991 resultados para volume flow
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Mode of access: Internet.
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A new flow-injection analytical procedure is proposed for the determination of the total amount of polyphenols in wines; the method is based on the formation of a colored complex between 4-aminoantipyrine and phenols, in the presence of an oxidizing reagent. The oxidizing agents hexacyanoferrate(III), peroxodisulfate, and tetroxoiodate(VII) were tested. Batch trials were first performed to select appropriate oxidizing agents, pH, and concentration ratios of reagents, on the basis of their effect on the stability of the colored complex. Conditions selected as a result of these trials were implemented in a flow-injection analytical system in which the influence of injection volume, flow rate, and reaction- coil length, was evaluated. Under the optimum conditions the total amount of polyphenols, expressed as gallic acid, could be determined within a concentration range of 36 to 544 mg L–1, and with a sensitivity of 344 L mol–1 cm–1 and an RSD <1.1%. The reproducibility of analytical readings was indicative of standard deviations <2%. Interference from sugars, tartaric acid, ascorbic acid, methanol, ammonium sulfate, and potassium chloride was negligible. The proposed system was applied to the determination of total polyphenols in red wines, and enabled analysis of approximately 55 samples h–1. Results were usually precise and accurate; the RSD was <3.9% and relative errors, by the Folin–Ciocalteu method, <5.1%.
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This paper provides a comparative study of the performance of cross-flow and counter-flow M-cycle heat exchangers for dew point cooling. It is recognised that evaporative cooling systems offer a low energy alternative to conventional air conditioning units. Recently emerged dew point cooling, as the renovated evaporative cooling configuration, is claimed to have much higher cooling output over the conventional evaporative modes owing to use of the M-cycle heat exchangers. Cross-flow and counter-flow heat exchangers, as the available structures for M-cycle dew point cooling processing, were theoretically and experimentally investigated to identify the difference in cooling effectiveness of both under the parallel structural/operational conditions, optimise the geometrical sizes of the exchangers and suggest their favourite operational conditions. Through development of a dedicated computer model and case-by-case experimental testing and validation, a parametric study of the cooling performance of the counter-flow and cross-flow heat exchangers was carried out. The results showed the counter-flow exchanger offered greater (around 20% higher) cooling capacity, as well as greater (15%–23% higher) dew-point and wet-bulb effectiveness when equal in physical size and under the same operating conditions. The cross-flow system, however, had a greater (10% higher) Energy Efficiency (COP). As the increased cooling effectiveness will lead to reduced air volume flow rate, smaller system size and lower cost, whilst the size and cost are the inherent barriers for use of dew point cooling as the alternation of the conventional cooling systems, the counter-flow system is considered to offer practical advantages over the cross-flow system that would aid the uptake of this low energy cooling alternative. In line with increased global demand for energy in cooling of building, largely by economic booming of emerging developing nations and recognised global warming, the research results will be of significant importance in terms of promoting deployment of the low energy dew point cooling system, helping reduction of energy use in cooling of buildings and cut of the associated carbon emission.
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Purpose: To investigate whether regional long-term changes in peripapillary retinal flow, measured by scanning laser Doppler flowmetry (SLDF), occur in patients with primary open angle glaucoma (POAG). Methods: 31 healthy volunteers (mean age: 65 8.3 years) and 33 POAG patients (mean age: 71.2 7.6 years) were followed up every 4 months for 16 months. Using SLDF, three images of the superior and inferior optic nerve head were obtained for each subject. A 1010-pixel frame was used to measure blood flow, volume and velocity in the four quadrants of the peripapillary retina. Central 24-2 visual field testing was carried out at each visit. Repeated measures analysis of covariance was used to assess change over time between the normal and POAG groups for the SLDF parameters. Univariate linear regression analysis for mean deviation and glaucoma change probability (GCP) analysis were used to identify visual field progression. Results: Blood volume, flow and velocity measured in the inferior nasal quadrant of the peripapillary retina decreased significantly over time for the POAG group compared to the normal group (p=0.0073, 0.0097, 0.0095 respectively). Overall, 2 glaucoma patients showed a significantly deteriorating MD slope, while 7 patients showed visual field progression with GPA. All of the patients progressing with GPA, showed change in the superior hemifield and, of those, 14% showed change in the inferior hemifield. Conclusion: Glaucoma patients showed a decrease in blood flow, volume and velocity in the inferior nasal peripapillary retina. A regional variation in microvascular retinal capillary blood flow may provide insight into the pathogenesis of glaucomatous optic neuropathy. Keywords: 331 blood supply • 554 retina • 624 visual fields
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The volume of the primary (PCS) and secondary (SCS) circulatory system in the Atlantic cod Gadus morhua was determined using a modified dye dilution technique. Cod (N=10) were chronically cannulated in the second afferent branchial artery with PE-50 tubing. Evans Blue dye was bound to harvested fish plasma at a concentration of 1 mg dye ml(-1) plasma, and injected at a concentration of 1 mg kg(-1) body mass. Serial sampling from the cannula produced a dye dilution curve, which could be described by a double exponential decay equation. Curve analysis enabled the calculation of the primary circulatory and total distribution volume. The difference between these volumes is assumed to be the volume of the SCS. From the dilution curve, it was also possible to calculate flow rates between and within the systems. The results of these experiments suggest a plasma volume in the PCS of 3.42+/-0.89 ml 100 g(-1) body mass, and in the SCS of 1.68+/-0.35 ml 100 g(-1) body mass (mean +/- S.D.) or approximately 50% that of the PCS. Flow rates to the SCS were calculated as 2.7% of the resting cardiac output. There was an allometric relationship between body mass and blood volumes. Increasing condition factor showed a tendency towards smaller blood volumes of the PCS, expressed as percentage body mass, but this was not evident for the volume of the SCS.
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Työssä tarkastellaan vortex-putken soveltuvuutta kostean ilman kuivatukseen ja vapautuvan latenttilämmön hyödyntämiseen. Soveltuvuutta arvioidaan veden ja ilman massataseita hyväksi käyttäen ja stationaarisen systeemin energiataseen avulla. Työn mittauksia varten rakennettiin koelaitteisto, jonka avulla mitattiin miten lämpötilaerot kuumassa ja kylmässä päässä käyttäytyivät mitattaessa kuivalla ilmalla ja ilmalla, jota oli kostutettu. Mitattavia suureita olivat syöttöpaine- ja lämpötila, lämpötilat kuumassa ja kylmässä päässä, kuuman pään paine ja tilavuusvirta tai virtausnopeus ja kuuman pään suhteellinen kosteus. Mittaustulosten avulla laskettiin lämpötilan muutokset kummassakin päässä ja verrattiin kuivan ja kostean ilman mittauksien tuloksia toisiinsa. Lisäksi laskettiin tiivistyneen veden määrä ja veden ja ilman massavirrat molemmissa päissä. Näin voitiin laskea tiivistymisessä vapautuva energia ja tarkastella mihin se siirtyy. Tulosten perusteella vortex-putki soveltuu hyvin huonosti ilman kuivatukseen. Tiivistyneen veden määrä ja sitä kautta tiivistymisessä vapautunut energia, olivat pieniä. Suurin osa kosteudesta meni kuuman pään virtauksen mukana. Tiivistymisessä vapautunut energia siirtyi kylmään päähän.
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In a centrifugal compressor the flow around the diffuser is collected and led to the pipe system by a spiral-shaped volute. In this study a single-stage centrifugal compressor with three different volutes is investigated. The compressorwas first equipped with the original volute, the cross-section of which was a combination of a rectangle and semi-circle. Next a new volute with a fully circular cross-section was designed and manufactured. Finally, the circular volute wasmodified by rounding the tongue and smoothing the tongue area. The overall performance of the compressor as well as the static pressure distribution after the impeller and on the volute surface were measured. The flow entering the volute was measured using a three-hole Cobra-probe, and flow visualisations were carriedout in the exit cone of the volute. In addition, the radial force acting on theimpeller was measured using magnetic bearings. The complete compressor with thecircular volute (inlet pipe, full impeller, diffuser, volute and outlet pipe) was also modelled using computational fluid dynamics (CFD). A fully 3-D viscous flow was solved using a Navier-Stokes solver, Finflo, developed at Helsinki University of Technology. Chien's k-e model was used to take account of the turbulence. The differences observed in the performance of the different volutes were quite small. The biggest differences were at low speeds and high volume flows,i.e. when the flow entered the volute most radially. In this operating regime the efficiency of the compressor with the modified circular volute was about two percentage points higher than with the other volutes. Also, according to the Cobra-probe measurements and flow visualisations, the modified circular volute performed better than the other volutes in this operating area. The circumferential static pressure distribution in the volute showed increases at low flow, constant distribution at the design flow and decrease at high flow. The non-uniform static pressure distribution of the volute was transmitted backwards across the vaneless diffuser and observed at the impeller exit. At low volume flow a strong two-wave pattern developed into the static pressure distribution at the impeller exit due to the response of the impeller to the non-uniformity of pressure. The radial force of the impeller was the greatest at the choke limit, the smallest atthe design flow, and moderate at low flow. At low flow the force increase was quite mild, whereas the increase at high flow was rapid. Thus, the non-uniformityof pressure and the force related to it are strong especially at high flow. Theforce caused by the modified circular volute was weaker at choke and more symmetric as a function of the volume flow than the force caused by the other volutes.
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Diplomityön tavoitteena oli selvittää hienopaperitehtaan BOD-päästön vähentämismahdollisuudet. Tehtaalla tapahtuvien uudistusten vaikutus BOD-päästön määrään selvitettiin. Lisäksi selvitettiin uudistetun paperivalmistusprosessin BOD-päästön alkuperä ja syntyvien jätevesien tilavuusvirta. BOD:n kuormitusmäärän kehittymistä arvioitiin mallintamalla. Kirjallisuusosassa on käsitelty hienopaperin valmistusprosessin vaiheita sekä tarkasteltu paperitehtaan vedenkäyttöä ja vesikiertoja. Myös jätevesien COD- ja BOD-kuormituslähteet on selvitetty. Kokeellinen osa alkaa hienopaperitehtaan prosessikuvauksella. Paperitehtaan malli rakennettiin VTT:n Tekesin CACTUS-teknologiaohjelmassa kehittämällä Balas-simulointiohjelmalla. Kokeellisessa osassa on käyty läpi mallin rakennusvaiheet. Paperinvalmistusprosessissa toteutettavien uudistusvaiheiden vaikutus päästöihin mallinnettiin. Tuloksena voitiin todeta, että tehtaan tuotantosuunnan ja -määrien muutoksesta huolimatta BOD-päästö ei merkittävästi muutu. Sen sijaan ominaiskuormitus laskee. Ennen uudistuksia BOD-kuorma oli pääasiassa peräisin pintaliimatusta hylystä, kun taas uudistusten jälkeen suurin osa BOD-kuormasta tulee tuoremassojen mukana prosessiin.
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Tämän diplomityön tavoitteena oli sekundäärisen esiflotaation optimointi Stora Enso Sachsen GmbH:n tehtaalla. Optimoinnin muuttujana käytettiin vaahdon määrää ja optimointiparametreinä ISO-vaaleutta, saantoja sekä tuhkapitoisuutta. Lisäksi tutkittiin flotaatiosakeuden vaikutusta myös muihin tehtaan flotaatioprosesseihin. Kirjallisuusosassa tarkasteltiin flotaatiotapahtumaa, poistettavien partikkeleiden ja ilmakuplien kontaktia, vaahdon muodostumista sekä tärkeimpiä käytössä olevia siistausflotaattoreiden laiteratkaisuja. Kokeellisessa osassa tutkittiin flotaatiosakeuden pienetämisen vaikutuksia tehtaan flotaatioprosesseihin tuhkapitoisuuden, ISO-vaaleuden, valon sironta- ja valon absorpiokerrointen kannalta. Sekundäärisen esiflotaation optimonti suoritettiin muuttamalla vaahdon määrää kolmella erilaisella injektorin koolla, (8 mm, 10 mm ja 13 mm), joista keskimmäinen kasvattaa 30 % massan tilavuusvirtaa ilmapitoisuuden muodossa. Optimonnin tarkoituksena oli kasvattaa hyväksytyn massajakeen ISO-vaaleutta, sekä kasvattaa kuitu- ja kokonaissaantoa sekundäärisessä esiflotaatiossa. Flotaatiosakeuden pienentämisellä oli edullisia vaikutuksia ISO-vaaleuteen ja valon sirontakertoimeen kussakin flotaatiossa. Tuhkapitoisuus pieneni sekundäärisissä flotaatioissa enemmän sakeuden ollessa pienempi, kun taas primäärisissä flotaatiossa vaikutus oli päinvastainen. Valon absorptiokerroin parani jälkiflotaatioissa alhaisemmalla sakeudella, kun taas esiflotaatioissa vaikutus oli päinvastainen. Sekundäärisen esiflotaation optimoinnin tuloksena oli lähes 5 % parempi ISO-vaaleus hyväksytyssä massajakeessa. Kokonaissaanto parani optimoinnin myötä 5 % ja kuitusaanto 2 %. Saantojen nousu tuottaa vuosittaisia säästöjä siistauslaitoksen tuotantokapasiteetin noustessa 0,5 %. Tämän lisäksi sekundäärisessä esiflotaatiossa rejektoituvan massavirran pienentyminen tuottaa lisäsäästöjä tehtaan voimalaitoksella.
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This master’s thesis handles an operating model for an electric equipment supplier conducted sale oriented energy audit for pumping, fan and other motor applications at power plants. The study goes through the largest factors affecting internal electricity use at a power plant, finds an energy audit –like approach for the basis of information gathering and presents the information needed for conducting the analysis. The model is tested in practice at a kraft recovery boiler of a chemical pulping mill. Targets chosen represent some of the largest electric motor applications in the boiler itself and in its fuel handling. The energy saving potential of the chosen targets is calculated by simulating the energy consumption of the alternatives for controlling the targets, and thereafter combining the information with the volume flow duration curve. Results of the research are somewhat divaricated, as all the information needed is not available in the automation system. Some of the targets could be simulated and their energy saving potential calculated quite easily. At some of the targets chosen the monitoring was not sufficient enough for this and additional measurements would have been needed to base the calculations on. In traditional energy audits, energy efficiency of pump and fan applications is not necessarily examined. This means that there are good possibilities for developing the now presented targeted energy audit procedure basis further.
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An improved defoamer dosage procedure and a more efficient dosing point to the approach system were studied in this thesis. Their influence on paper machine wet end operations was investigated. The improved defoamer dosing procedure was examined at UMP-Kymmene Tervasaari PM8. Air content and its controlling methods at the paper machine were studied in the literature survey. Also the influence of dissolved gases and entrained air in the papermaking furnish were introduced. Feeding methods – a TrumpJet chemical mixer and traditional feeding devices – were reviewed. The defoamer’s functioning methods were studied. The influence of the use of defoamers was estimated based on the main selected wet end operations. In the experimental part, defoamer mixing with a traditional feeding method and two improved mixing stages were compared based on the air content profiles in PM8’s approach system. The reference dosage procedure was PM8’s old dosing system. The first dosage procedure in the comparison involved two TrumpJet chemical mixers installed on the bottom wire trays. The second element of comparison involved the improvement brought by a third TrumpJet chemical mixer installed on the top wire tray. This second comparison of the efficient defoamer feeding concept was made at a higher production speed of PM8. The air content control situation was also studied at the higher production speed. In addition the connection between the defoamer and air content was observed and a mill-scale system was studied. The economical benefits of the new dosing procedure were also reviewed. Air content profiles of short circulation were measured in the reference situation and the two comparison points of the study. These air content measurements proved the main gas load is introduced to PM8's paper furnish from the white water tray. Thick stock air content was not essential when the air volume flow was considered. The improved defoamer dosing procedure made lower dosage amounts possible. Compared with the traditional feeding system, the new defoamer feeding concept made only few direct improvements to the wet end operations and the produced paper itself. The lower defoamer need was noticed to have a positive influence on hydrophobic sizing and paper defects. The surfaces of the white water tanks and the operation of pumps were assessed based on the density variations of the suspension. The temperature in the white water silo was stated to have a significant influence on the air content measured in the first centrifugal cleaning stage.
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Diplomityön tavoitteena oli selvittää Loviisan ydinvoimalaitoksen höyryturbiinin suoritus-kyvyn mittaamiseen käytettävissä olevia menetelmiä ja mittausjärjestelmiä. Tavoitteena oli selvittää mitkä tekijät aiheuttavat mittauksiin mittausvirheitä ja tutkia turbiineiden nykyisten mittalaitteiden epävarmuudet. Tässä diplomityössä selvitettiin millaisia standardinmukaisia testejä sekä muita varteenotettavia testejä turbiinin suorituskyvyn määrittämiseen on käytetty ja millaisia mittauksia ne vaativat. Lisäksi tutkittiin eri lähteistä millaisia mittalaitteita ja mittausjärjestelmiä voidaan käyttää turbiinin toiminnan mittauksiin. Soveltuvista mittausmenetelmistä esitettiin toimintaperiaatteet ja teoria. Kunnonvalvontaa varten esiteltiin värähtelyiden ja vääntö-momentin mittaamisen periaatteet. Epävarmuuksia arvioitiin mittalaitteiden teoreettisen epävarmuuden ja laitesijoittelun pohjalta. Työssä havaittiin, että suorituskyvyn arvioimiseksi on olemassa useita standardeja, mutta niiden mukaisiin mittauksiin tarvittaisiin nykyistä enemmän mittaustuloksia. Tarkkoja sekä luotettavia mittaustuloksia on haasteellista saada kaksifaasivirtauksesta. Mittalaitevalinnoilla ja mittalaitteiden määrää lisäämällä voidaan mittausten epävarmuutta pienentää. Loviisan ydinvoimalaitokselle ehdotettiin muutamia mittausjärjestelmiä turbiinin suoritus-kyvyn määrittämiseksi. Erityisesti turbiinin sisäiset olosuhteet tulisi määrittää nykyistä tarkemmin. Vääntömomentin mittaaminen olisi hyvä kunnonvalvonnan työkalu.
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Diplomityön tavoitteena oli kehittää mahdollisimman hyvä koordinaattiohjaus. Sen tuli olla jälkiasennettavissa perinteisen ohjauksen rinnalle työkoneisiin, joissa on käytetty sähköohjattuja proportionaaliventtiileitä. Työssä keskityttiin tutkimaan suuntaventtiilin yli vallitsevasta paine-erosta saatavan tilavuusvirtatiedon hyödyntämistä ohjauksessa. Työn ensimmäisessä vaiheessa koordinaattiohjaus toteutettiin käyttäen 0-peittoisilla karoilla ja karan asematakaisinkytkennällä varustettuja suuntaventtiileitä. Hydrauliseen kuristukseen perustuen saatiin paine-erosta käyttökelpoista tilavuusvirtasignaalia ja koordinaattiohjauksen liikeradan seurannassa oli parhaimmillaan vain 3 cm:n virhe koenosturin työliikkeen pituudella. Toisessa vaiheessa käytettiin työkoneissa yleisesti esiintyvää positiivisin karapeitoin varustettua mobiiliventtiilistöä, jossa oli karakohtaiset painekompensaattorit. Painekompensaattoreiden takia ei paine-eron mittaaminen puhtaasti suuntaventtiilin karan yli ollut mahdollista, jonka takia tyydyttiin koordinaattiohjaus toteuttamaan ilman paineen mittausta luottaen painekompensaattoreiden toimintaan. Käytetyn venttiilistön kavitoinninestotoiminnon huomiointi ohjauksessa jäi ratkaisematta ja se ohitettiin vastusvastaventtiileiden avulla. Koordinaattiohjauksen tarkkuus mobiiliventtiileillä oli vaatimaton ja tulosten toistettavuus heikko. Tulosten perusteella todettiin avoimellakin koordinaattiohjauksella olevan mahdollista saavuttaa lupaava tarkkuus ammattikuljettajiin verrattuna. Mobiiliventtiilistöön liittyvät, työn aikana esiinnousseet epäkohdat olisi ratkaistava ennen käytettyjen menetelmien soveltamista käytännön kohteisiin.
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The objective of this master’s thesis was to design and simulate a wind powered hydraulic heating system that can operate independently in remote places where the use of electricity is not possible. Components for the system were to be selected in such a way that the conditions for manufacture, use and economic viability are the as good as possible. Savonius rotor was chosen for wind turbine, due to its low cut in speed and robust design. Savonius rotor produces kinetic energy in wide wind speed range and it can withstand high wind gusts. Radial piston pump was chosen for the flow source of the hydraulic heater. Pump type was selected due to its characteristics in low rotation speeds and high efficiency. Volume flow from the pump is passed through the throttle orifice. Pressure drop over the orifice causes the hydraulic oil to heat up and, thus, creating thermal energy. Thermal energy in the oil is led to radiator where it conducts heat to the environment. The hydraulic heating system was simulated. For this purpose a mathematical models of chosen components were created. In simulation wind data gathered by Finnish meteorological institute for 167 hours was used as input. The highest produced power was achieved by changing the orifice diameter so that the rotor tip speed ratio follows the power curve. This is not possible to achieve without using electricity. Thus, for the orifice diameter only one, the optimal value was defined. Results from the simulation were compared with investment calculations. Different parameters effecting the investment profitability were altered in sensitivity analyses in order to define the points of investment profitability. Investment was found to be profitable only with high average wind speeds.
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It is common knowledge of the world’s dependency on fossil fuel for energy, its unsustainability on the long run and the changing trend towards renewable energy as an alternative energy source. This aims to cut down greenhouse gas emission and its impact on the rate of ecological and climatic change. Quite remarkably, wind energy has been one of many focus areas of renewable energy sources and has attracted lots of investment and technological advancement. The objective of this research is to explore wind energy and its application in household heating. This research aims at applying experimental approach in real time to study and verify a virtually simulated wind powered hydraulic house heating system. The hardware components comprise of an integrated hydraulic pump, flow control valve, hydraulic fluid and other hydraulic components. The system design and control applies hardware in-the-loop (HIL) simulation setup. Output signal from the semi-empirical turbine modelling controls the integrated motor to generate flow. Throttling the volume flow creates pressure drop across the valve and subsequently thermal power in the system to be outputted using a heat exchanger. Maximum thermal power is achieved by regulating valve orifice to achieve optimum system parameter. Savonius rotor is preferred for its low inertia, high starting torque and ease of design and maintenance characteristics, but lags in power efficiency. A prototype turbine design is used; with power output in range of practical Savonius turbine. The physical mechanism of the prototype turbine’s augmentation design is not known and will not be a focus in this study.