Backpressure effects on the flow-pressure relation of driplines

ABSTRACT For drip irrigation design and management, it is necessary to know the relation between flow and pressure acting on emitters. In the case of subsurface drip irrigation, the backpressure phenomenon may change the hydraulic characteristics of emitters. Thus, this study aimed at determining such relationship between flow and pressure of different driplines in surface and subsurface conditions; aiming to find possible differences in hydraulic behavior. We tested four emitter types; two pressure compensating (D5000 and Hydro PCND) and two non-pressure compensating (TalDrip and Jardiline). Emitter flow rates were attained in atmospheric conditions and submerged in water, in which submergence levels represented backpressure. Assays were performed using inlet pressures of 80, 100, 120, and 150 kPa for the Hydro PCND dripline and 25, 50, 100, and 150 kPa for the other ones; the backpressures were of 0.49, 1.47, 2.45, 4.41 and 6.37 kPa with four replications. The emitters had their proportionality constants and discharge exponents changed in submerged applications, representing backpressure effect. Non-pressure compensating emitters had their discharge exponent decreased, while in pressure compensating ones, it was increased. Backpressure reduced emitter flow rates at all evaluated pressures.

Determination of picloram in waters by sequential injection chromatography with UV detection

This paper describes a sequential injection chromatography procedure for determination of picloram in waters exploring the low backpressure of a 2.5 cm long monolithic C18 column. Separation of the analyte from the matrix was achieved in less than 60 s using a mobile phase composed by 20:80 (v v-1) acetonitrile:5.0 mmol L-1 H3PO4 and flow rate of 30 μL s-1. Detection was made at 223 nm with a 40 mm optical path length cell. The limits of detection and quantification were 33 and 137 μg L-1, respectively. The proposed method is sensitive enough to monitor the maximum concentration level for picloram in drinking water (500 μg L-1). The sampling frequency is 60 analyses per hour, consuming only 300 μL of acetonitrile per analysis. The proposed methodology was applied to spiked river water samples and no statistically significant differences were observed in comparison to a conventional HPLC-UV method.

A contribution for thermoeconomic modelling: A methodology proposal

This work presents a thermoeconomic optimization methodology for the analysis and design of energy systems. This methodology involves economic aspects related to the exergy conception, in order to develop a tool to assist the equipment selection, operation mode choice as well as to optimize the thermal plants design. It also presents the concepts related to exergy in a general scope and in thermoeconomics which combines the thermal sciences principles (thermodynamics, heat transfer, and fluid mechanics) and the economic engineering in order to rationalize energy systems investment decisions, development and operation. Even in this paper, it develops a thermoeconomic methodology through the use of a simple mathematical model, involving thermodynamics parameters and costs evaluation, also defining the objective function as the exergetic production cost. The optimization problem evaluation is developed for two energy systems. First is applied to a steam compression refrigeration system and then to a cogeneration system using backpressure steam turbine. (C) 2010 Elsevier Ltd. All rights reserved.

Supercritical steam cycles and biomass integrated gasification combined cycles for sugarcane mills

Back in 1970s and 1980s, cogeneration plants in sugarcane mills were primarily designed to consume all bagasse, and produce steam and electricity to the process. The plants used medium pressure steam boilers (21 bar and 300 degrees C) and backpressure steam turbines. Some plants needed also an additional fuel, as the boilers were very inefficient. In those times, sugarcane bagasse did not have an economic value, and it was considered a problem by most mills. During the 1990s and the beginning of the 2000s, sugarcane industry faced an open market perspective, thus, there was a great necessity to reduce costs in the production processes. In addition, the economic value of by-products (bagasse, molasses, etc.) increased, and there was a possibility of selling electricity to the grid. This new scenario led to a search for more advanced cogeneration systems, based mainly on higher steam parameters (40-80 bar and 400-500 degrees C). In the future, some authors suggest that biomass integrated gasification combined cycles are the best alternative to cogeneration plants in sugarcane mills. These systems might attain 35-40% efficiency for the power conversion. However, supercritical steam cycles might also attain these efficiency values, what makes them an alternative to gasification-based systems. This paper presents a comparative thermoeconomic study of these systems for sugarcane mills. The configurations studied are based on real systems that could be adapted to biomass use. Different steam consumptions in the process are considered, in order to better integrate these configurations in the mill. (C) 2009 Elsevier Ltd. All rights reserved.

Paikallisen energiayhtiön maakaasuliiketoimintojen kehittäminen

Työssä selvitetään mahdollisuuksia laajentaa kaasuliiketoimintaa sellaisilla alueilla, jotka sijaitsevat maakaasun siirtoputken läheisyydessä ja joilla kaukolämpöliiketoimintaa ei pidetä houkuttelevana vaihtoehtona. Tarkasteltavaksi valittiin yksi edellä mainitun kaltainen alue. Tutkimuksen pääasiallinen tarkoitus on vertailla kaukolämmön sekä maakaasun jakelun taloudellista kannattavuutta valitulla alueella. Työssä selvitetään maakaasun jakeluun ja käyttöön tarvittava laitteisto, sekä maakaasuliiketoiminnan taloudellinen kannattavuus. Työssä esitellään lisäksi mikroturbiinien toimintaperiaate ja selvitetään niiden käyttösovellukset sekä mitä mahdollisuuksia niiden käyttö tarjoaisi energiayhtiölle. Kaasuliiketoiminta on tutkitulla alueella kannattavampaa kuin kaukolämpö. Kaasuliiketoiminnasta tulee kannattavaa, jos asiakkaiksi saadaan yli 10 prosenttia alueen kiinteistöistä, kun asiakkailta peritään saman suuruiset maksut kuin kaukolämmöllä. Jos asiakasmaksuina käytetään sellaisia maksuja, että kaasusta tulee kuluttajalle edullisin lämmitystapa, niin tällöin kaasuliiketoiminnasta ei tule kannattavaa vielä 70 prosentin asiakasmäärälläkään. Mikroturbiinit eivät tämän hetkisillä sähkön hinnoilla ole energiayhtiölle järkevä tapa tuottaa sähköä ja lämpöä, sillä mikroturbiineilla tuotetun sähkön hinta on kaksinkertainen verrattuna kaasukombi vastapainelaitoksella tuotetun sähkön hintaan. Energiayhtiön on edullisempaa hankkia sähkö yhteispohjoismaisilta sähkömarkkinoilta, kuin tuottaa sitä mikroturbiinilla. Mikroturbiinit soveltuvat lähinnä kiinteistökohtaiseen sähkön- ja lämmöntuotantoon silloin, kun turbiinin koko lämmön ja sähkön tuotanto saadaan hyödynnettyä ja turbiinin omistaa kiinteistö. Tällöin kiinteistön energiakustannukset jäävät kiinteistökohtaisella mikroturbiinilla pienemmiksi kuin hankkimalla sähkö ja lämpö energiayhtiöltä.

Tukkusähkön hintapiikkeihin reagoinnin keinot sellu- ja kartonkitehtaalla.

Sähkön tukkuhinnat vaihtelivat hyvin voimakkaasti talvella 2009–2010. Työssä on esitetty rajahyötytarkasteluna yhdistetyn sellu- ja paperitehtaan mahdollisuudet lisätä vastapainesähkön tuotantoa sekä leikata sähkön kulutusta aikana, jolloin sähkön tuntihinta on korkea. Työssä tarkastellaan myös erilaisia sähkömarkkinaoperaatioita. Työn ensimmäisessä osiossa esitellään Stora Enson Imatran tehtaat. Myöhemmissä kappaleissa perehdytään pohjoismaisten sähkömarkkinoiden sekä kaasupörssin toimintaan. Jotta korkeista sähkön hinnoista voitaisiin hyötyä, tulee sähkön myyntitarjoukset jättää sähköpörssi Nord Poolin kaupankäyntijärjestelmään toimitusvuorokautta edeltävänä päivänä. Tässä työssä on määritetty sähköenergian mahdolliset myyntivolyymit sekä hinnat eri tuotantotilanteissa. Työssä pyritään parantamaan tehtaan sähkökaupankäynnin kannattavuutta käyttämällä eri sähkökaupan tuotteita. Työssä esitetään malleja, joiden avulla korkeita sähkön markkinahintoja voidaan pyrkiä hyödyntämään. Eri sähkömarkkinatuotteet soveltuvat myös riskienhallintaan voimakkaasti vaihtelevilla sähkömarkkinoilla

Development of a sequential injection chromatography (SIC) method for determination of simazine, atrazine, and propazine

This paper describes the development of a sequential injection chromatography (SIC) procedure for separation and quantification of the herbicides simazine, atrazine, and propazine exploring the low backpressure of a 2.5 cm long monolithic C(18) column. The separation of the three compounds was achieved in less than 90 s with resolution > 1.5 using a mobile phase composed by ACN/1.25 mmol/L acetate buffer (pH 4.5) at the volumetric ratio of 35:65 and flow rate of 40 mu L/s. Detection was made at 223 nm using a flow cell with 40 mm of optical path length. The LOD was 10 mu g/L for the three triazines and the quantification limits were of 30 mu g/L for simazine and propazine and 40 mu g/L for atrazine. The sampling frequency is 27 samples per hour, consuming 1.1 mL of ACN per analysis. The proposed methodology was applied to spiked water samples and no statistically significant differences were observed in comparison to a conventional HPLC-UV method. The major metabolites of atrazine and other herbicides did not interfere in the analysis, being eluted from the column either together with the unretained peak, or at retention times well-resolved from the studied compounds.

Modelagem dinâmica do escoamento de um sistema de elevação por plunger lift

A critical problem in mature gas wells is the liquid loading. As the reservoir pressure decreases, gas superficial velocities decreases and the drag exerted on the liquid phase may become insufficient to bring all the liquid to the surface. Liquid starts to drain downward, flooding the well and increasing the backpressure which decreases the gas superficial velocity and so on. A popular method to remedy this problem is the Plunger Lift. This method consists of dropping the "plunger"to the bottom of the tubing well with the main production valve closed. When the plunger reaches the well bottom the production valve is opened and the plunger carry the liquid to the surface. However, models presented in literature for predicting the behavior in plunger lift are simplistic, in many cases static (not considering the transient effects). Therefore work presents the development and validation of a numerical algorithm to solve one-dimensional compressible in gas wells using the Finite Volume Method and PRIME techniques for treating coupling of pressure and velocity fields. The code will be then used to develop a dynamic model for the plunger lift which includes the transient compressible flow within the well

A contribution for thermoeconomic modelling: A methodology proposal

This work presents a thermoeconomic optimization methodology for the analysis and design of energy systems. This methodology involves economic aspects related to the exergy conception, in order to develop a tool to assist the equipment selection, operation mode choice as well as to optimize the thermal plants design. It also presents the concepts related to exergy in a general scope and in thermoeconomics which combines the thermal sciences principles (thermodynamics, heat transfer, and fluid mechanics) and the economic engineering in order to rationalize energy systems investment decisions, development and operation. Even in this paper, it develops a thermoeconomic methodology through the use of a simple mathematical model, involving thermodynamics parameters and costs evaluation, also defining the objective function as the exergetic production cost. The optimization problem evaluation is developed for two energy systems. First is applied to a steam compression refrigeration system and then to a cogeneration system using backpressure steam turbine. (C) 2010 Elsevier Ltd. All rights reserved.

Optimization analysis of dual-purpose systems

This paper aims to analyze dual-purpose systems focusing the total cost optimization; a superstructure is proposed to present cogeneration systems and desalination technologies alternatives for the synthesis process. The superstructure consists of excluding components, gas turbines or conventional steam generators with excluding alternatives of supplying fuel for each combustion system. Also, backpressure or condensing/extraction steam turbine for supplying process steam could be selected. Finally one desalination unit chosen between electrically-driven or steam-driven reverse osmosis. multi-effect and multistage flash should be included. The analysis herein performed is based on energy and mass conservation equations, as well as the technological limiting equation of equipment. The results for ten different commercial gas turbines revealed that electrically-driven reverse osmosis was always chosen together with both natural gas and gasified biomass gas turbines. (C) 2009 Elsevier B.V. All rights reserved.

Avaliação termodinâmica, termoeconômica e econômica da integração de sistemas de gaseificação da biomassa em uma usina sucroalcooleira

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

Estudo da permeabilidade dos solos de fundação do aterro de resíduos sólidos urbanos de Bauru

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

Análise de sistemas de cogeração com gaseificação de licor negro no setor de papel e celulose

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

Síntese otimizada de sistemas de cogeração e dessalinização

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

Black liquor gasification combined cycle with CO2 capture-Technical and economic analysis

Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)