Academic literature on the topic 'Sulphate cellulose'
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Journal articles on the topic "Sulphate cellulose"
Kovensky, J., B. Sassetti, A. Fernández Cirelli, and L. Kordich. "Low Anticoagulant Activity of High Sulphated Heparan Sulphates." Thrombosis and Haemostasis 63, no. 03 (1990): 488–92. http://dx.doi.org/10.1055/s-0038-1645071.
Full textBateman, T. J., K. S. Dodgson, and G. F. White. "Primary alkylsulphatase activities of the detergent-degrading bacterium Pseudomonas C12B. Purification and properties of the P1 enzyme." Biochemical Journal 236, no. 2 (June 1, 1986): 401–8. http://dx.doi.org/10.1042/bj2360401.
Full textMatts, P. J., G. F. White, and W. J. Payne. "Purification and characterization of the short-chain alkylsulphatase of coryneform B1a." Biochemical Journal 304, no. 3 (December 15, 1994): 937–43. http://dx.doi.org/10.1042/bj3040937.
Full textHorwood, Jennifer. "Cellulose sulphate microbicide trial halted." Lancet Infectious Diseases 7, no. 3 (March 2007): 183. http://dx.doi.org/10.1016/s1473-3099(07)70039-7.
Full textDachavaram, Soma Shekar, Narsimha R. Penthala, Julie L. Calahan, Eric J. Munson, and Peter A. Crooks. "Highly sulphated cellulose: a versatile, reusable and selective desilylating agent for deprotection of alcoholic TBDMS ethers." Organic & Biomolecular Chemistry 16, no. 33 (2018): 6057–62. http://dx.doi.org/10.1039/c8ob01438h.
Full textGil-Castell, Oscar, Pablo Reyes-Contreras, Pabla Andrea Barra, Regis Teixeira Mendonça, Isabel Carrillo-Varela, José David Badia, Angels Serra, and Amparo Ribes-Greus. "The Role of Eucalyptus Species on the Structural and Thermal Performance of Cellulose Nanocrystals (CNCs) Isolated by Acid Hydrolysis." Polymers 14, no. 3 (January 21, 2022): 423. http://dx.doi.org/10.3390/polym14030423.
Full textFedoskin, I. A., E. D. Sofronova, and V. A. Lipin. "BLEACHING OF SULPHATE CELLULOSE FROM HARDWOOD." Вестник Санкт-Петербургского государственного университета технологии и дизайна. Серия 4: Промышленные технологии, no. 3 (2020): 90–94. http://dx.doi.org/10.46418/2619-0729_2020_3_8.
Full textLidholt, K., L. Kjellén, and U. Lindahl. "Biosynthesis of heparin. Relationship between the polymerization and sulphation processes." Biochemical Journal 261, no. 3 (August 1, 1989): 999–1007. http://dx.doi.org/10.1042/bj2610999.
Full textAntušková, V., and I. Kučerová. "The impact of inorganic compounds used for protection of wood on cellulose." Koroze a ochrana materialu 58, no. 2 (June 1, 2014): 36–42. http://dx.doi.org/10.2478/kom-2014-0008.
Full textKarim, Latiffah, and Shikh Mohd Shahrul Nizan Shikh Zahari. "Stability of cellulases in ionic liquids." Malaysian Journal of Fundamental and Applied Sciences 15, no. 3 (June 25, 2019): 432–35. http://dx.doi.org/10.11113/mjfas.v15n3.1297.
Full textDissertations / Theses on the topic "Sulphate cellulose"
Риляков, Ілля Леонідович. "Підвищення ефективності технології виробництва сигаретного паперу." Master's thesis, КПІ ім. Ігоря Сікорського, 2020. https://ela.kpi.ua/handle/123456789/38492.
Full textTheme actuality. Expansion of the raw material base of the pulp and paper industry of Ukraine due to the use of pulp from agricultural waste. Production of cigarette paper and ensuring the stability of its quality through the use of the latest advances in paper production and modern technologies for pulp production. The purpose and objectives of the study. The purpose of the dissertation is to study the features of cigarette paper and improve the technology of its production to improve product quality. To achieve the goal, you need to solve the following tasks: - acquaintance with the properties of cigarette paper; - to obtain straw cellulose by oxidative-organosolvent method of delignification and to investigate its paper-forming properties; - to improve the technological process of cigarette paper production; - select and calculate the main technological equipment. - to analyze the potential of this work for use in startups. Object of study: the process of making document paper. Subject of study: processes of production of straw cellulose and production of cigarette paper. Methods of study: technological parameters of the process of delignification of wheat straw chips, parameters of the processes of forming, pressing, gluing and drying of paper web. The practical value of the obtained results: the proposed technological stream for the production of cigarette paper with the use of straw pulp will improve the quality of finished products and reduce its cost. Approval of the thesis results: The main provisions of the dissertation were reported and discussed at the international international conference IV international scien-tific and practical conference. The world of science and innovation, London, United Kingdom, 11-13 November, 2020.
Silva, Marileide Gomes da. "Produtividade, idade e qualidade de madeira de Eucalyptus destinada à produção de polpa celulósica branqueada." Universidade de São Paulo, 2011. http://www.teses.usp.br/teses/disponiveis/11/11150/tde-17032011-162129/.
Full textThis study aimed to determine the influence of productivity and age on wood quality from hybrid clones of Eucalyptus grandis x Eucalyptus urophylla for bleached pulp production. The material considered were collected in areas with high productivity, an average of 33 m3 ha-1 year-1, clay soils and low-productive areas, an average of 17 m3 ha-1 year-1, sandy soils. In both types of soils, we evaluated trees aged 4, 5, 6 and 7 years, from forest stands from the state of Pará Brazil. For each sample were used 10 average trees (diameter). Materials were evaluated for chemical composition, basic density and performance in relation to the kraft pulping process. The cooking was performed at 166°C with 60 min heating, 85 min cooking and alkali charge varying according to the needs of each material to obtain kappa number of 18±0.5. Results showed that the basic density of wood increases with age, ranging from 0.510 to 604 g cm-3 with 4 and 7 years, respectively. This increased density in older ages is possibly explained by the higher proportion of mature wood, in relation to juvenile wood. The total amount of extractives also increased with age varying from 4.9 to 5.7% with 4 and 7 years, respectively. The amount of lignin was not significantly different ranging from 29.26 to 29.72%. Samples from clay soils had a higher yield of pulp (50 to 52%), and required lower alkali charge (21 to 24.5% active alkali) to the same level of delignification (kappa number 18±0.5); for samples from sandy soil alkali charge was 21.5 to 25% and yield of 48 to 51%. Pulp from material derived from clay soils had less hexenuronic acid and higher viscosity, which is justified by the lower alkali applied. In addition, also presented better physical and mechanical propert ies such as specific volume, air resistance, tensile, tear and burst index. Wood from an area of high productivity showed better quality for pulp production over an area of low productivity, for consuming a smaller amount of chemical charge to the same kappa number, higher pulp yield, pulp with higher viscosity and better physical and mechanical properties.
Mayende, Lungisa. "Isolation of a Clostridium Beijerinckii sLM01 cellulosome and the effect of sulphide on anaerobic digestion." Thesis, Rhodes University, 2007. http://hdl.handle.net/10962/d1004032.
Full textWalter, Karin. "Influence of acid hydrogen peroxide treatment on refining energy and TMP properties." Licentiate thesis, Mid Sweden University, Department of Natural Sciences, Engineering and Mathematics, 2009. http://urn.kb.se/resolve?urn=urn:nbn:se:miun:diva-9207.
Full textThe potential of using acid hydrogen peroxide under Fenton conditions to lower the electrical energy consumed during the production of Black spruce (Picea mariana) thermomechanical pulp (TMP) was investigated. The chemical system, which consisted of ferrous sulphate, hydrogen peroxide and optionally an enhancer (3,4-dimethoxybenzyl alcohol, ethylenediaminetetraacetic acid or oxalic acid/sodium oxalate), was evaluated as an inter-stage treatment where the primary refiner was used as a mixer. The produced TMPs were thoroughly characterised in order to explain the effect of the chemical system on fibre development and to be able to propose a mechanism for the impact on refining energy reduction. The possibility to improve the optical properties by washing, chelating and sodium dithionite or hydrogen peroxide bleaching the treated pulps was evaluated.
The results obtained in a pilot plant trial show that it is possible to significantly reduce the comparative specific energy consumption by approximately 20% and 35% at a freeness value of 100 ml CSF or a tensile index of 45 Nm/g by using 1% and 2% hydrogen peroxide respectively. The energy reduction is obtained without any substantial change in the fractional composition of the pulp, though tear strength is slightly reduced, as are brightness and pulp yield. No major differences between the reference pulp and the chemically treated pulps were found with respect to fibre length, width or cross-sectional dimensions. However, the acid hydrogen peroxide-treated pulps tend to have more collapsed fibres, higher flexibility, a larger specific surface area and a lower coarseness value. The yield loss accompanying the treatment is mainly a consequence of degraded hemicelluloses. It was also found that the total charge of the chemically treated pulps is higher compared to the reference pulps, something that may have influenced the softening behaviour of the fibre wall.
A washing or chelating procedure can reduce the metal ion content of the chemically treated TMPs considerably. The amount of iron can be further reduced to a level similar to that of untreated pulps by performing a reducing agent-assisted chelating stage (QY) with dithionite. The discoloration cannot, however, be completely eliminated. The brightness decrease of the treated pulps is thus not only caused by higher iron content in the pulp, but is also dependent on the type of iron compound and/or other coloured compounds connected with the acid hydrogen peroxide treatment. Oxidative bleaching with hydrogen peroxide (P) is more effective than reductive bleaching with sodium dithionite in regaining the brightness lost during the energy reductive treatment. Using a QY P sequence, a hydrogen peroxide charge of 3.8% was needed to reach an ISO brightness of 75% for the chemically treated pulps. The corresponding hydrogen peroxide charge for the untreated TMP reference was 2.5%.
The radicals generated in the Fenton reaction will probably attack and weaken/soften the available outer fibre wall layers. This could facilitate fibre development and consequently lower the electrical energy demand for a certain degree of refinement.
Kilian, André. "Control of an acid sulphite batch pulp digester based on a fundamental process model." Pretoria : [s.n.], 1999. http://upetd.up.ac.za/thesis/available/etd-12202006-100726/.
Full textHinojosa, Eduardo Alberto Lazo. "Remoção de matéria orgânica e cor de efluente kraft por adsorção usando carvão ativado e argila." Universidade Tecnológica Federal do Paraná, 2014. http://repositorio.utfpr.edu.br/jspui/handle/1/1302.
Full textAtualmente há preocupação da sociedade em relação aos impactos gerados pelas indústrias ao meio ambiente. Para produção de celulose e de papel é usada grande quantidade de água, madeira e produtos químicos, sendo gerado efluente nos diferentes processos produtivos da indústria. A matéria orgânica e a cor do efluente do processo Kraft se devem à presença de moléculas derivadas da lignina que são difíceis de serem removidas ou biodegradadas. Com vistas à remedição deste efluente, o presente trabalho busca avaliar a remoção de cor e matéria orgânica residual de efluente de celulose Kraft pré-tratado biologicamente, usando carvão ativado de casca de coco e argila montmorilonita pelo método de adsorção através de delineamentos experimentais. Para remoção de cor e matéria orgânica foram avaliados os fatores: a) pH do efluente; b) massa do material adsorvente no processo de adsorção e c) temperatura. A capacidade de adsorção de matéria orgânica e cor no carvão ativado e argila montmorilonita foram determinados pelo modelo matemático de Langmuir e Freundlich, por meio de ensaios de construção de isotermas de adsorção em efluente Kraft. O efluente foi caracterizado quanto a DQO, DBO5,20, COT e cor verdadeira antes e depois do tratamento terciário. Para o tratamento do efluente foram empregadas duas temperaturas: 25 e 40°C, seguiu-se planejamento fatorial completo 32 em triplicata com ponto central tendo como variáveis pH (5,0; 6,0 e 7,0) e massa de material adsorvente (0,5; 1,0 e 1,5 g). O planejamento experimental utilizado permitiu obter os melhores resultados com carvão ativado em 40 °C, pH 7,0 e 1,5 g de adsorvente com remoção de: 98% de COT, 83% de DQO, 97% de DBO5,20 e 95% de cor verdadeira e para argila em temperatura de 40 oC, pH 7, e 1,5 g de adsorvente com remoção de: 55% de COT, 50% de DQO, 90% de DBO5,20, e 56% de cor verdadeira. A principal variável responsável pela remoção de cor e matéria orgânica foi a massa de adsorvente seguida do pH. Também foi avaliada a possibilidade de aproveitamento do resíduo obtido a partir do processo de adsorção na incorporação de cinzas de carvão na produção de argamassas com teores de 0,4%, 1,0% e 1,2%; em cimento portland, areia e água com tempos de cura de 7 e 28 dias fazendo testes de resistência à compressão. Para a reutilização da argila foram utilizados 15% de argila do processo de adsorção, 25% de vidro e 60% de argila vermelha, para a confecção de corpos de prova cerâmico à temperatura de 1100 oC a 1150 oC. De modo geral, o processo de tratamento proposto neste trabalho utilizando carvão ativado, demostrou ser boa alternativa comparado com argila montmorilonita para redução de cor e matéria orgânica residual do efluente de processo Kraft, tendo-se em vista a utilização da cinza do carvão utilizado no processo de adsorção como um agregado para formação de argamassas na construção civil e argila utilizada na adsorção como material cerâmico.
Nowadays, there is a concern of society regarding the impacts caused by the industries on the environment. Large amounts of water, wood and chemichal are used to produce cellulose and paper, and contaminated effluents are generated through the various industrial processes associated. The organic matter and the color of the Kraft effluent are due to the presence of lignin-derived molecules that are difficult to be removed or biodegraded. With intent to remediate this effluent, this study aim to evaluate the removal of color and residual organic matter from biologically pretreated Kraft effluent, using activated carbon from coconut shell and montmorillonite clay by adsorption method through experimental designs. For the color and organic matter removal, the following factors were evaluated: a) pH of the effluent; b) the mass of the adsorbent material in the adsorption process and c) temperature. The adsorption capacity of organic matter and color in the activated carbon and in the montmorillonite clay were determined by the mathematical model of Langmuir and Freundlich, by means of isotherm adsorption construction in Kraft effluent.The effluent was characterized by COD, DBO5,20, COT and true color before and after the tertiary treatment. For it treatment two temperatures were employed: 25 °C and 40 °C, followed by a 32 full factorial design with center point in triplicate, using pH (5.0, 6.0 and 7.0) and masses of adsorbent material (0.5, 1.0 and 1.5 g) as variables. The experimental design used showed that the best results with activated carbon are obtained at 40 ° C, pH 7.0 and 1.5 g of adsorbent with removals of 98% of TOC, 83% of COD, 97% of BOD5,25 and 95% of true color. With clay, the best results occurred at temperature of 40 ° C, pH 7, and 1.5 g of adsorbent to remove 55% of COT, 50% of COD, 90% of BOD5,20 and 56% of true color. The main responsible for the removal of color and organic matter was the mass of adsorbent, followed by the pH. It was also evaluated the possibility of using the residue obtained from the adsorption process in the incorporation of carbon ash to produce mortars with levels of 0.4%, 1.0% and 1.2% in Portland cement, sand and water, with curing times of 7 and 28 days, for which compressive strength tests were performed. To reuse the clay, 15% of the clay from the adsorption process was used, together with 25% of glass and 60% of red clay, in order to construct ceramics bodies specimen generated at temperatures from 1100 °C to 1150 °C. The treatment process proposed in this work using activated carbon demonstrated to be, in general, a good alternative compared to montmorillonite clay for the color reduction and residual organic matter removal from Kraft process effluent, while residues from both process can be used as aggregates for mortars and ceramic body production.
Gustavsson, Catrin. "On the Interrelation Between Kraft Cooking Conditions and Pulp Composition." Doctoral thesis, Stockholm, 2006. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-4232.
Full textÅkerholm, Margaretha. "Ultrastructural Aspects of Pulp Fibers as Studied by Dynamic FT-IR Spectroscopy." Doctoral thesis, KTH, Fibre and Polymer Technology, 2003. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-3609.
Full textDynamic (or 2D) FT-IR spectroscopy in combination withpolarized IR irradiation has been used in this work to studywood polymer orientation and interactions on theultrastructural level in wood fibers in the native state aswell as the effects of different pulping processes. The woodpolymer interactions were studied under both dry and humidconditions.
The matrix of lignin and hemicelluloses located between thewell-ordered cellulose fibrils in the wood cell wall of sprucewas here shown to be more highly ordered than has earlier beenrevealed. It was confirmed that glucomannan is orientedparallel to the cellulose fibrils and is highly coupled to it.The lignin was also shown to have a main orientation in thestructure although this is probably not as strong as that ofglucomannan. The orientation of the lignin may derive from thefact that the polysaccharides act as templates during thelignification of the cell wall. This organization implies thatnot only the cellulose but also the lignin and thehemicelluloses have different mechanical properties in thelongitudinal and cross-fiber directions.
The ability to gain molecular information on the stresstransfer in polymers with dynamic FT-IR spectroscopy made itpossible to verify experimentally earlier molecularcalculations on the stress transfer within the cellulose chain.It was also possible to show, on the molecular level, thedominant importance of the cellulose fibrils for the stresstransfer in the longitudinal direction of pulp fibers,including lignin-rich mechanical pulp fibers. The glucomannanof softwood fibers was also shown to participate in the stresstransfer in the fiber direction indicating a close associationwith the cellulose, whereas the xylan showed no dynamicresponse. Already under dry conditions, the lignin was shown tohave a more viscoelastic response than the polysaccharidesduring the loading of pulp fibers and it was thus able to moveindependently of the cellulose.
The enhanced spectral resolution obtained with dynamic FT-IRspectroscopy made it possible to study the crystalstructure/chain order of cellulose in pulp fibers. Thepossibility of following changes in the relative cellulose Iallomorph composition of pulp fibers was demonstrated for somechemical pulps.
Dynamic FT-IR experiments under humid conditions and ofelevated temperatures made it possible to study the softeningof the biopolymers in their native environment. This was alsodemonstrated for some different pulps, and this may be apromising tool for obtaining viscoelastic information on themolecular level in composite systems such as wood fibers.
Keywords:cellulose, cooperation, crystallinity, dynamictest, glucomannan, hardwood, holocellulose, humidity, infraredspectroscopy, kraft pulp, lignin, mechanical pulp, orientation,polarised light, softwood, strain, sulphite pulp,viscoelasticity, xylan
Ferreira, Hugo Miguel Lambuça. "Overcome challenges in influenza virus-like particles downstream process." Master's thesis, 2017. http://hdl.handle.net/10362/24817.
Full textO desenvolvimento de novas vacinas para o vírus de influenza introduziu uma nova geração de vacinas utilizando partículas semelhantes a vírus (VLPs). A ausência de material genético, possibilidade de produção em linhas celulares e presença de antigénios com imunogenicidade são as principais vantagens em relação às vacinas tradicionais. O desenvolvimento de um processo de purificação de baixo custo mantendo a elevada pureza, potencia e qualidade das VLPs é um desafio. Nesta tese, alguns passos de purificação – clarificação, concentração, cromatografia, polimento e filtração estéril final – foram estudados para desenvolver um novo processo de purificação de VLPs de influenza. Na clarificação, a estratégia usando os filtros D0HC seguido do Opticap XL SHC apresentaram os melhores resultados. Na concentração, a cassete com cut-off de 300 kDa apresentou um maior rendimento na recuperação de hemaglutinina e o mais baixo tempo de operação. Na cromatografia, a membrana Sartobind Q e a resina HiTrap Q HP foram avaliadas, concluindo-se que a resina apresenta maior capacidade de ligação dinâmica e maior resolução na eluição. No polimento, a cromatografia de exclusão molecular e a cromatografia multimodal, operada em flow-through comparadas. Esta última apresentou valores superiores de recuperação de hemaglutinina sendo escolhida por não conter limitações no escalamento. Diferentes materiais foram analisados na filtração estéril final. Na realização da corrida de prova de conceito as condições ótimas e os melhores materiais foram estudadas. No final do processo, obteve-se VLPs de influenza na concentração e qualidade suficiente para avançar para estudos em animais in vivo e para fase clínica I. Adicionalmente, uma nova ferramenta – partículas magnéticas de celulose sulfatada – foram estudadas com objetivo de obter VLPs purificadas e concentradas para utilização em técnicas de caracterização. Em geral, esta tese contribuiu para introduzir uma nova ferramenta e um novo processo de purificação mais económico com elevada pureza, potência e qualidade, para a nova geração de vacinas - VLPs.
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Book chapters on the topic "Sulphate cellulose"
Dautzenberg, H., B. Lukanoff, and K. Neubauer. "Sodium cellulose sulphate as a component for polyelectrolyte complex formation—preparation, characterisation, testing." In Cellulose and Cellulose Derivatives, 435–44. Elsevier, 1995. http://dx.doi.org/10.1533/9781845698539.5.435.
Full text"The Diversity of Uses for Cellulose Sulphate Encapsulation." In Bioencapsulation of Living Cells for Diverse Medical Applications, edited by John A. Dangerfield, Brian Salmons, Randolph Corteling, Jean-Pierre Abastado, John Sinden, Walter H. Gunzburg, and Eva M. Brandtner, 70–92. BENTHAM SCIENCE PUBLISHERS, 2013. http://dx.doi.org/10.2174/9781608057207113010006.
Full textBamitale Osho, Michael, and Sarafadeen Olateju Kareem. "Prospects of Biocatalyst Purification Enroute Fermentation Processes." In Fermentation - Processes, Benefits and Risks [Working Title]. IntechOpen, 2021. http://dx.doi.org/10.5772/intechopen.97382.
Full textNousiainen, Pertti, and Marianna Vehviläinen. "CELSOL - MODIFICATION OF PINE SULPHATE PAPER GRADE PULP WITH TRICHODERMA REESEI CELLULASES FOR FIBRE SPINNING." In Recent Advances in Environmentally Compatible Polymers, 371–78. Elsevier, 2001. http://dx.doi.org/10.1533/9781845693749.6.371.
Full textConference papers on the topic "Sulphate cellulose"
Romanova, Lidia, and Ilona V. Iakimova. "New approach to environmental engineering for sulphate cellulose production." In International Heat Transfer Conference 12. Connecticut: Begellhouse, 2002. http://dx.doi.org/10.1615/ihtc12.3560.
Full textSuckling, Paul, Nicola Calder, Paul Humphreys, Fraser King, and Helen Leung. "The Development and Use of T2GGM: A Gas Modelling Code for the Postclosure Safety Assessment of OPG’s Proposed L&ILW Deep Geologic Repository, Canada." In ASME 2009 12th International Conference on Environmental Remediation and Radioactive Waste Management. ASMEDC, 2009. http://dx.doi.org/10.1115/icem2009-16291.
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