as an increasing amount of lignin was removed with the increasing pulping time. Comparison between the microstructure of the surface and the central parts of the treated chips showed a more delignified microstructure at the surface, which highlights the dependence of the delignification process on the mass transport (hydroxide ions and lignin fragments) through the wood tissue. The crystallite size of cellulose increased in the <200> crystal planes during the early stage of pulping while there was little effect on the <110> plane.
  •  
5.
  • Ahlbom, Anders, 1993, et al. (författare)
  • On the hydrothermal depolymerisation of kraft lignin using glycerol as a capping agent
  • 2023
  • Ingår i: Holzforschung. - : Walter de Gruyter GmbH. - 1437-434X .- 0018-3830. ; 77:3, s. 159-169
  • Tidskriftsartikel (refereegranskat)abstract
    • Depolymerisation of kraft lignin under hydrothermal conditions was investigated at short residence times (1–12 min) with glycerol being used as a capping agent. The weight average molecular weight (M w) of the products decreased within the first minute of residence time, with the inter-unit ether linkages breaking accordingly. Furthermore, the M w of the product fractions decreased at increasing residence times, while the char yield increased. Short residence times thus appear to be beneficial for mitigating the formation of char. Also, addition of NaOH reduced the yield of char. Although the addition of glycerol caused a decrease in the M w of the products, it seemed to increase the yield of char and therefore might not be a suitable capping agent for kraft lignin depolymerisation.
  •  
6.
  •  
7.
  • Ahlbom, Anders, 1993, et al. (författare)
  • Towards understanding kraft lignin depolymerisation under hydrothermal conditions
  • 2021
  • Ingår i: Holzforschung. - : Walter de Gruyter GmbH. - 1437-434X .- 0018-3830. ; 76:1, s. 37-48
  • Tidskriftsartikel (refereegranskat)abstract
    • Kraft lignin depolymerisation using hydrothermal liquefaction suffers from the formation of char, resulting in a decreased product yield as well as causing operational problems. While this may be mitigated by the addition of capping agents such as phenol and isopropanol, other reaction parameters, for example reaction time and temperature, are also important for the product yields. In this work, the effect of short reaction times on the hydrothermal liquefaction of kraft lignin in an alkaline water and isopropanol mixture was investigated at 1-12 min and 290 °C. The results show that there were swift initial reactions: the major ether bonds in the lignin were broken within the first minute of reaction, and the molecular weight of all product fractions was halved at the very least. Longer reaction times, however, do not cause as pronounced structural changes as the initial reaction, indicating that a recalcitrant carbon-carbon skeleton remained in the products. Nevertheless, the yields of both char and monomers increased slowly with increasing reaction time. The swift initial depolymerising reactions were therefore followed by slower repolymerisation as well as a slow formation of monomers and dimers, which calls for careful tuning of the reaction time.
  •  
8.
  • Ahlbom, Anders, 1993, et al. (författare)
  • Using guaiacol as a capping agent in the hydrothermal depolymerisation of kraft lignin
  • 2023
  • Ingår i: Nordic Pulp and Paper Research Journal. - 2000-0669 .- 0283-2631. ; 38:4, s. 619-631
  • Tidskriftsartikel (refereegranskat)abstract
    • The depolymerisation of softwood kraft lignin was investigated, under hydrothermal conditions at 290 °C and 250 bar, with guaiacol in the reactor feed to evaluate its impact on the formation of char and on the molecular weights of the products. The effect of residence time was investigated in the time span 1-12 min. Lignin is depolymerised during the process and guaiacol is both formed and consumed during the reaction, with clearly noticeable changes as early as in the first minute of reaction. Although the addition of guaiacol in the reactor feed causes a reduction in the weight average molecular weight of the products, the yield of char increases. Longer residence times result in repolymerisation of the reaction products as well as a further increase in the yield of monoaromatic components and char.
  •  
9.
  • Ahlbom, Anders, 1993, et al. (författare)
  • Using Isopropanol as a Capping Agent in the Hydrothermal Liquefaction of Kraft Lignin in Near-Critical Water
  • 2021
  • Ingår i: Energies. - : MDPI AG. - 1996-1073 .- 1996-1073. ; 14:4
  • Tidskriftsartikel (refereegranskat)abstract
    • In this study, Kraft lignin was depolymerised by hydrothermal liquefaction in near-critical water (290-335 degrees C, 250 bar) using Na2CO3 as an alkaline catalyst. Isopropanol was used as a co-solvent with the objective of investigating its capping effect and capability of reducing char formation. The resulting product, which was a mixture of an aqueous liquid, containing water-soluble organic compounds, and char, had a lower sulphur content than the Kraft lignin. Two-dimensional nuclear magnetic resonance studies of the organic precipitates of the aqueous phase and the char indicated that the major lignin bonds were broken. The high molar masses of the char and the water-soluble organics, nevertheless, indicate extensive repolymerisation of the organic constituents once they have been depolymerised from the lignin. With increasing temperature, the yield of char increased, although its molar mass decreased. The addition of isopropanol increased the yield of the water-soluble organic products and decreased the yield of the char as well as the molar masses of the products, which is indicative of a capping effect.
  •  
10.
  • Antonsson, Stefan, 1979- (författare)
  • Strategies for improving kraftliner pulp properties
  • 2008
  • Doktorsavhandling (övrigt vetenskapligt/konstnärligt)abstract
    • A large part of the world paper manufacturing consists of production of corrugated board components, kraftliner and fluting, that are used in many different types of corrugated boxes. Because these boxes are stored and transported, they are often subjected to changes in relative humidity. These changes together with mechanical loads will increase the deformation of the boxes compared to the case where the same loads are applied in a static environment. This enlarged creep due to the changes in relative humidity is called mechano-sorptive or accelerated creep. Mechano-sorptive creep forces producers to use high safety factors when designing boxes, and therefore, this is one of the key properties of kraftliner boards.   Different strategies to decrease mechano-sorptive creep, and to simultaneously gain more knowledge about the causes for this phenomenon in paper, are the aim of this work. Derivatised and underivatised black liquor lignins, a by-product produced in pulp mills in large quantities, have been used together with biomimetic methods, to modify the properties of kraftliner pulp. Furthermore, the properties of kraftliner pulp have been compared to other pulps in order to evaluate the influence of fibre morphological factors, such as fibre width and shape factor, on the mechano-sorptive creep. In addition the influence of the chemical composition of the kraftliner pulp has been evaluated both by means of treating a kraftliner pulp with chlorite and xylanase and by producing pulps with different chemical composition.   By using lignin and biomimetic methods, to create radical coupling reactions, it has been shown that it is possible to increase the wet strength of kraftliner pulp sheets. This method of treating the pulp showed, however, no significant effects on the mechano-sorptive creep. The addition of an apolar suberin-like lignin derivative, which has been shown to be possible to produce from natural resources, did show a positive effect on mechano-sorptive creep properties, but at the expense of stiffness properties in constant climate. Different pulps were compared with a kraftliner pulp and it was observed that the ratio between tensile stiffness and hygroexpansion can be used to estimate the mechano-sorptive creep properties. The hardwood kraft pulps investigated had lower hygroexpansion, probably due to more slender and straighter fibres, and higher tensile stiffness, probably due to lower lignin content. As the lignin content was varied by different methods in kraft pulps, it was observed that increased lignin content gives an increased hygroexpansion and decreased tensile stiffness as well as an increased mechano-sorptive creep. There were also indications of increased mechano-sorptive creep due to higher xylan content.    
  •  
11.
  • Arandia, Kenneth Gacutno, 1990, et al. (författare)
  • Fouling characteristics of microcrystalline cellulose during cross-flow microfiltration: Insights from fluid dynamic gauging and molecular dynamics simulations
  • 2023
  • Ingår i: Journal of Membrane Science. - : Elsevier BV. - 1873-3123 .- 0376-7388. ; 669
  • Tidskriftsartikel (refereegranskat)abstract
    • The fouling behaviour of microcrystalline cellulose (MCC) particles on polyethersulfone (PES) membranes was investigated using fluid dynamic gauging (FDG) and molecular dynamics (MD) simulations. Experimental cross-flow microfiltration (MF) of a dilute MCC suspension at 400 mbar transmembrane pressure using 0.45 μm PES membranes revealed an estimated fouling layer thickness of 616 ± 5 μm for both fouled and re-fouled membranes at an applied shear stress of 37 ± 2 Pa. A decline in pure water flux was observed after each membrane cleaning and flushing procedure, indicating that highly resilient layers were formed close to the membrane surface. A possible explanation for the formation of resilient cellulose layers was obtained through MD simulations of the free energy profiles, which predicted deep energy minima at close interparticle separations of the cellulose–cellulose and cellulose–PES systems. The consequence of this energy minima is that attractive and repulsive forces are in balance at a specific distance between the particles, suggesting high binding energy at close interparticle distances. This implies that a certain force is needed to remove the layer or redisperse the cellulose particles. MD simulations also suggested that contributions made by repulsive hydration forces negatively influenced the adsorption of cellulose particles onto the PES membrane. These results highlight how experimental FDG measurements, when complemented with MD simulations, can provide insights into the fouling behaviour of an organic model material during cross-flow filtration.
  •  
12.
  • Arandia, Kenneth Gacutno, 1990, et al. (författare)
  • Monitoring Membrane Fouling Using Fluid Dynamic Gauging: Influence of Feed Characteristics and Operating Conditions
  • 2023
  • Ingår i: Membranes. - 2077-0375. ; 13:10
  • Tidskriftsartikel (refereegranskat)abstract
    • Recent studies on membrane fouling have made considerable progress in reducing its adverse effects. However, a lack of comprehensive studies focusing on the underlying fouling mechanisms remains. This work aims to address a part of this gap by investigating the influence of feed suspension chemistry and operating conditions on the fouling characteristics of microcrystalline cellulose. Fluid dynamic gauging (FDG) was employed to monitor the properties of fouling layers under varied conditions. FDG results revealed that the cohesive strength of fouling layers increased in the direction towards the membrane, which can be associated with the higher compressive pressures exerted on foulants deposited near the surface. At lower pHs and higher ionic strengths, reduced electrostatic repulsions between particles likely resulted in particle agglomeration, leading to the formation of thicker cakes. In addition, thicker cake layers were also observed at higher feed concentrations, higher operating transmembrane pressures, and longer filtration times. The cross-flow velocity influenced the resilience of fouling layers significantly, resulting in thinner yet stronger cake layers in the transition and turbulent flow regimes. These findings regarding the influence of feed characteristics and operating conditions on the fouling behavior can be beneficial in developing effective antifouling strategies in membrane separation processes.
  •  
13.
  • Azhar, Shoaib, 1980-, et al. (författare)
  • Extraction of hemicelluloses from fiberized spruce wood
  • 2015
  • Ingår i: Carbohydrate Polymers. - : Elsevier BV. - 0144-8617 .- 1879-1344. ; 117, s. 19-24
  • Tidskriftsartikel (refereegranskat)abstract
    • A novel mechanical pre-treatment method was used to separate the wood chips into fiber bundles in order to extract high molecular weight wood polymers. The mechanical pre-treatment involved chip compression in a conical plug-screw followed by defibration in a fiberizer. The fiberized wood was treated with hot water at various combinations of time and temperature in order to analyze the extraction yield of hemicelluloses at different conditions. Nearly 6 mg/g wood of galactoglucomannan was obtained at 90◦C/120min which was about three times more than what could be extracted from wood chips. The extracted carbohydrates had molecular weight ranging up to 60 kDa. About 10% of each of the extracted material had a molecular weight above 30 kDa. The extraction liquor could also be reused for consecutive extractions with successive increase in the extraction yield of hemicelluloses. 
  •  
14.
  • Belkheiri, Tallal, 1985, et al. (författare)
  • Effect of pH on Kraft Lignin Depolymerisation in Subcritical Water
  • 2016
  • Ingår i: Energy & Fuels. - : American Chemical Society (ACS). - 1520-5029 .- 0887-0624. ; 30:6, s. 4916-4924
  • Tidskriftsartikel (refereegranskat)abstract
    • Softwood kraft lignin was depolymerized using subcritical water (623 K and 25 MPa) in a continuous small pilot unit. ZrO2 and K2CO3 were used as catalysts, and phenol was used as capping agent to suppress repolymerization. The effect of pH was investigated by adding KOH in five steps to the feed. The yield of water-soluble organics increased with pH. The yield of bio-oil was also influenced by the pH and varied between 28 and 32 wt %. The char yield on the zirconia catalyst showed a minimum at pH 8.1. The yield of suspended solids was low at pH below 8.1 but increased at higher pH values. The oxygen content in the bio-oil was only 15 wt %, compared to about 26 wt % in the kraft lignin.
  •  
15.
  • Belkheiri, Tallal, 1985, et al. (författare)
  • Hydrothermal liquefaction of kraft lignin in sub-critical water: the influence of the sodium and potassium fraction
  • 2018
  • Ingår i: Biomass Conversion and Biorefinery. - : Springer Science and Business Media LLC. - 2190-6815 .- 2190-6823. ; 8:3, s. 585-595
  • Tidskriftsartikel (refereegranskat)abstract
    • As a part of developing a hydrothermal liquefaction (HTL) process to valorise lignin, it is important to consider integration possibilities with existing infrastructures in order to obtain an overall positive economic impact. One obvious example is to integrate the HTL process with the kraft pulp mill: transport and storage costs is reduced, the temperature levels on process streams can be matched (energy integration) and the recovery/use of alkali can be made efficient. In this study, softwood kraft lignin was depolymerised using sub-critical water (623 K; 25 MPa) in a continuous, small pilot unit with a flow rate of 2 kg/h. ZrO2, K2CO3/KOH and Na2CO3/NaOH were used as catalytic system, and phenol as the capping agent. The influence of the ratio between sodium and potassium in the feed on the yield and composition of the product stream was investigated. The results showed that bio-oil, water-soluble organics (WSO) and char yields were not remarkably influenced by shifting the catalytic system from potassium to sodium. Moreover, the yields of most phenolic compounds did not change significantly when the sodium fraction was varied in the feed. The amounts of suspended solids in the bio-oil produced showed, however, a diminishing trend, (decrease from 10.8 to 3.8%) when the sodium fraction was increased in the feed, whilst the opposite trend was observed for the heavy oil, which increased from 24.6 to 37.6%.
  •  
16.
  • Belkheiri, Tallal, 1985, et al. (författare)
  • Hydrothermal Liquefaction of Kraft Lignin in Subcritical Water: Influence of Phenol as Capping Agent
  • 2018
  • Ingår i: Energy & Fuels. - : American Chemical Society (ACS). - 1520-5029 .- 0887-0624. ; 32:5, s. 5923-5932
  • Tidskriftsartikel (refereegranskat)abstract
    • The depolymerization of LignoBoost Kraft lignin in subcritical water, i.e. hydrothermal liquefaction (HTL), was investigated using ZrO 2 , K 2 CO 3 , and KOH as catalysts in a fixed-bed reactor with recirculation. Focus was placed on the effect exerted by the concentration of the phenol in suppressing repolymerization, which is responsible for forming char. Feeds with various concentrations of phenol (2-10%) were investigated, and the results showed that phenol partially prevents repolymerization even at low concentrations. The bio-oil yield of (61.0 ± 2.7) % was fairly stable when the concentration of phenol was varied. In the case of the formation of char on the catalyst, the char yield revealed a weakly decreasing trend (14.6-12.3%) when the amount of phenol in the feed was increased. The results also showed that the phenolic monomers that are alkylated, such as o-/p-cresols, increased significantly with increasing concentrations of phenol, while aromatic compounds, based on a guaiacol ring structure, showed decreasing trends.
  •  
17.
  • Belkheiri, Tallal, 1985, et al. (författare)
  • Kraft Lignin Depolymerization in Near-Critical Water: Effect of Changing Co-Solvent
  • 2014
  • Ingår i: Cellulose Chemistry and Technology. - 0576-9787. ; 48:9-10, s. 813-818
  • Tidskriftsartikel (refereegranskat)abstract
    • As part of developing a process to valorize lignin in a pulp mill with lignin separation, the depolymerisation of lignin to valuable chemicals was investigated in near-critical water. This was done by using methanol as co-solvent and hydrogen donor, phenol to suppress repolymerization (e.g. formation of char), and ZrO2 as a heterogeneous catalyst, with potassium carbonate as a co-catalyst. The reaction was carried out in a continuous flow fixed-bed reactor (500 cm(3)), at 280-350 degrees C and 25MPa. An important aspect is to suppress char formation. Therefore, the char formation was studied by using different concentrations of methanol and phenol. The char yield varied between 14% and 26%. When using methanol as the only co-solvent, the char yield decreased with increasing methanol concentration. Adding phenol resulted in a further decrease. The reactor outlet consisted mainly of two liquid phases, an aqueous and an oil phase, mixed together. The chemical analysis of the aqueous phase showed the presence of mainly phenolic compounds, for instance guaiacol, catechol, phenol and cresol.
  •  
18.
  • Bengtsson, Andreas, et al. (författare)
  • Improved yield of carbon fibres from cellulose and kraft lignin
  • 2018
  • Ingår i: Holzforschung. - : Walter de Gruyter GmbH. - 0018-3830 .- 1437-434X. ; 72:12, s. 1007-1016
  • Tidskriftsartikel (refereegranskat)abstract
    • To meet the demand for carbon-fibre-reinforced composites in lightweight applications, cost-efficient processing and new raw materials are sought for. Cellulose and kraft lignin are each interesting renewables for this purpose due to their high availability. The molecular order of cellulose is an excellent property, as is the high carbon content of lignin. By co-processing cellulose and lignin, the advantages of these macromolecules are synergistic for producing carbon fibre (CF) of commercial grade in high yields. CFs were prepared from precursor fibres (PFs) made from 70:30 blends of softwood kraft lignin (SW-KL) and cellulose by dry-jet wet spinning with the ionic liquid (IL) 1-ethyl-3-methylimidazolium acetate ([EMIm][OAc]) as a solvent. In focus was the impact of the molecular mass of lignin and the type of cellulose source on the CF yield and properties, while membrane-filtrated kraft lignin and cellulose from dissolving kraft pulp and fully bleached paper-grade SW-KP (kraft pulp) served as sources. Under the investigated conditions, the yield increased from around 22% for CF from neat cellulose to about 40% in the presence of lignin, irrespective of the type of SW-KL. The yield increment was also higher relative to the theoretical one for CF made from blends (69%) compared to those made from neat celluloses (48-51%). No difference in the mechanical properties of the produced CF was observed.
  •  
19.
  •  
20.
  •  
21.
  • Bengtsson, Jenny, et al. (författare)
  • Identifying breach mechanism during air-gap spinning of lignin–cellulose ionic-liquid solutions
  • 2019
  • Ingår i: Journal of Applied Polymer Science. - : John Wiley and Sons Inc.. - 0021-8995 .- 1097-4628.
  • Tidskriftsartikel (refereegranskat)abstract
    • To be able to produce highly oriented and strong fibers from polymer solutions, a high elongational rate during the fiber-forming process is necessary. In the air-gap spinning process, a high elongational rate is realized by employing a high draw ratio, the ratio between take-up and extrusion velocity. Air-gap spinning of lignin–cellulose ionic-liquid solutions renders fibers that are promising to use as carbon fiber precursors. To further improve their mechanical properties, the polymer orientation should be maximized. However, achieving high draw ratios is limited by spinning instabilities that occur at high elongational rates. The aim of this experimental study is to understand the link between solution properties and the critical draw ratio during air-gap spinning. A maximum critical draw ratio with respect to temperature is found. Two mechanisms that limit the critical draw ratio are proposed, cohesive breach and draw resonance, the latter identified from high-speed videos. The two mechanisms clearly correlate with different temperature regions. The results from this work are not only of value for future work within the studied system but also for the design of air-gap spinning processes in general.
  •  
22.
  • Bengtsson, Jenny, 1990, et al. (författare)
  • Mass transport and yield during spinning of lignin-cellulose carbon fiber precursors
  • 2019
  • Ingår i: Holzforschung. - : Walter de Gruyter GmbH. - 1437-434X .- 0018-3830. ; 73:5, s. 509-516
  • Tidskriftsartikel (refereegranskat)abstract
    • Lignin, a substance considered as a residue in biomass and ethanol production, has been identified as a renewable resource suitable for making inexpensive carbon fibers (CFs), which would widen the range of possible applications for light-weight CFs reinforced composites. Wet spinning of lignin-cellulose ionic liquid solutions is a promising method for producing lignin-based CFs precursors. However, wet-spinning solutions containing lignin pose technical challenges that have to be solved to enable industrialization. One of these issues is that a part of the lignin leaches into the coagulation liquid, which reduces yield and might complicate solvent recovery. In this work, the mass transport during coagulation is studied in depth using a model system and trends are confirmed with spinning trials. It was discovered that during coagulation, efflux of ionic liquid is not hindered by lignin concentration in solution and the formed cellulose network will enclose soluble lignin. Consequently, a high total concentration of lignin and cellulose in solution is advantageous to maximize yield. This work provides a fundamental understanding on mass transport during coagulation of lignin-cellulose solutions, crucial information when designing new solution-based fiber forming processes.
  •  
23.
  • Bengtsson, Jenny, et al. (författare)
  • The challenge of predicting spinnability : Investigating benefits of adding lignin to cellulose solutions in air-gap spinning
  • 2021
  • Ingår i: Journal of Applied Polymer Science. - : John Wiley and Sons Inc. - 0021-8995 .- 1097-4628. ; 138:26
  • Tidskriftsartikel (refereegranskat)abstract
    • In this study, the underlying mechanism for improved spinnability when mixing lignin and cellulose in solution was investigated. Co-processing of lignin and cellulose has previously been identified as a potential route for production of inexpensive and bio-based carbon fibers. The molecular order of cellulose contributes to the strength of the fibers and the high carbon content of lignin improves the yield during conversion to carbon fibers. The current work presents an additional benefit of combining lignin and cellulose; solutions that contain both lignin and cellulose could be air-gap spun at substantially higher draw ratios than pure cellulose solutions, that is, lignin improved the spinnability. Fibers were spun from solutions containing different ratios of lignin, from 0 to 70 wt%, and the critical draw ratio was determined at various temperatures of solution. The observations were followed by characterization of the solutions with shear and elongational viscosity and surface tension, but none of these methods could explain the beneficial effect of lignin on the spinnability. However, by measuring the take-up force it was found that lignin seems to stabilize against diameter fluctuations during spinning, and plausible explanations are discussed
  •  
24.
  • Bialik, Marta Anna, 1978, et al. (författare)
  • Boiling Point Rise Calculations in Sodium Salt Solutions
  • 2008
  • Ingår i: Industrial & Engineering Chemistry Research. - : American Chemical Society (ACS). - 1520-5045 .- 0888-5885. ; 47:4, s. 1283-1287
  • Tidskriftsartikel (refereegranskat)abstract
    • The boiling point rise (elevation) of aqueous industrial solutions is often regarded as an important propertywith respect to chemical process design. This work shows an application of the Pitzer method for calculatingthe activity coefficients to the estimation of the boiling point rise of single-component and multicomponentelectrolyte solutions. Good agreement between experimental and predicted values of the boiling point elevationsof solutions of several salts (NaOH, Na2CO3, Na2SO4, NaCl, Na2S2O3, Na2S, mixed NaOH-Na2CO3, andmixed Na2CO3-Na2SO4) was obtained. A method for using the boiling point rise data to obtain ionic interactionparameters for the Pitzer method is also shown.
  •  
25.
  •  
26.
  •  
27.
  •  
28.
  • Bialik, Marta Anna, 1978, et al. (författare)
  • Solubility and Solid-Phase Composition in Na2CO3-Na2SO4 Solutions at Boiling Temperature: A Modeling Approach
  • 2008
  • Ingår i: Industrial & Engineering Chemistry Research. - : American Chemical Society (ACS). - 1520-5045 .- 0888-5885. ; 47:9, s. 3233-3238
  • Tidskriftsartikel (refereegranskat)abstract
    • Scaling caused by Na2CO3-Na2SO4 double salts constitutes a severe problem in black liquor evaporators.The ability to predict the solubility and solid-phase composition of these species would be conclusive inminimizing the adverse effects of scaling. Experimental solubility data for (sodium sulfate) dicarbonate, acarbonate-rich double salt identified in Na2CO3-Na2SO4 precipitates, were generated and used for fitting anempirical solubility model. A thermodynamically based approach for predicting the solubility and solidphasecomposition, previously used for burkeite precipitates, was applied to solid solutions of dicarbonate.
  •  
29.
  • Bialik, Marta Anna, 1978, et al. (författare)
  • Using the Pitzer method to estimate the boiling point rise in black liquor solutions
  • 2009
  • Ingår i: Nordic Pulp and Paper Research Journal. - 2000-0669 .- 0283-2631. ; 24:2, s. 172-182
  • Tidskriftsartikel (refereegranskat)abstract
    • The b.p. rise (elevation) of aq. industrial solns. is often of significant importance for the design of process conditions, equipment, heat balances, etc. However, few rigorous methods exist for predicting b.p. elevation in complex, multicomponent, electrolyte solns. An example of such a soln. is the black liquor obtained in kraft pulp prodn.: a complex mixt. of org. and inorg. ions including Na+, K+, OH-, HS-, CO32-, SO42-, S2O32-, CH3COO-, various phenolates and many more. This work shows one application of the semi-empirical Pitzer method to the theor. prediction of the b.p. rise in industrial black liquor solns. The values of the b.p. elevation were measured in two series of black liquors from representative Swedish mills, including both the original and lignin-lean black liquor at different solid contents. The results show a good agreement between exptl. and predicted values at low to moderate solid content, and good qual. prediction at high solid content.
  •  
30.
  •  
31.
  •  
32.
  •  
33.
  •  
34.
  •  
35.
  •  
36.
  • Bogren, Johannes, 1979, et al. (författare)
  • Impact of dissolved sodium salts on kraft cooking reactions
  • 2009
  • Ingår i: Holzforschung. - 1437-434X .- 0018-3830. ; 63:2, s. 226-231
  • Tidskriftsartikel (refereegranskat)abstract
    • This study examined the effects of inactive ions - ions not reacting with wood - during kraft cooking, which thus far have received modest attention. Six different sodium salts were added to kraft cooking liquors at two different levels of alkalinities. Delignification as well as the formation and degradation of hexenuronic acid (HexA) were observed of Scots pine sapwood meal. The delignification rate was greatly affected by the presence of additional anions. Chloride ions had the greatest retarding effect, while the addition of polyacrylate ions had almost no effect. When carbonate, sulphate and lactate ions were added to the liquors, the delignification rates were in-between the series with chloride and polyacrylates ions. We suggest that the anions affect the solubility of lignin fragments in analogy to the Hofmeister effect observed in various macromolecular systems in the presence of dissolved salts. When the reactions involving HexA were examined, the opposite results were obtained. In that case, the highest reaction rates were in the presence of chloride ions, and the lowest rates were obtained when no extra ions were added, and the second lowest rates were obtained in the presence of polyacrylate ions. As for delignification, the cooking series containing carbonate, sulphate and lactate ions had a reaction rate in-between the series with the highest and lowest rates. The differences obtained with various inorganic ions can be qualitatively explained by the Donnan equilibrium theory and by the variation in activity coefficients of hydroxide ions. Findings imply that knowledge of kraft cooking is far from complete. The effects of inactive ions on reaction kinetics should also receive more attention. © 2009 by Walter de Gruyter.
  •  
37.
  •  
38.
  •  
39.
  • Bogren, Johannes, 1979, et al. (författare)
  • Reaction kinetics of softwood kraft delignification –General considerations and experimental data
  • 2007
  • Ingår i: Nordic Pulp and Paper Research Journal. - 2000-0669 .- 0283-2631. ; 22:2, s. 177-183
  • Tidskriftsartikel (refereegranskat)abstract
    • For a delignification reaction to occur, cooking chemicals must be transported to the reaction site. After fragmentation reactions in the lignin structure, lignin fragments need to be solubilised in order to diffuse out of the fibre wall and complete the complicated delignification reaction. Despite major research efforts, there are still several aspects of this complex process that are not fully understood. This study is part of a larger investigation aimed at increasing the knowledge of the reaction kinetics of a kraft cook.In the present paper, different aspects of reaction kinetics of delignification and approaches to the modelling of kraft delignification are discussed. In the experimental part, the effect of active chemical concentrations on the reaction kinetics of delignification of Scots pine (Pinus silvestris) was investigated at five temperature levels. Cooks with the addition of an industrial softwood black liquor and increased sodium ion concentration were also performed. To minimise the influence of mass transport on the reaction rates, wood meal was used as a substrate and all cooks were conducted at a high liquor-to-wood ratio (200: 1) to minimise the deviation from initial bulk concentrations.The rate of delignification in the kraft cook increased with increasing hydrosulphide ion and hydroxide ion concentrations. An increase in sodium ion concentration retarded the rate of delignification, while an increase in concentration of dissolved kraft lignin in the cooking liquor increased the delignification rate during the main part of the cook. These results qualitatively resemble many of the results found in the literature. Indications of the influence of covalent bonds between lignin and carbohydrates on the delignification rate are shown and discussed. Data obtained in this investigation cover a broad range of cooking conditions, and are suitable for modelling the reaction kinetics of delignification without the influence of mass transfer resistance.
  •  
40.
  • Bogren, Johannes, 1979, et al. (författare)
  • Towards a general kraft delignification model
  • 2009
  • Ingår i: Nordic Pulp and Paper Research Journal. - 2000-0669 .- 0283-2631. ; 24:1, s. 33-37
  • Tidskriftsartikel (refereegranskat)
  •  
41.
  •  
42.
  •  
43.
  •  
44.
  • Brodin, Ida (författare)
  • Chemical Properties and Thermal Behaviour of Kraft Lignins
  • 2009
  • Licentiatavhandling (övrigt vetenskapligt/konstnärligt)abstract
    • Research concerning lignin has increased during the last years due to its renewability and ready availability in black liquor at pulp mills. Today, the kraft lignin found in black liquor is used as a fuel to gain energy in the recovery boiler at the mill. However, a new isolation concept, LignoBoost®, has enabled isolation of part of the lignin while allowing the use of black liquor as a fuel. This isolated lignin can be utilised as a fuel in, for example, thermal power stations or further upgraded to more value-added products. In this context, the most interesting value-added product is carbon fibre. The demand for carbon fibre has increased, but the biggest obstacle for a more extended use is the high production cost. About half of the production cost is related to the raw material. In this work, the possibility of using kraft lignin as a precursor for carbon fibre production has been investigated through fundamental studies. Kraft lignins originating from birch, Eucalyptus globulus, softwoods and softwoods from liner production have been studied. By separating the lignin while still in solution in the black liquor, unwanted large particles such as carbohydrates can easily be removed. After isolation according to the LignoBoost process and purification with the use of an ion-exchanger, the lignins have been both chemically and thermally characterised. Identification of the released compounds at different temperatures has been performed because only 40% of carbon relative to original lignin remains, down from theoretical 60% after thermal treatment up to 1000°C. The main released compounds were phenols, as revealed by pyrolysis-GC/MS. Additionally, a pre-oxidation was done in order to try to stabilise the lignins. It was shown that an oxidation prior to the thermal treatment increases the yield by more than 10% and that the main release of compounds takes place between 400°C and 600°C. Fractionated lignin is better qualified as raw material for carbon fibre production because it is purer and its softening temperature can be detected. Fractionated kraft lignins from all investigated wood sources have high possibilities to act as precursors for the manufacture of carbon fibre.
  •  
45.
  • Bylin, Susanne, 1982, et al. (författare)
  • Lignin Structure and Aggregation Behavior in a Two-Component Ionic Liquid Solvent System
  • 2014
  • Ingår i: BioResources. - : BioResources. - 1930-2126 .- 1930-2126. ; 9:4, s. 6002-6018
  • Tidskriftsartikel (refereegranskat)abstract
    • Ionic liquids are of potential interest in the processing of lignocellulosic biomass. In this study, the ionic liquid co-solvent system of 1-methylimidazole (MIM) and 1-ethyl-3-methyl-imidazolium acetate (EMIMAc) was used to solvate LignoBoost lignin fractionated from black liquor obtained from a kraft paper mill. Lignin ethanol-precipitated (LEP) and ethanol-soluble (LES) fractions were characterized via gel permeation chromatography (GPC) and 13C- and 31P-nuclear magnetic resonance spectroscopy (NMR) to determine structural characteristics and their relationship to polymer solubility in the system. Polymer integrity and solubility were optimal at ~20% lignin loading (w/w). Results showed that LEPs were generally of higher apparent molecular weight (Mw) and enriched with condensed/aliphatic ether linkages and aliphatic hydroxyls. The LESs had a lower apparent Mw and were enriched with carboxylic and phenolic groups. This newly gained knowledge on lignin fractionation and aggregation in the present solvent system provides future opportunities for tuning fractionation/extraction to suit a specific biomass-derived product, e.g., carbon fibers
  •  
46.
  • Bylin, Susanne, 1982, et al. (författare)
  • Solvation behavior of cellulose and xylan in the MIM/EMIMAc ionic liquid solvent system – parameters for small scale solvation
  • 2014
  • Ingår i: BioResources. - : BioResources. - 1930-2126 .- 1930-2126. ; 9:1, s. 1038-1054
  • Tidskriftsartikel (refereegranskat)abstract
    • Ionic liquid treatment has been reported by several researchers as a possible step in the process of fractionating lignocellulosic biomass within the biorefinery concept. However, understanding how solvation can be achieved and how the feedstock biopolymers are affected is needed prior to a viable implementation. An effective two component solvent system for the wood components cellulose and xylan has been developed. Furthermore, the solvation of these components in the system consisting of the ionic liquid (IL) 1-ethyl-3-methylimidazolium acetate (EMIMAc) in a novel combination with the co-solvent 1-methylimidazole (MIM) is investigated. Focused beam reflectance measurement (FBRM) particle characterization in combination with microscopic analysis and molecular weight determinations (xylan) shows that cellulose and xylan can be most efficiently solvated using only 3 to 4% IL (n/n anhydro-glucose units and n/n anhydro-xylose units) and 9% IL, respectively, while still avoiding any significant polymer degradation. A model for a two-step process of cellulose solvation in the present system is proposed.
  •  
47.
  • Dang, Binh, 1980, et al. (författare)
  • Carbohydrate content of black liquor and precipitated lignin at different ionic strengths in flow-through kraft cooking
  • 2018
  • Ingår i: Holzforschung. - : Walter de Gruyter GmbH. - 1437-434X .- 0018-3830. ; 72:7, s. 539-547
  • Tidskriftsartikel (refereegranskat)abstract
    • The influence of sodium ion concentration [Na+] on the dissolution of carbohydrates in black liquor (BL) during flow-through kraft cooking of Scots pine wood meal (Pinus sylvestris) was studied. Fractions of BL were collected at different times and the carbohydrate content of the various fractions was analysed. Lignin was precipitated from the BL by lowering the pH, and the carbohydrate content of the precipitated lignins (Lprec) was also examined. The molecular weight distribution (MWD) of the Lprecsamples was analysed. Xylose (Xyl) was found to be the most predominant sugar in BL aside from arabinose (Ara) and galactose (Gal), while the amounts of these sugars decreased with increasing levels of [Na+] in the cooking liquor. The minor amounts of mannose (Man) found in BL was not influenced by the [Na+]. The effects of NaCl and Na2CO3on the carbohydrate dissolution were similar, but slightly lower concentrations of Ara and Xyl were found in the case of NaCl application. All of the Lprecsamples contained some carbohydrate residues, the contents of which increased with increasing cooking time and decreased with higher [Na+]. It can be concluded that arabinoglucuronoxylan (AGX) along with arabinogalactans (AG) and arabinan, are covalently linked to lignin. The glucose (Glc) residue detected in Lprecmay originate from 1,3-β-glucan linked to lignin.
  •  
48.
  •  
49.
  • Dang, Binh, 1980, et al. (författare)
  • Effect of sodium ion concentration profile during softwood kraft pulping on delignification rate, xylan retention and reactions of hexenuronic acids
  • 2014
  • Ingår i: Nordic Pulp and Paper Research Journal. - 2000-0669 .- 0283-2631. ; 29:4, s. 604-611
  • Tidskriftsartikel (refereegranskat)abstract
    • The objective of this investigation was to study how different concentration profiles of sodium ions influence the delignification rate, hexenuronic acid formation/degradation and xylan retention under kraft cooking conditions. The concentration of sodium ions was varied in time between 0.52 and 3.00 mol/kg solvent, taking two different routes by the controlled addition of sodium carbonate. The reaction rates of hexenuronic acid were found to increase when the sodium ion concentration was at the higher level. Furthermore, the results implied that the kinetics of hexenuronic acid reactions responds rapidly to changes in sodium ion concentration. Delignification and the removal rates of xylan decreased rapidly after the sodium ion concentration was increased. However, when the sodium ion concentration was decreased, the response to the change was delayed. These findings indicate that effects of ionic strength on the rate of delignification and removal of xylan arise as a consequence of changes in solubility and on mass transport phenomena rather than from the rates of chemical reaction. Furthermore, the results suggest that non-dissolved xylan located in the fibre wall matrix may also sorb on cellulose surfaces relatively early on in the cook if the concentration of sodium ions is at high level.
  •  
50.
  • Dang, Binh, 1980, et al. (författare)
  • Impact of ionic strength on delignification and hemicellulose removal during kraft cooking in a small-scale flow-through reactor
  • 2013
  • Ingår i: Nordic Pulp & Paper Research Journal. - : Walter de Gruyter GmbH. - 0283-2631 .- 2000-0669. ; 28:3
  • Tidskriftsartikel (refereegranskat)abstract
    • The effect of ionic strength/sodium ion concentration and type of anions on the delignification rate, the retention of xylan and the reactions of hexenuronic acid during kraft cooking has been investigated. A novel, small, flow-through digester was used in the cooking experiments in order to prevent the resorption of lignin and xylan and to maintain a constant concentration of active chemicals throughout the kraft cook. An increase in ionic strength/sodium ion concentration in the cooking liquor decreases the removal rate of both lignin and xylan during kraft cooking. In general, the removal rate of xylan tends to correlate with the delignification rate. However, the present investigation finds that the retention of xylan at a given degree of delignification increases at high ionic strength/sodium ion concentration. The addition of sodium salts of carbonate or chloride to the cooking liquor was shown to increase the rate of formation/degradation reactions of hexenuronic acids and the total amount of uronic acids substituted on the xylan backbone decreases when the concentration of sodium ions increases in the cooking liquor. This promotes a decrease in the dissolution of xylan and consequently an increase in the retention of xylan in the wood residues. The obtained results demonstrate that the xylan content in the fiber wall increases at higher ionic strength/sodium ion concentration, which leads to a slight increase in pulp yield.
  •  
Skapa referenser, mejla, bekava och länka
  • Resultat 1-50 av 254
Typ av publikation
tidskriftsartikel (176)
konferensbidrag (67)
rapport (2)
annan publikation (2)
doktorsavhandling (2)
bokkapitel (2)
visa fler...
licentiatavhandling (2)
patent (1)
visa färre...
Typ av innehåll
refereegranskat (210)
övrigt vetenskapligt/konstnärligt (42)
populärvet., debatt m.m. (2)
Författare/redaktör
Theliander, Hans, 19 ... (192)
Theliander, Hans (58)
Brelid, Harald, 1960 (29)
Sedin, Maria, 1972 (28)
Hasani, Merima, 1978 (20)
Mattsson, Tuve, 1979 (19)
visa fler...
Köhnke, Tobias (17)
Bogren, Johannes, 19 ... (14)
Richards, Tobias, 19 ... (13)
Andersson, Sven-Ingv ... (12)
Vamling, Lennart, 19 ... (12)
Hedlund, Artur (12)
Jedvert, Kerstin (11)
Mattsson, Tuve (10)
Mattsson, Cecilia, 1 ... (10)
Henriksson, Gunnar (9)
Maschietti, Marco, 1 ... (8)
Åmand, Lars-Erik, 19 ... (8)
Lindström, Mikael E. (8)
Dang, Binh, 1980 (8)
Saltberg, Anna, 1978 (8)
Nohlgren, Ingrid (8)
Westman, Gunnar, 196 ... (7)
Tomani, Per (7)
Bengtsson, Jenny (7)
Belkheiri, Tallal, 1 ... (7)
Olausson, L. (7)
Köhnke, Tobias, 1978 (7)
Bialik, Marta Anna, ... (7)
Moosavifar, Ali Seid ... (7)
Durruty, Julie, 1988 (7)
Lawoko, Martin (6)
Lindau, Jenny, 1975 (6)
Hasani, Merima (6)
Ahlbom, Anders, 1993 (5)
Nielsen, Rudi (5)
Karna, Nabin Kumar, ... (5)
Nguyen Lyckeskog, Hu ... (5)
Helander, Mikaela (5)
Lyckeskog, Huyen, 19 ... (4)
Mahmoudkhani, Maryam ... (4)
Lindström, Mikael (4)
Sedin, Maria, PhD (4)
Theliander, Hans, Pr ... (4)
Wang, Yan (4)
Lindgren, K. (4)
Dingwell, Kristofer, ... (4)
Sewring, Tor (4)
Ragauskas, A. J. (4)
Olausson, Lars, 1945 (4)
visa färre...
Lärosäte
Chalmers tekniska högskola (218)
Kungliga Tekniska Högskolan (58)
RISE (36)
Luleå tekniska universitet (9)
Lunds universitet (6)
Göteborgs universitet (2)
visa fler...
Mittuniversitetet (2)
Linköpings universitet (1)
Högskolan i Borås (1)
Karlstads universitet (1)
visa färre...
Språk
Engelska (253)
Svenska (1)
Forskningsämne (UKÄ/SCB)
Teknik (233)
Naturvetenskap (78)
Lantbruksvetenskap (14)
Medicin och hälsovetenskap (1)
Samhällsvetenskap (1)

År

Kungliga biblioteket hanterar dina personuppgifter i enlighet med EU:s dataskyddsförordning (2018), GDPR. Läs mer om hur det funkar här.
Så här hanterar KB dina uppgifter vid användning av denna tjänst.

 
pil uppåt Stäng

Kopiera och spara länken för att återkomma till aktuell vy