Rotor retaining sleeve design for a 1.12-MW high-speed PM machine

Permanent-magnet (PM) synchronous machines (PMSMs) can provide excellent performance in terms of torque density, energy efficiency, and controllability. However, PMs on the rotor are prone to centrifugal force, which may break their physical integrity, particularly at high-speed operation. Typically, PMs are bound with carbon fiber or retained by alloy sleeves on the rotor surface. This paper is concerned with the design of a rotor retaining sleeve for a 1.12-MW 18-kr/min PM machine; its electromagnetic performance is investigated by the 2-D finite-element method (FEM). Theoretical and numerical analyses of the rotor stress are carried out. For the carbon fiber protective measure, the stresses of three PM configurations and three pole filler materials are compared in terms of operating temperature, rotor speed, retaining sleeve thickness, and interference fit. Then, a new hybrid protective measure is proposed and analyzed by the 2-D FEM for operational speeds up to 22 kr/min (1.2 times the rated speed). The rotor losses and machine temperatures with the carbon fiber retaining sleeve and the hybrid retaining sleeve are compared, and the sleeve design is refined. Two rotors using both designs are prototyped and experimentally tested to validate the effectiveness of the developed techniques for PM machines. The developed retaining sleeve makes it possible to operate megawatt PM machines at high speeds of 22 kr/min. This opens doors for many high-power high-speed applications such as turbo-generator, aerospace, and submarine motor drives.

A Sensorless PMDC Motor Speed Controller with a Logical Overcurrent Protection

A method to control the speed or the torque of a permanent-magnet direct current motor is presented. The rotor speed and the external torque estimation are simultaneously provided by appropriate observers. The sensorless control scheme is based on current measurement and switching states of power devices. The observer’s performances are dependent on the accurate machine parameters knowledge. Sliding mode control approach was adopted for drive control, providing the suitable switching states to the chopper power devices. Despite the predictable chattering, a convenient first order switching function was considered enough to define the sliding surface and to correspond with the desired control specifications and drive performance. The experimental implementation was supported on a single dsPIC and the controller includes a logic overcurrent protection.

Crowbar System in Doubly Fed Induction Wind Generators

In the last 15 years, the use of doubly fed induction machines in modern variable-speed wind turbines has increased rapidly. This development has been driven by the cost reduction as well as the low-loss generation of Insulated Gate Bipolar Transistors (IGBT). According to new grid code requirements, wind turbines must remain connected to the grid during grid disturbances. Moreover, they must also contribute to voltage support during and after grid faults. The crowbar system is essential to avoid the disconnection of the doubly fed induction wind generators from the network during faults. The insertion of the crowbar in the rotor circuits for a short period of time enables a more efficient terminal voltage control. As a general rule, the activation and the deactivation of the crowbar system is based only on the DC-link voltage level of the back-to-back converters. In this context, the authors discuss the critical rotor speed to analyze the instability of doubly fed induction generators during grid faults.

Effect of impeller type and mechanical agitation on the mass transfer and power consumption aspects of ASBR operation treating synthetic wastewater

The effect of flow type and rotor speed was investigated in a round-bottom reactor with 5 L useful volume containing 2.0 L of granular biomass. The reactor treated 2.0 L of synthetic wastewater with a concentration of 800 mgCOD/L in 8-h cycles at 30 degrees C. Five impellers, commonly used in biological processes, have been employed to this end, namely: a turbine and a paddle impeller with six-vertical-flat-blades, a turbine and a paddle impeller with six-45 degrees-inclined-flat-blades and a three-blade-helix impeller. Results showed that altering impeller type and rotor speed did not significantly affect system stability and performance. Average organic matter removal efficiency was about 84% for filtered samples, total volatile acids concentration was below 20 mgHAc/L and bicarbonate alkalinity a little less than 400 mgCaCO(3)/L for most of the investigated conditions. However, analysis of the first-order kinetic model constants showed that alteration in rotor speed resulted in an increase in the values of the kinetic constants (for instance, from 0.57 h(-1) at 50 rpm to 0.84 h(-1) at 75 rpm when the paddle impeller with six-45 degrees-inclined-flat-blades was used) and that axial flow in mechanically stirred reactors is preferable over radial-flow when the vertical-flat-blade impeller is compared to the inclined-flat-blade impeller (for instance at 75 rpm, from 0.52 h(-1) with the six-flat-blade-paddle impeller to 0.84 h(-1) with the six-45 degrees-inclined-flat-blade-paddle impeller), demonstrating that there is a rotor speed and an impeller type that maximize solid-liquid mass transfer in the reaction medium. Furthermore, power consumption studies in this reduced reactor volume showed that no high power transfer is required to improve mass transfer (less than 0.6 kW/10(3) m(3)). (C) 2008 Elsevier Ltd. All rights reserved.

Avaliação do potencial eólico para geração de energia eléctrica

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

Study and modeling of the desintegration kinetics of coated paper

The disintegration of recovered paper is the first operation in the preparation of recycled pulp. It is known that the defibering process follows a first order kinetics from which it is possible to obtain the disintegration kinetic constant (KD) by means of different ways. The disintegration constant can be obtained from the Somerville index results (%lsv and from the dissipated energy per volume unit (Ss). The %slv is related to the quantity of non-defibrated paper, as a measure of the non-disintegrated fiber residual (percentage of flakes), which is expressed in disintegration time units. In this work, disintegration kinetics from recycled coated paper has been evaluated, working at 20 revise rotor speed and for different fiber consistency (6, 8, 10, 12 and 14%). The results showed that the values of experimental disintegration kinetic constant, Ko, through the analysis of Somerville index, as function of time. Increased, the disintegration time was drastically reduced. The calculation of the disintegration kinetic constant (modelled Ko), extracted from the Rayleigh’s dissipation function, showed a good correlation with the experimental values using the evolution of the Somerville index or with the dissipated energy

Study and modeling of the desintegration kinetics of coated paper

The disintegration of recovered paper is the first operation in the preparation of recycled pulp. It is known that the defibering process follows a first order kinetics from which it is possible to obtain the disintegration kinetic constant (KD) by means of different ways. The disintegration constant can be obtained from the Somerville index results (%lsv and from the dissipated energy per volume unit (Ss). The %slv is related to the quantity of non-defibrated paper, as a measure of the non-disintegrated fiber residual (percentage of flakes), which is expressed in disintegration time units. In this work, disintegration kinetics from recycled coated paper has been evaluated, working at 20 revise rotor speed and for different fiber consistency (6, 8, 10, 12 and 14%). The results showed that the values of experimental disintegration kinetic constant, Ko, through the analysis of Somerville index, as function of time. Increased, the disintegration time was drastically reduced. The calculation of the disintegration kinetic constant (modelled Ko), extracted from the Rayleigh’s dissipation function, showed a good correlation with the experimental values using the evolution of the Somerville index or with the dissipated energy

Study and modeling of the desintegration kinetics of coated paper

The disintegration of recovered paper is the first operation in the preparation of recycled pulp. It is known that the defibering process follows a first order kinetics from which it is possible to obtain the disintegration kinetic constant (KD) by means of different ways. The disintegration constant can be obtained from the Somerville index results (%lsv and from the dissipated energy per volume unit (Ss). The %slv is related to the quantity of non-defibrated paper, as a measure of the non-disintegrated fiber residual (percentage of flakes), which is expressed in disintegration time units. In this work, disintegration kinetics from recycled coated paper has been evaluated, working at 20 revise rotor speed and for different fiber consistency (6, 8, 10, 12 and 14%). The results showed that the values of experimental disintegration kinetic constant, Ko, through the analysis of Somerville index, as function of time. Increased, the disintegration time was drastically reduced. The calculation of the disintegration kinetic constant (modelled Ko), extracted from the Rayleigh’s dissipation function, showed a good correlation with the experimental values using the evolution of the Somerville index or with the dissipated energy

Lajittelun laadun hallinta

Tässä diplomityössä tarkastellaan kuumahierteen lajittimien akseptimassan laadun hallintaan vaikuttavia tekijöitä. Tarkastelussa keskitytään pääasiassa roottorin pyörintänopeuden ja syöttösakeuden vaikutukseen lajittimien lajittelutuloksiin. Lisäksi työssä tarkastellaan lajittimen roottorin pyörintänopeuden muuttamiseen perustuvaa akseptimassan freeness-säädön toimintaa ja sen käyttökelpoisuutta akseptimassan freeness-tason hallitsemiseksi. Tulosten perusteella painelajittimien roottorin pyörintänopeudella on vaikutusta aksepti- ja rejektimassan laatuominaisuuksiin. Roottorin pyörintänopeuden muuttamiseen perustuva akseptimassan freeness-tason säätö on periaatteeltaan toimiva. Säätö toimii parhaiten tilanteissa, joissa lajittimen syöttömassan freeness nousee. Tarkastelujakson aikana roottorin pyörintänopeussäätö oli uusi, lisäksi lajittelussa tehtiin muutakin säätökehitystä, joten se miten paljon säädöstä on hyötyä freeness-huojunnan tasaajana, jäi selvittämättä. Työssä osoitettiin myös se, että syöttösakeudella voidaan vaikuttaa akseptimassan freeness-tasoon. Vaikutus ei ole kuitenkaan yhtä selkeä kuin roottorin pyörintänopeussäädön.

Study and modeling of the desintegration kinetics of coated paper

The disintegration of recovered paper is the first operation in the preparation of recycled pulp. It is known that the defibering process follows a first order kinetics from which it is possible to obtain the disintegration kinetic constant (KD) by means of different ways. The disintegration constant can be obtained from the Somerville index results (%lsv and from the dissipated energy per volume unit (Ss). The %slv is related to the quantity of non-defibrated paper, as a measure of the non-disintegrated fiber residual (percentage of flakes), which is expressed in disintegration time units. In this work, disintegration kinetics from recycled coated paper has been evaluated, working at 20 revise rotor speed and for different fiber consistency (6, 8, 10, 12 and 14%). The results showed that the values of experimental disintegration kinetic constant, Ko, through the analysis of Somerville index, as function of time. Increased, the disintegration time was drastically reduced. The calculation of the disintegration kinetic constant (modelled Ko), extracted from the Rayleigh’s dissipation function, showed a good correlation with the experimental values using the evolution of the Somerville index or with the dissipated energy

Fraktioinnin tehostaminen lajittelussa

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.

Estudo da estabilidade a pequenas perturbações do sistema elétrico de potência sob a ação do dispositivo FACTS PHASE SHIFTER - PS

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

Técnica de projeto de controlador fuzzy aplicada ao acionamento vetorial de motor de indução

Este trabalho investiga uma estratégia de controle fuzzy Takagi-Sugeno aplicada ao controle de velocidade do motor de indução. A estratégia implementa uma interpolação ponderada entre um conjunto de controladores locais previamente projetados. Ao ocorrer variações nas condições operacionais do motor de indução, os ganhos da lei de controle são ajustados automaticamente, de modo a manter satisfatório o desempenho do sistema de controle. Para o projeto do controlador fuzzy a representação em espaço de estados da planta foi considerada sob a forma de um sistema aumentado, incluindo-se uma nova variável de estado que, nesse caso, foi selecionada como sendo a integral do erro de velocidade. Tal formulação permitiu o projeto de controladores locais com a estrutura PI, através de realimentação completa de estados, com posicionamento de pólos. Como variáveis de operação para o chaveamento fuzzy dos controladores locais, foram selecionados as variáveis velocidade angular do rotor e a componente da corrente de estator responsável pelo torque elétrico do motor. Em seguida, a estabilidade do controlador fuzzy Takagi- Sugeno projetado foi comprovada através do critério de Lyapunov, para isso o problema de estabilidade foi escrito na forma de LMIs. O desempenho do controlador fuzzy Takagi-Sugeno foi avaliado através de estudos de simulação, e seus resultados comparados ao desempenho de um controlador PI convencional, para a regulação da velocidade do rotor. Os resultados obtidos nas simulações mostram que o emprego da estratégia proposta torna o sistema mais robusto a variações paramétricas no sistema de acionamento.

Enteric coated mucoadhesive micropellets in rotary agglomeration process for wet spheronization

In this work a generally applicable method for the preparation of mucoadhesive micropellets of 250 to 600µm diameter is presented using rotor processing without the use of electrolytes. The mucoadhesive micropellets were developed to combine the advantages of mucoadhesion and microparticles. It was possible to produce mucoadhesive micropellets based on different mucoadhesive polymers Na-CMC, Na-alginate and chitosan. These micropellets are characterized by a lower friability (6 to 17%) when compared to industrial produced cellulose pellets (Cellets®) (41.5%). They show great tapped density and can be manufactured at high yields. The most influencing variables of the process are the water content at the of the end spraying period, determined by the liquid binder amount, the spraying rate, the inlet air temperature, the airflow and the humidity of the inlet air and the addition of the liquid binder, determined by the spraying rate, the rotor speed and the type of rotor disc. In a subsequent step a fluidized bed coating process was developed. It was possible to manifest a stable process in the Hüttlin Mycrolab® in contrast to the Mini-Glatt® apparatus. To reach enteric resistance, a 70% coating for Na-CMC micropellets, an 85% for chitosan micropellets and a 140% for Na-alginate micropellets, based on the amount of the starting micropellets, was necessary. Comparative dissolution experiments of the mucoadhesive micropellets were performed using the paddle apparatus with and without a sieve inlay, the basket apparatus, the reciprocating cylinder and flow-through cell. The paddle apparatus and the modified flow-through cell method turned out to be successful methods for the dissolution of mucoadhesive micropellets. All dissolution profiles showed an initial burst release followed by a slow release due to diffusion control. Depending on the method, the dissolution profiles changed from immediate release to slow release. The dissolution rate in the paddle apparatus was mainly influenced by the agitation rate whereas the flow-through cell pattern was mainly influenced by the particle size. Also, the logP and the HLB values of different emulsifiers were correlated to transfer HLB values of excipients into logP values and logP values of API´s into HLB values. These experiments did not show promising results. Finally, it was shown that manufacture of mucoadhesive micropellets is successful resulting in product being characterized by enteric resistency combined with high yields and convincing morphology.

Tratamento de soro de queijo no ASBR: influência da estratégia de alimentação

Avaliou-se o desempenho do reator anaeróbio em batelada seqüencial com biomassa imobilizada (ASBBR) no tratamento de soro de queijo quanto submetido a diferentes estratégias de alimentação e cargas orgânicas volumétricas (COV). O reator operou com agitação mecânica através de impelidor do tipo hélice na rotação de 500 rpm. Um volume de 2 litros foi alimentado por ciclo com 1 litro de volume residual, totalizando 3 litros. O substrato utilizado foi soro de queijo desidratado reconstituído. Suplementou-se o sistema com NaHCO3 na razão de 50% NaHCO3/DQO. Foram testadas as seguintes COVs: 2, 4, 8 e 12 gDQO/l.d. Para ciclos de 8 horas e em cada COV, três estratégias de alimentação foram testadas: (a) operação em batelada com ciclo de 8 horas, (b) batelada alimentada de 2 horas (c) batelada alimentada de 4 horas. Na COV de 2 gDQO/l.d, a conversão de matéria orgânica como DQO em amostras filtradas foi de 92, 96 e 91% para as estratégias de alimentação (a), (b) e (c), respectivamente. Para a COV de 4 gDQO/l.d, o desempenho foi de 94, 97 e 93%, respectivamente. Para a COV de 8 gDQO/l.d houve redução nas eficiências de conversão a 83, 85 e 86%, respectivamente. O aumento da COV para 12 gDQO/l.d, resultou na redução em eficiências de 72, 73 e 81%, respectivamente. Os perfis durante os ciclos da concentração de ácidos voláteis totais mostraram que, apesar do aumento gradual com o tempo de enchimento aumentando, nenhuma diferença significativa foi detectada em termos dos seus valores máximos. Foi observada a redução de ácido propiônico como conseqüência do aumento do tempo de enchimento. Assim, para COV de 2 e 4 gDQO/l.d, a estratégia de alimentação (b) proporcionou maiores eficiências de conversão e estabilidade operacional, enquanto que este comportamento foi observado na estratégia de alimentação (c) para os valores de COV de 8 e 12 gDQO/l.d.