17 results on '"Andre, Furtado"'
Search Results
2. Seismic Sequence Vulnerability of Low-Rise Special Moment-Resisting Frame Buildings with Brick Infills
- Author
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Pushpa Mahat, Piyush Pradhan, Rabindra Adhikari, Andre Furtado, Dipendra Gautam, and Rajesh Rupakhety
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seismic vulnerability ,fragility function ,foreshock–mainshock–aftershock sequence ,low-rise RC ,brick infill ,Technology ,Engineering (General). Civil engineering (General) ,TA1-2040 ,Biology (General) ,QH301-705.5 ,Physics ,QC1-999 ,Chemistry ,QD1-999 - Abstract
When buildings are exposed to earthquake sequence, damage aggravation is expected to occur. Although several studies report seismic vulnerability of reinforced concrete (RC) buildings under the mainshock–aftershock sequence, indicating damage aggravation due to aftershock, none, to the best of our knowledge, quantifies seismic vulnerability of buildings under foreshock–mainshock–aftershock sequences. Since foreshock–mainshock–aftershock sequences are also expected in many active seismic regions, we aim to quantify the level of vulnerability under seismic sequences considering the seismically highly active Himalayan region as the case study location. Fragility functions are derived considering foreshock, foreshock–mainshock sequence, and foreshock–mainshock–aftershock sequence for a low-rise special moment-resisting frame (SMRF) building that represents a typical low-rise owner-built construction system in Nepal, one of the most active seismic regions in the world. The results highlight that the foreshock significantly increases seismic vulnerability of the structures with respect to the often-considered case of a mainshock–aftershock sequence.
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- 2022
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3. Methanol Production from Biomass Gasification: Techno-economic Assessment of Different Feedstocks
- Author
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Andre Furtado Amaral, Daniele Previtali, Anna Dell'Angelo, Filippo Bisotti, Alessandro Di Pretoro, Ecem Muge Andoglu, Simone Colombo, and Flavio Manenti
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Chemical engineering ,TP155-156 ,Computer engineering. Computer hardware ,TK7885-7895 - Abstract
This work presents an updated techno-economic assessment of methanol production, considering an entrained flow gasifier with different second generation biomasses. Computer simulations were performed with the aid of a gasification simulator GasDS and with commercial process simulator Aspen HYSYS. A method was proposed to determine biomass composition in terms of cellulose, hemicellulose and three surrogate compounds that account for the most abundant monomers that compose lignin chains; the lower heat value (LHV) relative error was not bigger than 10%. The kinetic model deriving from this biomass characterization (composition) is not sufficiently accurate to describe biomass gasification; this is due to unrealistically small residence times and the (not modelled) catalytic effect of molten slag. Biomass gasification output is efficiently estimated by using chemical equilibrium. At current methanol market price (350 €/t) the process is economically unfeasible at the current plant capacity of 100 MW LHV biomass input (production costs vary between 360 and 440 €/t).
- Published
- 2019
- Full Text
- View/download PDF
4. Smart Implementation of Bender Equation of State
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Filippo Bisotti, Alessandro Di Pretoro, Anna Dell'Angelo, Daniele Previtali, Andre Furtado Amaral, Ecem Muge Andoglu, and Flavio Manenti
- Subjects
Chemical engineering ,TP155-156 ,Computer engineering. Computer hardware ,TK7885-7895 - Abstract
In this paper matrix and vector products are exploited to reformulate Bender Equation of State. Finally, the new formulation is used to generate results which has been compared with experimental data sets available in literature and the analogous findings coming from different thermodynamic packages commonly used in Aspen Hysys for Air Separation Unit.
- Published
- 2019
- Full Text
- View/download PDF
5. The mutagenic, DNA-damaging and antioxidative properties of bark and leaf extracts from Coutarea hexandra (Jacq.) K. Schum
- Author
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Nunes, Líria Granato, Gontijo, Douglas Costa, Souza, Carlos J.A., Fietto, Luciano Gomes, Carvalho, André Furtado, and Leite, João Paulo Viana
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- 2012
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6. Modeling and Simulation of an Industrial Top-Fired Methane Steam Reforming Unit
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Flavio Manenti, Francesco Rossi, Poliana P. S. Quirino, Andre Furtado Amaral, and Karen Valverde Pontes
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business.industry ,General Chemical Engineering ,02 engineering and technology ,General Chemistry ,021001 nanoscience & nanotechnology ,Combustion ,Industrial and Manufacturing Engineering ,Unit (housing) ,Modeling and simulation ,Steam reforming ,020401 chemical engineering ,Work (electrical) ,Phenomenological model ,Environmental science ,0204 chemical engineering ,0210 nano-technology ,Process engineering ,business - Abstract
This work aims to develop a stationary phenomenological model of an industrial steam reforming unit. Unlike the usual approach in literature, the combustion reactions at the furnace are described t...
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- 2020
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7. Turning curse into cure: Potential of water hyacinth for bio-refining - A contextual investigation of Lake Tana
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Derese Tekestebrihan Nega, A. Venkata Ramayya, Andre Furtado Amaral, and Flavio Manenti
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Global and Planetary Change ,Curse ,Environmental Engineering ,biology ,Waste management ,Hyacinth ,Bioethanol ,Management, Monitoring, Policy and Law ,biology.organism_classification ,Pollution ,Biorefinery ,Environmental sciences ,Bio-fertilizer ,Refining ,Water hyacinth ,Environmental science ,GE1-350 ,Waste Management and Disposal ,Biomethane ,Techno-economic analysis - Abstract
Water hyacinth (WH, Eichhornia crassipes, ’Emboch’ in Ethiopia) is a highly disturbing class of invasive and noxious aquatic plants found worldwide in other water bodies and as such is a prime problem in Lake Tana. One approach to successfully control the rapid invasion of WH is to utilize it as a feedstock to produce high-valued commodities in a biorefinery framework. Preliminary life cycle analysis carried out in the study shows that WH biomass is a competitive feedstock for biorefinery systems with a unit cost at $ 24.40 per ton of dry matter. Based on the annual generation capacity of 0.71 million tons of dry mass in lake Tana and following the standard biorefinery process protocols, the predictions indicate that the economic potential of converting WH biomass into 38.8 billion liters of biomethane alone to be at $ 38.8 million, 74.2 million liters of bioethanol alone at $ 51.9 million, and o.52 million tons organic agro-fertilizer alone at $ 130.5/78.3 million as a partial substitute for Anhydrous Ammonia or Muriate of Potash (MOP) fertilizers. Hence the integrated WH management and utilization as a biorefinery feedstock ranks it among the world’s most competitive feedstocks with attractive socio-economic and environmental benefits.
- Published
- 2021
8. Impact of kinetic models in the prediction accuracy of an industrial steam methane reforming unit
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Karen Valverde Pontes, Flavio Manenti, Andre Furtado Amaral, Francesco Rossi, and P. P. S. Quirino
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Work (thermodynamics) ,business.industry ,020209 energy ,General Chemical Engineering ,Context (language use) ,02 engineering and technology ,industrial reformer ,kinetic model ,Kinetic energy ,Computer Science Applications ,steam methane reforming ,Steam reforming ,020401 chemical engineering ,0202 electrical engineering, electronic engineering, information engineering ,Environmental science ,0204 chemical engineering ,Process engineering ,business - Abstract
Catalyzed chemical reactions inside tubular reactors play a key role in steam methane reforming process, as they define the temperature and composition profiles of the reformer and, consequently, its efficiency. Although the kinetic modeling of reforming reactions has already been widely discussed, studies that carry out the comparison between kinetic reform models are still scarce. In this context, this work aims to evaluate the influence of different kinetics on the stationary behavior of industrial reformer. The kinetic models of Singh and Saraf (1979), Numaguchi and Kikuchi (1988), Xu and Froment (1989a), and Hou and Hughes (2001) were analyzed and compared with each other. All models describe the reformer satisfactorily with relative deviations around 3.5% compared to experimental and literature data. The results show that the simplest kinetic models present advantages compared to traditional models, such as Xu and Froment (1989a), which is widely used without any prior analysis.
- Published
- 2021
9. Biogas beyond CHP: The HPC (heat, power & chemicals) process
- Author
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Antonio Vita, Lidia Pino, Daniele Previtali, Alessandra Palella, Cristina Italiano, Andre Furtado Amaral, Flavio Manenti, Andrea Bassani, Giulia Bozzano, and Carlo Pirola
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Process (engineering) ,020209 energy ,CHP ,Biogas ,02 engineering and technology ,Industrial and Manufacturing Engineering ,Energy policy ,Biogas,Reforming, Methanol, Biomethane, CHP ,020401 chemical engineering ,Reforming ,0202 electrical engineering, electronic engineering, information engineering ,Production (economics) ,0204 chemical engineering ,Electrical and Electronic Engineering ,Operating expense ,Civil and Structural Engineering ,Rate of return ,Waste management ,business.industry ,Mechanical Engineering ,Methanol ,Settore ING-IND/25 - IMPIANTI CHIMICI ,Subsidy ,Building and Construction ,Pollution ,Settore AGR/15 - SCIENZE E TECNOLOGIE ALIMENTARI ,General Energy ,Environmental science ,Electricity ,business ,Biomethane - Abstract
The techno-economic feasibility of three biogas utilization processes was assessed through computer simulations on commercial process simulator Aspen HYSYS: HPC (biogas to methanol), BioCH4 (biogas to biomethane) and CHP (biogas to heat & electricity). The last two processes are already used commercially with the aid of subsidy policies. The economic analysis indicates that, without these policies, none of these attain economic self-sustainability due to high overall manufacturing costs. The estimated minimum support cost (MSCs) were 108, 62 and 109 €/MWh for the HPC, BioCH4 and CHP processes, respectively. The model could explain currently practised government subsidies in Italy and Germany. It was seen that the newly proposed HPC process is economically comparable to the traditional CHP process. Therefore, the HPC process is a possible alternative to biogas usage. A support policy was proposed: 50, 66, 158 and 148 €/MWh for available heat, methane, electricity and methanol (respectively); the proposed energy policy results in a 10% OpEx rate of return for any of the processes, thus avoiding a disparity in the production of different products.
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- 2020
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10. Histórias no Singular: Textos, Práticas & Sujeitos
- Author
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Giselle Martins Venancio, Nayara Galeno do Vale, André Furtado, Giselle Martins Venancio, Nayara Galeno do Vale, and André Furtado
- Abstract
Histórias no Singular: textos, práticas & sujeitos, livro organizado por Giselle Martins Venancio, Nayara Galeno do Vale e André Furtado, reúne uma plêiade de jovens pesquisadores brasileiros instigados em desvelar e compreender as ações e trajetórias de diferentes sujeitos sociais. Personagens de histórias em quadrinhos, historiadores, folcloristas, educadoras, escritores, entre outros são aqui abordados, promovendo uma enriquecedora discussão acerca do papel do indivíduo e de seu contexto social. Desde a Grécia clássica que os historiadores costuravam suas narrativas por intermédio de discursos (logoi) e ações de diversos personagens. Em Hecateu de Mileto, Heródoto e Tucídides, historiadores do VI e V séculos a.C., são exploradas as atuações de generais, guerreiros, sacerdotes, tiranos e reis.
- Published
- 2020
11. Biomass to X: Gasification and Pyrolysis Integrated
- Author
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Andre Furtado Amaral, Carlo Pirola, Giulia Bozzano, and Flavio Manenti
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Optimal design ,Work (thermodynamics) ,business.industry ,Economic analysis ,Environmental science ,Biomass ,Process engineering ,business ,Pyrolysis ,Syngas - Abstract
In this work (part of a series in which different biomass conversion routes are studied) a novel coupling between gasification and pyrolysis is described: by means of a design parameter (α) biomass is distributed between these two operations. In order to characterize the quality of the syngas produced, simulations are performed with a gasification / pyrolysis simulator, GASDS. Profiles were obtained for oxygen consumption, together with bio-char, syngas and steam production as a function of α. In a further work, an economic analysis shall define optimal design conditions.
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- 2017
12. Methanol Production from Biomass Gasification: Techno-Economic Assessment of Different Feedstocks.
- Author
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Amaral, Andre Furtado, Previtali, Daniele, Dell'Angelo, Anna, Bisotti, Filippo, Di Pretoro, Alessandro, Andoglu, Ecem M., Colombo, Simone, and Manenti, Flavio
- Subjects
METHANOL production ,BIOMASS gasification ,FEEDSTOCK ,COMPUTER simulation ,HEMICELLULOSE - Abstract
This work presents an updated techno-economic assessment of methanol production, considering an entrained flow gasifier with different second generation biomasses. Computer simulations were performed with the aid of a gasification simulator GasDS and with commercial process simulator Aspen HYSYS. A method was proposed to determine biomass composition in terms of cellulose, hemicellulose and three surrogate compounds that account for the most abundant monomers that compose lignin chains; the lower heat value (LHV) relative error was not bigger than 10%. The kinetic model deriving from this biomass characterization (composition) is not sufficiently accurate to describe biomass gasification; this is due to unrealistically small residence times and the (not modelled) catalytic effect of molten slag. Biomass gasification output is efficiently estimated by using chemical equilibrium. At current methanol market price (350 €/t) the process is economically unfeasible at the current plant capacity of 100 MW LHV biomass input (production costs vary between 360 and 440 €/t). [ABSTRACT FROM AUTHOR]
- Published
- 2019
- Full Text
- View/download PDF
13. Smart Implementation of Bender Equation of State.
- Author
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Bisotti, Filippo, di Pretoro, Alessandro, Dell'Angelo, Anna, Previtali, Daniele, Amaral, Andre Furtado, Andoglu, Ecem Muge, and Manenti, Flavio
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EQUATIONS of state ,MATRICES (Mathematics) ,CROSS product (Mathematics) ,EXPERIMENTAL design ,SEPARATION of gases - Abstract
In this paper matrix and vector products are exploited to reformulate Bender Equation of State. Finally, the new formulation is used to generate results which has been compared with experimental data sets available in literature and the analogous findings coming from different thermodynamic packages commonly used in Aspen Hysys for Air Separation Unit. [ABSTRACT FROM AUTHOR]
- Published
- 2019
- Full Text
- View/download PDF
14. Modelagem e resolução numérica dos sistemas de equações de uma torre de resfriamento em corrente cruzada
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Andre Furtado Amaral and Idalmo Montenegro de Oliveira
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Torre de Resfriamento ,Corrente Cruzada ,Simulação ,Engenharia quimica ,Modelagem - Abstract
Foi desenvolvido um modelo para representar uma torre de resfriamento operando em corrente cruzada a partir de balanços diferenciais de massa e energia. A utilização de uma função de ativação permitiu a unificação das formulações de gás saturado e insaturado, o que simplificou a forma final do sistema de equações resultantes e o seu processo de dedução. O modelo fez uso de expressões para a transferência de massa e energia que foram originadas a partir de analogias com o transporte de vapor e calor através de ar estagnado em um tubo vertical. O uso da expansão em séries de potência permitiu a criação de um sistema simplificado de equações, válido para baixos valores de umidade e baixas taxas de transferência de massa. Vários métodos numéricos foram propostos para a solução do sistema de equações diferenciais resultantes, dentre os quais estão o método de Euler, do Pontomédio, de BulirschStoer e o de Runge Kutta de 4ª ordem. Tais métodos foram usados na resolução do sistema de equações segundo o esquema proposto, o qual requereu a combinação de dois desses métodos: um para a direção principal e outro para a direção secundária. Neste esquema, cada uma das direções (principal e secundária) esteve associada a uma das fases (ar ou água) e a solução das equações da direção principal sempre precedeu a solução daquelas da direção secundária. As simulações foram realizadas através de scripts em Matlab® R2013b e foram utilizados os dados de BOUROUNI ET AL, GROBBELAAR ET AL E CORTINOVIS ET AL. Exceto para os dados fornecidos por BOUROUNI ET AL, os valores encontrados para os coeficientes de transferência de massa foram próximos daqueles reportados pelos autores. O valor reportado por BOUROUNI ET AL foi aproximadamente 45 vezes maior que o valor encontrado neste trabalho. Associase a tal discrepância o uso do método de Gauss Seidel por tais autores, o qual é um método de convergência lenta e baixa precisão. Os dados de CORTINOVIS ET AL são mais bem representados pelo modelo proposto nesse trabalho que aquele proposto por tais autores. Tal conclusão advém da grande concordância entre os resultados teóricos e experimentais relacionados com a correlação levantada para o coeficiente de transferência de massa. Utilizouse os dados de BOUROUNI ET AL para a realização de comparações entre os diferentes métodos numéricos. A combinação mais rápida e precisa foi aquela em que o método do Pontomédio e de Runge Kutta foram utilizados para a resolução das direções principal e secundária (respectivamente). O gás foi escolhido como componente principal e o domínio foi dividido em cinco intervalos na direção x e seis na direção y. Utilizouse a formulação exata do sistema de equações e a função de ativação degrau. O sistema de equações apresentado é particularmente desafiador devido à grande variação de temperaturas do líquido ao longo do domínio. A configuração escolhida, por ter conseguindo atingir alta precisão para tal sistema, não deve encontrar grandes dificuldades em apresentar bons resultados na resolução do sistema de equações de outras torres de resfriamento. A model was developed for the representation of a crossflow cooling tower through differential mass and energy balances. The use of activation functions allowed the unification of the saturated and insaturated gas formulations, thus enabling a simpler presentation of the system of equations and its development. The model used mass and energy transfer equations which were derived from analogies with the transport of steam and heat in a vertical tube through stagnant air. Power series expansions of the resulting equation system permitted the simplification of such system, one which is valid for low humidity values and low mass transfer rates. Several numerical methods were proposed for the solution of the resulting differential equation system, among which are Eulers method, the Midpoint method, BulirschStoers and the 4th order RungeKutta method. Such methods were used for solving the system of equations following the proposed scheme, which required the combination of two of these methods at a time: one for the main direction and another for the secondary direction. In this scheme each of the directions (main and secondary) were associated with one of the phases (air or water) and the solutions of the equations of the main direction always preceded those from the secondary direction. The simulations were run in scripts in Matlab® R2013b with the data of BOUROUNI ET AL, GROBBELAAR ET AL and CORTINOVIS ET AL. Except for the data acquired from BOUROUNI ET AL, the values found for the mass transfer coefficient were close to those reported by the other authors. The value reported by BOUROUNI ET AL was approximately 45 times greater than the one found in this work. Such discrepancy is attributed to the use of the GaussSeidel method by such authors, which is a slowconvergence, lowprecision method. The data from CORTINOVIS ET AL is better represented by the models proposed in this work than by the models proposed by such authors. Such conclusion is drawn from the close agreement between theoretical and experimental values of the mass transfer coefficient related to the correlation obtained. The data of BOUROUNI ET AL was used for the comparison of different numerical methods. The fastest, most precise configuration was the one in which the Midpoint and RungeKutta methods was used in the main and secondary direction (respectively). The gas was chosen as the main component and the dominium was divided in five intervals in the direction and six in the direction. The exact formulation of the system of equations was used, together with the step activation function. The presented system of equations is particularly challenging due to the great steepness of the liquid temperature profile through the dominium. After achieving a high precision for such a system, the chosen configuration shall not present difficulties in delivering good results when dealing with other cooling tower equation systems.
- Published
- 2015
15. Evaluation of an oviposition-stimulating kairomone for the yellow fever mosquito, Aedes aegypti, in Recife, Brazil
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Rosângela M R, Barbosa, Andre, Furtado, Lêda, Regis, and Walter S, Leal
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Aedes ,Oviposition ,Fatty Acids ,Yellow Fever ,Animals ,Female ,Myristic Acid ,Myristic Acids ,Brazil ,Pheromones - Abstract
A synthetic mixture of an oviposition-stimulating kairomone for the yellow fever mosquito, Aedes aegypti, comprising of 83% tetradecanoic acid, 16% nonanoic acid and 1% tetradecanoic acid methyl ester (NTT, in short) was tested in a dengue endemic area in Recife, Brazil. Gravid female mosquitoes confined to a cage under semi-field conditions deposited significantly higher numbers of eggs in traps baited with NTT at doses ranging from 0.6 to 600 ng/microl than in control (water) traps. When tested in homes, egg-laying in traps baited with 60 ng NTT/microl (final concentration in trap, approximately 3.33 ng/ml) and in control traps was not significantly different, but egg deposited in traps with lower dosage (6 ng NTT/microl; final concentration in trap, approximately 0.33 ng/ml) was significantly higher than in control traps. In subsequent trials, the numbers of eggs laid in traps baited with 0.6 ng NTT/microl (final concentration in trap, approximately 0.033 ng/ml) were not significantly different from the numbers deposited in trap loaded with 6 ng NTT/microl. Egg-laying was significantly higher in these treatments than in control traps.
- Published
- 2010
16. Dorstenia cayapia: agronomic aspects
- Author
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Carvalho, Andre Furtado, Silva, Monalisa Alves Diniz da, Luz, José Magno Queiroz, Santana, Denise Garcia de, and Carauta, Jorge Pedro Pereira
- Subjects
Brotação ,Protrusão ,Protrusion ,Dorstenia - Propagação ,Germinação ,CIENCIAS AGRARIAS::AGRONOMIA [CNPQ] ,Germination ,Rizoma ,Sprouting ,Carapiá ,Rizhome - Abstract
Conselho Nacional de Desenvolvimento Científico e Tecnológico Dorstenia cayapia Vellozo (Carapiá) is a native, shade living and medicinal grass. It belongs to the category "threatened" due to drastic habitat reduction and population decline to a critical level. This work was carried through in glasshouse at Laboratory of Seed Analysis and Experimental Farm of Glória, Uberlândia MG, pertaining to the Center of Agrarian Sciences of the Federal University of Uberlândia and had as objective to get part of agronomic informations that allow to cultivate and explore carapiá rationally permitting at the carapiá specie preservation and attainment of material cultivated for phytotherapeutic products. Three experiments had been carried through: Experiment 1: rhizome prop, Experiment 2: physiological quality of seeds and Experiment 3: plant development came from prop experiment in field. In the rhizome prop Experiment 3, three substrata, three rhizome parts and two types of tray had been evaluated. The delineation was entirely randomized (DIC) in a factorial design (3x3x2). In the experiment of seed physiological quality, the following studies had been carried through: number of seeds by alveolus, degree of humidity, weight of a thousand seeds, seed germination by using different kind of stratum and temperature, electric conductivity, drenching and seed physiological conditioning. The germination assay consisted of two temperatures and three substrata.The delineation used was an entirely randomized design (ERD) in a factorial scheme (3x2). In the electric conductivity, different times of drenching were tested and evaluated through conductive meter readings. The seed drenching consisted of different periods in water contact and these seeds had been used for determination of physiological conditioning. Experiment 3 evaluated the development of sprouted plants came from Experiment 1 in seedbeds under shade plastic sheet by using 20 x 20 cm space during six months. The substrata had not affected the sprouting in trays and in field plant development. The apical part of rizhome sprouting was superior to basal and medium positions. The 128 tray cell was better than in 200 tray cells of rhizome sproutings. The plotting paper substratum and the constant 25 ºC temperature makes possible high seed germination. The electric conductivity can be used to determine the seed vigor of Dorstenia cayapia. The assays of drenching and physiological conditioning had not been significant to improve the indices related with the germination. Six months after transplanting in field, an increasing in relation to plant dry mass taken in tray root was observed, approximately 10 times higher than that produced by underground part and 41 times by aerial part. Dorstenia cayapia Vellozo - Moraceae (carapiá) é uma erva nativa e medicinal. Pertence à categoria vulnerável , devido à drástica redução dos seus habitats e ao declínio populacional. Este trabalho foi realizado na casa de vegetação, no Laboratório de Análise de Sementes e na Fazenda Experimental do Glória, Uberlândia - Minas Gerais, Brasil, pertencentes ao Centro de Ciências Agrárias da Universidade Federal de Uberlândia e teve como objetivo obter parte das informações agronômicas que permitam cultivar e explorar racionalmente o carapiá, visando à conservação da espécie e obtenção de material cultivado para produtos fitoterápicos e indústria química. Foram realizadas três pesquisas: experimento 1: estaquia de rizomas; experimento 2: qualidade fisiológica das sementes; e experimento 3: desenvolvimento das plantas do experimento de estaquia, em campo. No experimento de estaquia de rizomas avaliaram-se 3 substratos, 3 partes de rizoma e 2 tipos de bandeja. O delineamento foi inteiramente casualisado (DIC) em esquema fatorial (3x3x2). No experimento da qualidade fisiológica das sementes, foram realizadas as seguintes pesquisas: número de sementes por cenanto, grau de umidade, peso de mil sementes, germinação das sementes utilizando-se diferentes substratos e temperaturas, condutividade elétrica, embebição e condicionamento fisiológico de sementes. O ensaio de germinação constou de duas temperaturas e três substratos. O delineamento foi inteiramente casualisado (DIC) em esquema fatorial (3x2). Na condutividade elétrica foram testados diferentes tempos de embebição e avaliados através do condutivímetro. A embebição das sementes constou de diferentes períodos em contato com a água e essas sementes foram utilizadas para o condicionamento fisiológico. No experimento 3 avaliou-se o desenvolvimento das plantas brotadas do experimento 1, em canteiros sob sombrite, no espaçamento de 20 x 20 cm, por aproximadamente 6 meses. Os substratos não tiveram efeito na brotação dos rizomas em bandejas. A brotação da parte apical do rizoma foi superior às brotações das posições basal e mediana do rizoma. A bandeja de 128 células foi melhor do que a bandeja de 200 células, nas brotações de rizoma. Os substratos papel mataborrão e vermiculita, na temperatura constante de 25ºC, possibilitaram maior germinação das sementes. A condutividade elétrica pôde ser utilizada para determinar o vigor das sementes de Dorstenia cayapia. O condicionamento fisiológico não proporcionou melhoria ao potencial fisiológico das sementes. O tipo de substrato e o tipo de bandeja não afetaram o desenvolvimento das plantas, em campo. Aproximadamente seis meses após transplante em campo, observou-se um acréscimo, em relação à massa seca das plantas enraizadas em bandeja, de aproximadamente 10 vezes a parte subterrânea e 41 vezes a parte aérea. Mestre em Agronomia
- Published
- 2008
17. Education and rehabilitation in a prison setting
- Author
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Andre Furtado and Don Johnson
- Subjects
Fallacy ,education.field_of_study ,business.industry ,media_common.quotation_subject ,Population ,Rehabilitation ,Alienation ,Prison ,Interpersonal communication ,Public relations ,Bachelor ,Variety (cybernetics) ,Reading (process) ,Pedagogy ,business ,education ,Psychology ,Law ,media_common - Abstract
This paper examines the physical environment, institutional structure and objectives, interpersonal dynamics, and shortcomings of existing treatment programs, especially the counseling process, at the State Prison of Southern Michigan at Jackson (population greater than 5,000) with a view to providing a perspective on the difficulties in creating and sustaining a genuine learning situation in such an environment. Next, the evolution and adaptation of an innovative multidisciplinary four-year Bachelor of General Studies Degree program for such a setting using a variety of instructional formats (workshops, conferences, television) is described. Provisions for specialization, and student involvement in and reaction to the program and ways of dealing with reading, writing and math skill deficiency are discussed. Next, a reform proposal that recognizes the fallacy of rehabilitation in the course of punishment is suggested. Lastly, the role of the larger society in fostering the alienation that leads to crime i...
- Published
- 1980
- Full Text
- View/download PDF
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