7 resultados para Bacillus pumilus xylanase

em Doria (National Library of Finland DSpace Services) - National Library of Finland, Finland


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Membrane filtration has become increasingly attractive in the processing of both foodand biotechnological products. However, the poor selectivity of the membranes and fouling are the critical factors limiting the development of UF systems for the specific fractionation of protein mixtures. This thesis gives an overview on fractionation of proteins from model protein solutions or from biological solutions. An attempt was made to improve the selectivity of the available membranes by modifying the membranes and by exploiting the different electrostatic interactions between the proteins and the membrane pore surfaces. Fractionation and UF behavior of proteins in the model solutions and in the corresponding biological solutions were compared. Characterization of the membranes and protein adsorptionto the membrane were investigated with combined flux and streaming potential studies. It has been shown that fouling of the membranes can be reduced using "self-rejecting" membranes at pH values where electrostatic repulsion is achieved between the membrane and the proteins in solution. This effect is best shown in UF of dilute single protein solutions at low ionic strengths and low pressures. Fractionation of model proteins in single, binary, and ternary solutionshas been carried out. The results have been compared to the results obtained from fractination of biological solutions. It was generally observed that fractination of proteins from biological solutions are more difficult to carry out owingto the presence of non studied protein components with different properties. Itcan be generally concluded that it is easier to enrich the smaller protein in the permeate but it is also possible to enrich the larger protein in the permeateat pH values close to the isoelectric point of the protein. It should be possible to find an optimal flux and modification to effectively improve the fractination of proteins even with very similar molar masses.

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The first objective of this study was to find out reliable laboratory methods to predict the effect of enzymes on specific energy consumption and fiber properties of TMP pulp. The second one was to find with interactive software called “Knowledge discovery in databases” enzymes or other additives that can be used in finding a solution to reduce energy consumption of TMP pulp. The chemical composition of wood and enzymes, which have activity on main wood components were presented in the literature part of the work. The results of previous research in energy reduction of TMP process with enzymes were also highlighted. The main principles of knowledge discovery have been included in literature part too. The experimental part of the work contains the methods description in which the standard size chip, crushed chip and fiberized spruce chip (fiberized pulp) were used. Different types of enzymatic treatment with different dosages and time were tested during the experiments and showed. Pectinase, endoglucanase and mixture of enzymes were used for evaluation of method reliability. The fines content and fiber length of pulp was measured and used as evidence of enzymes' effect. The refining method with “Bauer” laboratory disc refiner was evaluated as not highly reliable. It was not able to provide high repeatability of results, because of uncontrolled feeding capacity and refining consistency. The refining method with Valley refiner did not have a lot of variables and showed stable and repeatable results in energy saving. The results of experiments showed that efficient enzymes impregnation is probably the main target with enzymes application for energy saving. During the work the fiberized pulp showed high accessibility to enzymatic treatment and liquid penetration without special impregnating equipment. The reason was that fiberized pulp has larger wood surface area and thereby the contact area between the enzymatic solution and wood is also larger. Standard size chip and crushed chip treatment without special impregnator of enzymatic solution was evaluated as not efficient and did not show visible, repeatable results in energy consumption decrease. Thereby it was concluded that using of fiberized pulp and Valley refiner for measurements of enzymes' effectiveness in SEC decrease is more suitable than normal size chip and crushed chip with “Bauer” refiner. Endoglucanase with 5 kg/t dosage showed about 20% energy consumption decrease. Mixture of enzymes with 1.5 kg/t dosage showed about 15% decrease of energy consumption during the refining. Pectinase at different dosages and treatment times did not show significant effect on energy consumption. Results of knowledge discovery in databases showed the xylanase, cellulase and pectinase blend as most promising for energy reduction in TMP process. Surfactants were determined as effective additives for energy saving with enzymes.

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Prosessiteollisuudessa tarvitaan usein erilaisia apujärjestelmiä pääprosessin tueksi. Tyypillisiä tällaisia järjestelmiä ovat jäähdytys-, höyry- ja ilmajärjestelmät. Hyödykejärjestelmien kehitys jää helposti pääprosessin varjoon, joka usein johtaa tarpeettoman suuriin hyödykekustannuksiin ja järjestelmien teknisen tilan laskuun. Työn kirjallisuusosassa käsitellään Roal Oy:n fermentointiprosessin kannalta olennaisimpia hyödykevaatimuksia, niiden laskennallista ilmaisua ja vuorovaikutuksia sekä PINCH-menetelmää lämpöenergian hyötykäyttöön. Jäähdytysjärjestelmän osalta käydään läpi merkittävimmät laitetekniset ratkaisut, jäähdytystorni ja lämpöpumppu, toimintaperiaatteineen sekä luonnonvesien käyttö jäähdytykseen. Työn soveltavassa osassa seurattiin Aspergillus, Trichoderma ja Bacillus fermentointeja, joiden pohjalta luotiin kasvatuskohtainen empiirinen malli jäähdytystarpeen arviointiin perustuen sekoitustehoon, kasvatuksen hiilidioksidituottoon ja haihtumisen vaikutukseen. Kasvatuksien aikana seurattiin myös tilavuusperusteista lämmönsiirtokerrointa. Mitattujen lämmönsiirtokertoimien perustella laskettiin ominaislämmöntuottoon perustuva maksimilämpötila käytettävälle jäähdytysvedelle ja fermentorien maksimitilavuudet tunnetuilla kasvatusparametreilla eri lämpöisille jäähdytysvesille. Soveltavassa osassa käydään myös läpi Roalin höyry- ja kuumavesikulutukset ja tärkeimmät käyttökohteet. Mittaustulosten ja mallien perusteella on tehtiin kehitysehdotukset hyödykejärjestelmän optimoimiseksi.

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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 objective of this work was to study the effects of partial removal of wood hemicelluloses on the properties of kraft pulp.The work was conducted by extracting hemicelluloses (1) by a softwood chip pretreatment process prior to kraft pulping, (2) by alkaline extraction from bleached birch kraft pulp, and (3) by enzymatic treatment, xylanase treatment in particular, of bleached birch kraft pulp. The qualitative and quantitative changes in fibers and paper properties were evaluated. In addition, the applicability of the extraction concepts and hemicellulose-extracted birch kraft pulp as a raw material in papermaking was evaluated in a pilot-scale papermaking environment. The results showed that each examined hemicellulose extraction method has its characteristic effects on fiber properties, seen as differences in both the physical and chemical nature of the fibers. A prehydrolysis process prior to the kraft pulping process offered reductions in cooking time, bleaching chemical consumption and produced fibers with low hemicellulose content that are more susceptible to mechanically induced damages and dislocations. Softwood chip pretreatment for hemicellulose recovery prior to cooking, whether acidic or alkaline, had an impact on the physical properties of the non-refined and refined pulp. In addition, all the pretreated pulps exhibited slower beating response than the unhydrolyzed reference pulp. Both alkaline extraction and enzymatic (xylanase) treatment of bleached birch kraft pulp fibers indicated very selective hemicellulose removal, particularly xylan removal. Furthermore, these two hemicellulose-extracted birch kraft pulps were utilized in a pilot-scale papermaking environment in order to evaluate the upscalability of the extraction concepts. Investigations made using pilot paper machine trials revealed that some amount of alkalineextracted birch kraft pulp, with a 24.9% reduction in the total amount of xylan, could be used in the papermaking stock as a mixture with non-extracted pulp when producing 75 g/m2 paper. For xylanase-treated fibers there were no reductions in the mechanical properties of the 180 g/m2 paper produced compared to paper made from the control pulp, although there was a 14.2% reduction in the total amount of xylan in the xylanase-treated pulp compared to the control birch kraft pulp. This work emphasized the importance of the hemicellulose extraction method in providing new solutions to create functional fibers and in providing a valuable hemicellulose co-product stream. The hemicellulose removal concept therefore plays an important role in the integrated forest biorefinery scenario, where the target is to the co-production of hemicellulose-extracted pulp and hemicellulose-based chemicals or fuels.

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Phosphoserine aminotrasferase (PSAT: EC 2.6.1.52) is a vitamin B6-dependent enzyme and a member of the subgroup IV in the aminotransferase superfamily. Here, X-ray crystallography was used to determine the structure of PSAT from Bacillus alcalophilus with pyridoxamine 5′-phosphate (PMP) at high resolution (1.57 Å). In addition, analysis of active residues and their conformational changes was performed. The structure is of good quality as indicated, for example, by the last recorded Rwork and Rfree numbers (0.1331 and 0.1495, respectively). The enzyme was initially crystallized in the presence of substrate L-glutamate with the idea to produce the enzyme-substrate complex. However, the structure determination revealed no glutamate bound at the active site. Instead, the Schiff base between Lys196 and PLP appeared broken, resulting in the formation of PMP owing to the excess of the donor substrate used during co-crystallization. Structural comparison with the free PSAT enzyme and the PSAR-PSER complex showed that the aromatic ring of the co-factor remains in almost the same place in all structures. A flexible nearby loop in the active site was found in the same position as in the free PSAT structure while in the PSAT-PSER structure it moves inwards to interact with PSER. B-factors comparison in all three structures (PSAT-PMP complex, free PSAT, and PSAT-PSER complex) showed elevated loop flexibility in the absence of the substrate, indicating that loop flexibility plays an important role during substrate binding. The reported structure provides mechanistic details into the reaction mechanism of PSAT and may help in understanding better the role of various parts in the structure towards the design of novel compounds as potential disruptors of PSAT function. This may lead to the development of new drugs which could target the human and bacterial PSAT active site.