984 resultados para continuous pulp digester control


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Työssä tarkastellaan yleisiä menetelmiä säätöpiirien suorituskyvyn analysointiin ja sovelletaan niitä jatkuvatoimisen sellukeittimen säätöihin. Esitellyt menetelmät tarjoavat keinoja myös huonon säätötuloksen syyn selvittämiseen ja vinkkejä paremman suorituskyvyn saavuttamiseksi. Analyysissä edettiin top-down periaatteen mukaisesti lähtien liikkeelle keittimen tärkeimmästä säädöstä eli kappaluvun säädöstä. Sitten etsittiin tähän vaikuttavia tekijöitä mitatuista suureista. Seuraavaksi arvioitiin tärkeimmäksi katsotun tekijän (hakepinnankorkeus) säädön suorituskyky, jossa havaittiin parannettavaa. Lopuksi hakepinnankorkeuden säädön viritystämuutettiin ja tehtiin identifiointikoe säätörakenteen uudelleen järjestelyä varten.

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The paper develops a method to solve higher-dimensional stochasticcontrol problems in continuous time. A finite difference typeapproximation scheme is used on a coarse grid of low discrepancypoints, while the value function at intermediate points is obtainedby regression. The stability properties of the method are discussed,and applications are given to test problems of up to 10 dimensions.Accurate solutions to these problems can be obtained on a personalcomputer.

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Control of chaos in the single-mode optically pumped far-infrared (NH3)-N-15 laser is experimentally demonstrated using continuous time-delay control. Both the Lorenz spiral chaos and the detuned period-doubling chaos exhibited by the laser have been controlled. While the laser is in the Lorenz spiral chaos regime the chaos has been controlled both such that the laser output is cw, with corrections of only a fraction of a percent necessary to keep it there, and to period one. The laser has also been controlled while in the period-doubling chaos regime, to both the period-one and -two states.

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We develop an extension to the tactical planning model (TPM) for a job shop by the third author. The TPM is a discrete-time model in which all transitions occur at the start of each time period. The time period must be defined appropriately in order for the model to be meaningful. Each period must be short enough so that a job is unlikely to travel through more than one station in one period. At the same time, the time period needs to be long enough to justify the assumptions of continuous workflow and Markovian job movements. We build an extension to the TPM that overcomes this restriction of period sizing by permitting production control over shorter time intervals. We achieve this by deriving a continuous-time linear control rule for a single station. We then determine the first two moments of the production level and queue length for the workstation.

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Excitation-continuous music instrument control patterns are often not explicitly represented in current sound synthesis techniques when applied to automatic performance. Both physical model-based and sample-based synthesis paradigmswould benefit from a flexible and accurate instrument control model, enabling the improvement of naturalness and realism. Wepresent a framework for modeling bowing control parameters inviolin performance. Nearly non-intrusive sensing techniques allow for accurate acquisition of relevant timbre-related bowing control parameter signals.We model the temporal contour of bow velocity, bow pressing force, and bow-bridge distance as sequences of short Bézier cubic curve segments. Considering different articulations, dynamics, and performance contexts, a number of note classes are defined. Contours of bowing parameters in a performance database are analyzed at note-level by following a predefined grammar that dictates characteristics of curve segment sequences for each of the classes in consideration. As a result, contour analysis of bowing parameters of each note yields an optimal representation vector that is sufficient for reconstructing original contours with significant fidelity. From the resulting representation vectors, we construct a statistical model based on Gaussian mixtures suitable for both the analysis and synthesis of bowing parameter contours. By using the estimated models, synthetic contours can be generated through a bow planning algorithm able to reproduce possible constraints caused by the finite length of the bow. Rendered contours are successfully used in two preliminary synthesis frameworks: digital waveguide-based bowed stringphysical modeling and sample-based spectral-domain synthesis.

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Diplomityön tarkoituksena oli selvittää kuitujen kihartuvuuden profiili koivu- ja havusellulinjalla prosessivaiheiden suhteen. Profiilin perusteella pyrittiin selvittämään kuitulinjojen prosessista kuitujen kiharuuteen voimakkaimmin vaikuttavia tekijöitä. Työn kirjallisuusosassa käsiteltiin kuitujen ominaisuuksia sekä teollisen sellun valmistusprosessin kuituihin aiheuttamia kuituvaurioita ja niiden mahdollisia syitä. Lisäksi käytiin läpi kuituvaurioiden analysointimenetelmiä ja kuituvaurioiden kanssa korreloivia sellun laatuarvoja. Työn kokeellinen osa suoritettiin kuitulinjojen normaalin tuotannon ohessa. Kokeellisen osan massanäytteitä otettiin varsin moninaisista tuotantotilanteista mahdollisimman kattavan kiharuusprofiilin aikaansaamiseksi. Koivusellulinjalla vuokeittimen tuotantotaso vaikutti suuresti valmistettavan sellun ominaisuuksiin. Kuituvaurioiden syntyyn voimakkaimmin vaikuttavaksi tekijäksi osoittautui keittimen pohja-alueen, puskun ja massan pesuvaiheen sakeus. Tämän alueen sakeus muuttui tuotantotason mukaan, tuotantotason kasvun myötä alueen sakeus laski. Sakeuden lasku vähensi kuitujen kiharuutta sekä massan venymää ja paransi vetojäykkyyttä. Tuotantotason kasvu paransi myös keittimestä otettujen massanäytteiden vetojäykkyyspotentiaalia. Havusellulinjalla käytetyn Lo-Solids –keittomallin ja konventionaalisen keittomallin kesken esiintyi varsin merkittäviä laadullisia eroja. Lo-Solids –keittomallilla keitetyt sellukuidut kihartuivat konventionaalisella keittomallilla keitettyjä sellukuituja enemmän. Lo-Solids –keittomallilla keitetyn sellun vetojäykkyys oli konventionaalisella mallilla keitetyn sellun vetojäykkyyttä heikompi.

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This paper presents two discrete sliding mode control (SMC) design. The first one is a discrete-time SMC design that doesn't take into account the time-delay. The second one is a discrete-time SMC design, which takes in consideration the time-delay. The proposed techniques aim at the accomplishment simplicity and robustness for an uncertainty class. Simulations results are shown and the effectiveness of the used techniques is analyzed. © 2006 IEEE.

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Biopulping of Eucalyptus grandis wood chips with Phanerochaete chrysosporium RP-78 was evaluated under non-aseptic conditions in laboratory and mill wood-yard. The ability of P. chrysosporium to compete with indigenous fungi present in fresh wood chips was notorious under controlled laboratory experiments. A subsequent step involved an industrial test performed with 10-ton of fresh wood chips inoculated and maintained at 37 +/- 38 degrees C for 39 days in a biopulping pilot plant. Biotreated wood chips were pulped in a chemithermomechanical pulping mill. Net energy consumption during refining was 745 kWh ton(-1) and 610 kWh ton(-1) of processed pulp for control and biotreated wood chips, respectively. Accordingly, 18.5% net energy saving could be achieved. Biopulps contained lower shive content and had improved strength properties compared to control pulps. Tensile index improved from 25 +/- 1 N m g(-1) to 33.6 +/- 0.5 N m g(-1) and delamination strength from 217 +/- 19 kPa to 295 +/- 30 kPa.

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Trabalho Final de Mestrado para obtenção do grau de Mestre em Engenharia Mecânica

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Captopril, an inhibitor of angiotensin converting enzyme, was administered twice daily to 13 hypertensive patients for a mean period of 9 weeks. Continuous blood pressure control in the ambulatory patients was established with a portable blood pressure recorder. Notwithstanding, in eight patients with normal renal function, plasma converting enzyme was found to resume normal activity before administration of the morning dose of captopril. Only in 5 patients with impaired renal function did some blockade of plasma converting enzyme persist for more than 12 hours. Measured plasma converting enzyme activity seemed to reflect total conversion of angiotensin I, including conversion in the pulmonary vascular bed, since changes in its activity were closely paralled by changes in plasma aldosterone levels. Bradykinin accumulation seems unlikely when converting enzyme and thus, presumably, kininase II has resumed normal activity. Captopril administration does not seem to alter plasma epinephrine or norepinephrine levels. Blood pressure reduction in the face of normal angiotensin converting enzyme activity is probably due to hyporesponsiveness of the arterioles to pressor hormones, which may be due to specific renin-related and/or nonspecific effects of captopril.

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Painelajittimet ovat yleisimpiä hiokkeen lajitteluun käytettyjä lajittimia. Painelajittimien suorituskyky on parantunut viimeisten vuosikymmenien aikana niin paljon, että pyörrepuhdistuksesta on pääosin voitu luopua osana hiokkeen lajittelua. Painelajittimen erinomaisuus perustuu siihen, että sillä voidaan erottaa massasta hyvinkin erilaisia epäpuhtauksia. Nykyään vallitsevia painelajittelun trendejä ovat sakeuden nosto, energiankulutuksen vähentäminen sekä eri fraktioiden erottumisen tehostuminen. Kaikilla pyritään vähentämään vedenkäyttöä ja parantamaan massan ominaisuuksia jatkoprosesseja silmälläpitäen. Tässä työssä tarkasteltiin painelajittimen roottorin kierrosnopeuden vaikutusta akseptimassan laatuun. Luodaan malli freeness-pudotukselle lajittimen yli. Sekä tarkastellaan myös automaatioon pohjautuvan säädön käyttöönottoa lajittimen akseptimassan freenesvaihteluiden tasaamiseksi. Toisaalta tehdään myös suppea selvitys lajittimien energiankulutuksista erilaisilla roottorin pyörimisnopeuksilla. Tuotantokäytössä oleviin lajittimiin asennettujen invertterisäätöjen ja koepisteistä saatujen tulosten avulla voidaan todeta, että laskemalla roottorin pyörimisnopeutta voidaan lajittimessa tapahtuvaa freenespudotusta kasvattaa. Samalla saavutetaan hyötyjä myös muissa massan ominaisuuksissa, kuten vetolujuudessa. Automaattisäädön käyttöönotolla saavutetaan huomattavasti pienempi hajonta akseptimassan freeneksessä. Rejektilinjan lajittimissa hajonta lähes puolittui ja päälinjan lajittimissa päästiin noin kolmanneksen parannukseen. Energian kulutuksia tutkittaessa huomataan, että roottorin kierrosnopeutta alentamalla voidaan merkittävästi vähentää lajittimien energian kulutusta. Parhaassa tapauksessa voidaan säästää neljännes lajittelun energiakustannuksissa.

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

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

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Background and Objectives - It is essential to reduce health care costs without impairing the quality of care. Propofol is associated to faster recovery and it is known that post-anesthesia care unit (PACU) costs are high. The aim of this study was to evaluate the advantages of two anesthesia regimens - propofol continuous infusion or isoflurane - taking into account the cost of both techniques on PACU stay. Methods - Forty seven patients, physical status ASA I, II and III, undergoing laparoscopic cholecystectomy were divided into 2 groups according to the anesthetic agent: G1, conventional propofol continuous infusion (100-150 μg.kg-1.min-1) and G2, isoflurane. All patients were induced with sufentanil (1 μg.kg-1) and propofol (2 mg.kg-1) and were kept in a re-inhalation circuit (2 L.min-1 of fresh gas flow) with 50% N2O in O2, sufentanil (0.01 μg.kg-1.min-1) and atracurium (0.5 mg.kg-1), or pancuronium (0.1 mg.kg-1) for asthma patients. All patients received atropine and neostigmine at the end of the surgery. Prophylactic ondansetron, dipyrone and tenoxican were administered and, when necessary, tramadol and N-butylscopolamine. Costs of anesthetic drugs (COST), total PACU stay (t-PACU), and PACU stay after extubation (t-EXT) were computed for both groups. Results - Costs were significantly lower in the isoflurane group but t-PACU was 26 minutes longer and t-EXT G1continuous infusion group.