979 resultados para equipment sizing
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Työn tavoitteena oli määritellä kirjallisuustutkimuksen ja suunnitteluesimerkin avulla vaatimuksia integroidulle simulointiympäristölle, joka sisältää simulointiohjelmien lisäksi prosessilaitteiden mitoitusohjelmia ja prosessilaite- ja mallitietokannan. Lisäksi pohdittiin simulointiympäristön tuomia etuja prosessissuunnitteluun. Esimerkkinä käytettiin yksinkertaista putkilinjaa. Ensin selvitettiin prosessisuunnittelun kulkua, menetelmiä, apuvälineitä ja ajankohtaisia teemoja kirjallisuuden perusteella. Prosessisuunnittelun menetelmistä keskityttiin yksityiskohtaisemmin prosessisimulointiin. Lisäksi etsittiin kirjallisuudesta esimerkkejä integroiduista suunnitteluympäristöistä. Kirjallisuusselvityksen perusteella määriteltiin yleisiä vaatimuksia integroidulle simulointiympäristölle. Seuraavaksi suunniteltiin esimerkkinä käytetty putkilinja ja kuvattiin suunnittelun eteneminen. Suunnitteluesimerkin avulla pyrittiin tunnistamaan suunnitteluprosessista ne kohdat, joissa integroitu simulointiympäristö helpottaisi työskentelyä sekä pohtimaan yksityiskohtaisemmin integroidun simulointiympäristön toimintoja. Lopuksi kuvattiin putkilinjan suunnittelun eteneminen integroidussa simulointiympäristössä ja pohdittiin sen etuja verrattuna perinteiseen putkilinjan suunnitteluun. Tutkimuksen perusteella integroitu simulointiympäristö tehostaa prosessisuunnittelua siten, että simulointimallien määrittelyissä tarvittavat laitetiedot ovat saatavissa helposti ja nopeasti ohjelmien ymmärtämässä muodossa. Simulointiympäristössä tieto eri sovellusten välillä siirtyy osittain automaattisesti, minkä takia ohjelmiin ei erikseen tarvitse syöttää samoja tietoja. Lisäksi integroitu simulointiympäristö tukee rinnakkaista suunnittelua ja automaatio- ja prosessisuunnittelun integrointia.Jatkotutkimusehdotuksena on lisäselvitykset siitä, miten simulointiympäristö sijoittuisi yrityksissä jo olemassa oleviin suunnittelujärjestelmiin, etenkin tiedonhallintajärjestelmiin nähden. Muina jatkotutkimusehdotuksina on integroidun simulointiympäristön tarkasteleminen automaatiosuunnittelijan kannalta sekä vaatimusmäärittelyjen tarkentaminen. Työssä ei juuri ole kiinnitetty huomiota siihen, kuinka helposti ehdotetut simulointiympäristön toiminnot ja vaatimukset ovat toteutettavissa teknisesti tai ylipäätään ovatko toteutettavissa, joten tämäkin vaatinee jatkotutkimuksia.
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Today the limitedness of fossil fuel resources is clearly realized. For this reason there is a strong focus throughout the world on shifting from fossil fuel based energy system to biofuel based energy system. In this respect Finland with its proven excellent forestry capabilities has a great potential to accomplish this goal. It is regarded that one of the most efficient ways of wood biomass utilization is to use it as a feedstock for fast pyrolysis process. By means of this process solid biomass is converted into liquid fuel called bio-oil which can be burnt at power plants, used for hydrogen generation through a catalytic steam reforming process and as a source of valuable chemical compounds. Nowadays different configurations of this process have found their applications in several pilot plants worldwide. However the circulating fluidized bed configuration is regarded as the one with the highest potential to be commercialized. In the current Master’s Thesis a feasibility study of circulating fluidized bed fast pyrolysis process utilizing Scots pine logs as a raw material was conducted. The production capacity of the process is 100 000 tonne/year of bio-oil. The feasibility study is divided into two phases: a process design phase and economic feasibility analysis phase. The process design phase consists of mass and heat balance calculations, equipment sizing, estimation of pressure drops in the pipelines and development of plant layout. This phase resulted in creation of process flow diagrams, equipment list and Microsoft Excel spreadsheet that calculates the process mass and heat balances depending on the bio-oil production capacity which can be set by a user. These documents are presented in the current report as appendices. In the economic feasibility analysis phase there were at first calculated investment and operating costs of the process. Then using these costs there was calculated the price of bio-oil which is required to reach the values of internal rate of return of 5%, 10%, 20%, 30%, 40%, and 50%.
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Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)
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Sugarcane has a significant role on Brazilian agribusiness economy. The harvesting cane is considered as one of the most important operations of the process for it has to attend the raw material demanded by the sugar mill in quality and a competitive cost. The objective of this work it is it of analyzing, of systemic way, the variables influence on economical and operational performance in sugarcane mechanized harvesting process for sizing of machines. For this purpose a model called "ColheCana", was developed in a spreadsheet and in a programming language. The results showed that the field efficiency and harvester´s initial value are variables of great impact in the cost and that there is a maximum area that one equipment can attend and for this area the cost is minimum.
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Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)
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This paper addresses the capacitated lot sizing problem (CLSP) with a single stage composed of multiple plants, items and periods with setup carry-over among the periods. The CLSP is well studied and many heuristics have been proposed to solve it. Nevertheless, few researches explored the multi-plant capacitated lot sizing problem (MPCLSP), which means that few solution methods were proposed to solve it. Furthermore, to our knowledge, no study of the MPCLSP with setup carry-over was found in the literature. This paper presents a mathematical model and a GRASP (Greedy Randomized Adaptive Search Procedure) with path relinking to the MPCLSP with setup carry-over. This solution method is an extension and adaptation of a previously adopted methodology without the setup carry-over. Computational tests showed that the improvement of the setup carry-over is significant in terms of the solution value with a low increase in computational time.
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This study presents a decision-making method for maintenance policy selection of power plants equipment. The method is based on risk analysis concepts. The method first step consists in identifying critical equipment both for power plant operational performance and availability based on risk concepts. The second step involves the proposal of a potential maintenance policy that could be applied to critical equipment in order to increase its availability. The costs associated with each potential maintenance policy must be estimated, including the maintenance costs and the cost of failure that measures the critical equipment failure consequences for the power plant operation. Once the failure probabilities and the costs of failures are estimated, a decision-making procedure is applied to select the best maintenance policy. The decision criterion is to minimize the equipment cost of failure, considering the costs and likelihood of occurrence of failure scenarios. The method is applied to the analysis of a lubrication oil system used in gas turbines journal bearings. The turbine has more than 150 MW nominal output, installed in an open cycle thermoelectric power plant. A design modification with the installation of a redundant oil pump is proposed for lubricating oil system availability improvement. (C) 2009 Elsevier Ltd. All rights reserved.
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Development and Characterization of L-Alanyl-L-Glutamine Containing Pellets employing Extrusion-Spheronization Method and Drying Process in Fluidized Bad Equipment"". In this work, five formulations of L-alanyl-L-glutamine (glutamine dipeptide) containing pellets with different drug concentration were developed and evaluated: F1 (9.07%); F2 (17.70%); F3 (27.98%); F4 (37.74%) e F5 (47.53%). Pellets were prepared by extrusion-spheronization method and, further, dried in fluidized bad equipment. The following assays were carried out with the batches obtained: granulometry, friability, true density and morphologic analysis. Between the five formulations evaluated, pellets obtained from F3 present best yield (75.80%), most uniform particle size distribution (89.67% of pellets with size in the range of 0.80 to 1.18), most high true density (2.1634 g/ml) and best aspect (1.0795 +/- 0.0410). Due to these features, pellets obtained from F3 were considered adequate to further polymeric coating process in order to produce a multiparticulate system to prolong L-alanyl-L-glutamine release.
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A tandem ionization chamber was developed for quality control programs of X-ray equipment used in conventional radiography and mammography. A methodology for the use of the tandem chamber in the constancy check of diagnostic X-ray beam qualities was established. The application at a medical X-ray imaging facility of this established methodology is presented. The use of the tandem chamber in the constancy check of diagnostic X-ray beam qualities is a useful method to control the performance of the X-ray equipment. (c) 2008 Elsevier Ltd. All rights reserved.
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A technique based on laser light diffraction is shown to be successful in collecting on-line experimental data. Time series of floc size distributions (FSD) under different shear rates (G) and calcium additions were collected. The steady state mass mean diameter decreased with increasing shear rate G and increased when calcium additions exceeded 8 mg/l. A so-called population balance model (PBM) was used to describe the experimental data, This kind of model describes both aggregation and breakage through birth and death terms. A discretised PBM was used since analytical solutions of the integro-partial differential equations are non-existing. Despite the complexity of the model, only 2 parameters need to be estimated: the aggregation rate and the breakage rate. The model seems, however, to lack flexibility. Also, the description of the floc size distribution (FSD) in time is not accurate.
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The concept of a basic (i.e., essential) medical emergency kit suitable for a general dental practitioner varies somewhat between different authorities. A practitioner's choice is also dependant on the proximity of medical aid and the nature of the dental practice. Over recent years the trend has been to restrict the items to a minimum, in the interest of both common sense and safety, for example, just oxygen, adrenaline 1:1000, an oral carbohydrate source, glyceryl trinitrate and aspirin as first options. Ancillary equipment should include an oxygen therapy facemask, a pocket mask and a set of oral (Guedel) airways. Two further medication options for consideration are an aerosol bronchodilator and, in certain circumstances, an injectable antihypoglycaemic agent. This paper provides a selective overview of the subject. An absolute necessity is for dentists to be competent in Basic Life Support skills, and to maintain a complete and current medical history for all patients.
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Pretende-se com este trabalho de Projecto de Mestrado conceber uma câmara frigorífica de 20000 m3 para armazenar produtos congelados e estudar um sistema frigorífico com dois fluidos frigorigénios que serão o CO2 (R-744) e o NH3 (R-717) O trabalho inicia-se com a definição dos objectivos principais para o projecto de um sistema frigorífico deste tipo. Após a definição dos objectivos, o projecto propõe um estudo termodinâmico do CO2 (R-744) como fluido frigorigénio, definindo se o seu historial de utilização, características principais, diagrama pressão-entalpia com a distinção das diversas fases do fluído, comparação em diversos parâmetros com outros fluidos, o porquê da utilização deste fluído, problemas comuns em sistemas com a presença deste fluído, entre outros parâmetros de estudo. De seguida será feito o dimensionamento de uma câmara frigorífica de 20000 m3 para armazenar produtos congelados paletizados através de um balanço térmico manual e um balanço térmico informático através do programa da Centauro comparando no final o resultado dos dois métodos. Será feito uma descrição das características básicas da câmara frigorífica com um esquema simples do edifício. Será abordado de seguida o sistema frigorífico a CO2 (R-744) e a NH3 (R-717) nas suas diversas características, nomeadamente no cálculo de caudais, diagrama pressão-entalpia, dimensionamento de tubagens e finalmente selecção de equipamento. Procede-se assim também ao estudo um sistema apenas a NH3 (R-717) com as suas diversas características nomeadamente no cálculo de caudais, diagrama pressão-entalpia, dimensionamento de tubagens e finalmente selecção dos equipamentos mais importantes, para que desta forma se proceda à comparação dos dois sistemas a nível energético, consumo eléctrico e manutenção de equipamentos. Finalmente proceder-se-á interpretação de resultados com o objectivo final de escolher a melhor solução nos vários parâmetros de comparação, para o esquema em questão.
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This paper proposes a computationally efficient methodology for the optimal location and sizing of static and switched shunt capacitors in large distribution systems. The problem is formulated as the maximization of the savings produced by the reduction in energy losses and the avoided costs due to investment deferral in the expansion of the network. The proposed method selects the nodes to be compensated, as well as the optimal capacitor ratings and their operational characteristics, i.e. fixed or switched. After an appropriate linearization, the optimization problem was formulated as a large-scale mixed-integer linear problem, suitable for being solved by means of a widespread commercial package. Results of the proposed optimizing method are compared with another recent methodology reported in the literature using two test cases: a 15-bus and a 33-bus distribution network. For the both cases tested, the proposed methodology delivers better solutions indicated by higher loss savings, which are achieved with lower amounts of capacitive compensation. The proposed method has also been applied for compensating to an actual large distribution network served by AES-Venezuela in the metropolitan area of Caracas. A convergence time of about 4 seconds after 22298 iterations demonstrates the ability of the proposed methodology for efficiently handling large-scale compensation problems.