Radiative Heat Transfer in Boiler Furnaces

Better models are needed for radiative heat transfer in boiler furnaces. If the process is known better, combustion in the furnace can be optimized to produce low emissions. It makes the process to be environmental friendly. Furthermore, if there is a better model of the furnace it can more fully explain what is happening inside the furnace. Using of the model one can quickly and easily analyze how it operates with bio fuels, moist fuels or difficult fuels and improve the operation. Models helps with better estimation of furnace dimensions and result in more accurate understanding of operation. Key component lacking in these models is radiative heat transfer in particle laden gases. If there are no particles than radiative heat transfer can be calculated approximately. There are two problems with current models when used with flow modeling. The first one is a need to account for a particle laden gas and the second one is an absence of a fast algorithm. Fast calculation is needed if radiative heat transfer calculation is done for a large CDF model. Computations slow down if time is required for calculating radiative properties over and over again. This thesis presents a band model for radiative heat transfer in boiler furnaces. Advantage is a quickness of calculation and account of particles in the process.

Metsäpolttoaineiden vesitiekuljetus proomukalustolla

Metsäpolttoaineiden käyttö kasvaa lämpö- ja voimalaitoksissa ja mahdollisissa biojalostamoissa. Metsäpolttoaineilla voidaan saavuttaa päästövähennyksiä korvaamalla päästöintensiivisempiä polttoaineita. Metsäpolttoaineen kysynnän kasvu suurkäyttöpaikoilla luo uusia vaatimuksia metsäbiomassan hankintaan. Metsäpolttoaineiden vesitiekuljetuksen sisältämiä logistiikkajärjestelmiä kehittämällä toimitusvarmuutta pystytään parantamaan ja hankintaa laajentamaan kustannustehokkaasti ja ympäristöystävällisesti. Kuljetuskokeilut antoivat uutta tietoa vesitiekuljetuksen sisältämästä hankinnasta. Lastikapasiteetti nykyisen kaltaisessa Eurooppa IIa -suurproomussa vaihtelee 1200 tonnista jopa 1800 tonniin (kosteus 40 %) riippuen tiivistymisestä ja proomun modifiointiasteesta. Metsähakkeen energiatiheys oli suurproomukuljetuksissa keskimäärin 1 MWh/i-m3, joka oli 25 % parempi kuin vertailun hakerekkakuljetuksissa. Vesitiekuljetuksen kustannukset olivat kuljetuskokeiluissa lastauksineen ja purkuineen 0,02 €/MWh/km, ollen noin 20 % ketjun kokonaiskustannuksista. Simuloinnin edullisimpien vesitiekuljetusvaihtoehtojen vaihteluvälin kustannukset olivat vastaavasti 0,013 - 0,026 €/MWh/km. Lastauksen ja purun kustannus oli 0,4 - 0,6 €/MWh ja vesitiekuljetus 0,9 - 2,0 €/MWh (100 km). Ketjun kokonaiskustannukset hakkuutähdehakkeelle vaihtelivat simuloinnin edullisimpien vaihtoehtojen perusteella välillä 10,8 - 12,1 €/MWh (30 km rekka, 100 km proomu). Kuljetusketjujen simuloinnin kustannukset osoittivat proomukuljetusketjun olevan kilpailukykyinen vaihtoehto hakerekkakuljetusketjulle kalustosta ja vuosittaisista käyttötunneista riippuen kuljetusetäisyyden ylittäessä 100 km. Kustannustehokkain ratkaisu vesitiekuljetuksessa saavutettiin pienen aluksen ja suuren kokoluokan proomuyksikön kytkyeellä. Haketus kannattaa toteuttaa ennen proomukuljetuksen osuutta metsähakkeen paremman tiiviyden ja käsiteltävyyden perusteella. Logistiikkajärjestelmiä pitää kehittää tapauskohtaisesti käyttöpaikan tarpeet ja olosuhteet huomioon ottaen. Metsäpolttoaineiden vesitiekuljetuksen sisältämän logistiikan liiketoimintamallien vertailussa arvioitiin vaihtoehtoiset ulkoistetut toimintamallit paremmaksi kuin nykyinen urakointimalli. Tämä mahdollistaa paremman metsähakkeen saatavuuden ja logistiikan tehokkuuden lastausterminaaleissa. Terminaalitoiminnot ja proomukuljetukset lisäävät uusia liiketoimintamahdollisuuksia ja mahdollistavat metsäpolttoaineiden

Coolant Flow and Heat Transfer in Pebble-Bed Reactor Core

This thesis gathers knowledge about ongoing high-temperature reactor projects around the world. Methods for calculating coolant flow and heat transfer inside a pebble-bed reactor core are also developed. The thesis begins with the introduction of high-temperature reactors including the current state of the technology. Process heat applications that could use the heat from a high-temperature reactor are also introduced. A suitable reactor design with data available in literature is selected for the calculation part of the thesis. Commercial computational fluid dynamics software Fluent is used for the calculations. The pebble-bed is approximated as a packed-bed, which causes sink terms to the momentum equations of the gas flowing through it. A position dependent value is used for the packing fraction. Two different models are used to calculate heat transfer. First a local thermal equilibrium is assumed between the gas and solid phases and a single energy equation is used. In the second approach, separate energy equations are used for the phases. Information about steady state flow behavior, pressure loss, and temperature distribution in the core is obtained as results of the calculations. The effect of inlet mass flow rate to pressure loss is also investigated. Data found in literature and the results correspond each other quite well, considered the amount of simplifications in the calculations. The models developed in this thesis can be used to solve coolant flow and heat transfer in a pebble-bed reactor, although additional development and model validation is needed for better accuracy and reliability.

Statistical Optimum Design of Heat Exchangers

The optimal design of a heat exchanger system is based on given model parameters together with given standard ranges for machine design variables. The goals set for minimizing the Life Cycle Cost (LCC) function which represents the price of the saved energy, for maximizing the momentary heat recovery output with given constraints satisfied and taking into account the uncertainty in the models were successfully done. Nondominated Sorting Genetic Algorithm II (NSGA-II) for the design optimization of a system is presented and implemented inMatlab environment. Markov ChainMonte Carlo (MCMC) methods are also used to take into account the uncertainty in themodels. Results show that the price of saved energy can be optimized. A wet heat exchanger is found to be more efficient and beneficial than a dry heat exchanger even though its construction is expensive (160 EUR/m2) compared to the construction of a dry heat exchanger (50 EUR/m2). It has been found that the longer lifetime weights higher CAPEX and lower OPEX and vice versa, and the effect of the uncertainty in the models has been identified in a simplified case of minimizing the area of a dry heat exchanger.

Pientalojen ilmalämpöpumput sähköverkossa

Työssä tutkitaan ilmalämpöpumppujen kokonaisvaltaista vaikutusta sähköverkkoon. Tarkastelu aloitetaan lämpöpumppujen toiminnasta ja rakenteesta, josta jatketaan laitteen käytettävyyteen ja muiden lämmitysmenetelmien vertailuun. Sähköisten ominaisuuksien tarkastelussa pohditaan ilmalämpöpumppujen vaikutusta suomalaiseen sähköverkkoon muun muassa yleissähkötekniikan, taloudellisuuden ja energiatehokkuuden sekä häiriöiden kannalta. Tämä tutkielma rajoittuu pientaloihin, ja niihin asennettuihin ilma-ilmalämpöpumppuihin. Työn loppupäätelmänä on, että ilmalämpöpumppujen käytöstä ei juuri aiheudu vaikutuksia suomalaiseen sähköverkkoon. Suurimmat ilmalämpöpumppujen käytöstä syntyvät seuraukset kohdistuvat sähköverkkoyhtiöihin, joihin ilmalämpöpumput aiheuttavat taloudellisia menetyksiä. Suuret ja tulevaisuudessa kasvavat ilmalämpöpumppumäärät aiheuttavat sähköntuotantoon lisätehontarvetta huippukuorman aikaan. Toisaalta välitehoalueella tehontarve sekä energiankulutus pienenevät. Sähköverkoissa ei ole toistaiseksi havaittu ilmalämpöpumpuista johtuvia häiriöitä.

Wood pellet markets in Russia

Bioenergy came to Russia through wood pellets. On account of prevalence of oil and gas in the Russian economy «bioenergy» has come with a great delay. Certainly, there were many woodworking enterprises and even municipal boiler-houses using wood waste and fire wood for energy reception, but this activity was not purposeful. More likely it was connected with necessity of waste recycling and with the organization of heat supply in the remote areas of the country. However, in 2001 was founded the first pellet plant in Russia. The purpose of this work was to analyze wood pellets market in Russia, investigate current situation on the home and export market, evaluates supply and demand development, opportunities for wood pellets manufactures in Russia, the main manufactures in Russian market; cost and prices for wood pellets in Russia. Also the work was intended to give better understanding of the main problems of wood pellets industry in Russia. Besides, this work had updated information about Russian customs and logistic systems.

Heat Transfer in Plate Heat Exchangers

This study illustrates the different types of plate heat exchangers that are commonly used in various domestic and industrial applications. The main purpose of this paper was to devise a methodology that is capable of calculating optimum number of plates in the design of a plate heat exchanger. To obtain the appropriate number of plates, typically several iterations must be made before a final acceptable design is completed, since plate amount depends on many factors such as, flow velocities, physical properties of the streams, flow channel geometry, allowable pressure drop, plate dimensions, and the gap between the plates. The methodology presented here can be used as a general guide for designing a plate heat exchanger. To investigate the effects of relevant parameters on the thermal-hydraulic design of a plate heat exchanger, several experiments were carried out for single-phase and counter flow arrangement with two brazed plate heat exchangers by varying the flow rates and the inlet temperatures of the fluid streams. The actual heat transfer coefficients obtained based on the experiment were nearly close to the calculated values and to improve the design, a correction factor was introduced. Besides, the effect of flow channel velocity on the pressure drop inside the unit is presented.

Heat transfer in superheaters of the bubbling fluidized bed boiler conversions

It is often reasonable to convert old boiler to bubbling fluidized bed boiler instead of building a new one. Converted boiler consists of old and new heat surfaces which must be fitted to operate together. Prediction of heat transfer in not so ideal conditions sets challenges for designers. Two converted boilers situated in Poland were studied on the grounds of acceptance tests and further studies. Calculation of boiler process was performed with boiler design program. Main interest was heat transfer in superheaters and factors affecting it. Theory for heat transfer is presented according to information found from literature. Results obtained from experimental studies and calculations have been compared. With correct definitions calculated parameters corresponded well to measured data at boiler maximum design load. However overload situations revealed to be difficult to model at least without considering changes in the combustion process which requires readjustments to the design program input values.

Removal of chromium (vi) in aqueous environments using cork and heat-treated cork samples from quercus cerris and quercus suber

Chromium (VI) removal and its reduction to chromium (III) from aqueous solution by untreated and heat-treated Quercus cerris and heat-treated Quercus suber black agglomerate cork granules was investigated. Initial screening studies revealed that among the sorbents tested, untreated Q. cerris and Q. suber black agglomerate are the most efficient in the removal of Cr(VI) ions and were selected for adsorption essays. Heat treatment adversely affected chromium adsorption and chromium (VI) reduction in Q. cerris cork. The highest metal uptake was found at pH 3.0 for Q. cerris and pH 2.0 for black agglomerate. The experimental data fitted the Langmuir model and the calculated qmax was 22.98 mg/g in black agglomerate and 21.69 mg/g in untreated Q. cerris cork. The FTIR results indicated that while in black agglomerate, lignin is the sole component responsible for Cr(VI) sorption, and in untreated Q. cerris cork, suberin and polysaccharides also play a significant role on the sorption. The SEM-EDX results imply that chromium has a homogenous distribution within both cork granules. Also, phloemic residues in Q. cerris granules showed higher chromium concentration. The results obtained in this study show that untreated Q. cerris and black agglomerate cork granules can be an effective and economical alternative to more costly materials for the treatment of liquid wastes containing chromium

A three dimensional study of heat transfer in a supercritical circulating fluidized bed combustor

From the boiler design point of view, it is imperative to know and understand the operation of the boiler. Since comprehensive measurement of a large furnace is impossible, the furnace can be modeled in order to study its behavior and phenomena. This requires the used model to be validated to correspond with the physical furnace behavior. In this thesis, a three dimensional furnace model is validated to match a bituminous coal utilizing, supercritical once-through circulating fluidized bed combustor based on measurement data. The validated model is used for analyzing the furnace heat transfer. Other heat transfer analysis methods are energy balance method based on tube surface temperature measurements and a method based on measured temperature difference between the tube crest and the fin. The latter method was developed in the thesis using Fluent-software. In the theory part, literature is reviewed and the fundamental aspects of circulating fluidized bed are discussed. These aspects are solid particle behavior in fluidization known as hydrodynamics, behavior of fuel and combustion and heat transfer. Fundamental aspects of modeling are also presented.

Statistical Analysis and Numerics of Heat Exchanger Models

The identifiability of the parameters of a heat exchanger model without phase change was studied in this Master’s thesis using synthetically made data. A fast, two-step Markov chain Monte Carlo method (MCMC) was tested with a couple of case studies and a heat exchanger model. The two-step MCMC-method worked well and decreased the computation time compared to the traditional MCMC-method. The effect of measurement accuracy of certain control variables to the identifiability of parameters was also studied. The accuracy used did not seem to have a remarkable effect to the identifiability of parameters. The use of the posterior distribution of parameters in different heat exchanger geometries was studied. It would be computationally most efficient to use the same posterior distribution among different geometries in the optimisation of heat exchanger networks. According to the results, this was possible in the case when the frontal surface areas were the same among different geometries. In the other cases the same posterior distribution can be used for optimisation too, but that will give a wider predictive distribution as a result. For condensing surface heat exchangers the numerical stability of the simulation model was studied. As a result, a stable algorithm was developed.

Sellutehtaan sekundäärilämmön käytön tehostaminen

Energia on olennainen osa nykyaikaisen sellutehtaan prosesseja, joissa kuluu suuria määriä lämpöä ja sähköä. Pyrittäessä entistä kustannustehokkaampaan liiketoimintaan nousee energiatehokkuus usein mielenkiinnon kohteeksi. Pitkälle viety sähkön ja lämmön yhteistuotanto yhdistettynä korkeaan biopolttoaineiden osuuteen energian tuotannossa luovat pohjan tälle pyrkimykselle. Sekundäärilämpöä syntyy prosessien sivutuotteena ja sen mahdollisimman suuri hyödyntäminen on yksi keino päästä kohti parempaa energiatehokkuutta. Joissain tapauksissa sillä voidaan korvata jopa primäärienergian käyttöä ja mahdollisesti pienentää ostopolttoaineiden tarvetta. Diplomityössä tutkitaan sellutehtaan sekundäärilämpöjärjestelmän toimintaa, ohjausta ja energiankulutusta. Sekundäärilämpöjärjestelmästä muodostetaan taseet talvitilanteessa ja samalla etsitään mahdollisia uusia talteenotettavia sekundäärilämpövirtoja tai vastaavasti käyttökohteita. Lisäksi päivitetään sekundäärilämpöjärjestelmän raportoinnin ja ohjauksen työkaluja nykytilannetta vastaavaksi. Työn aikana kiinnitetään myös huomiota järjestelmän toimintaan muutostilanteissa, joissa kaikkia vesijakeita ei välttämättä ole saatavilla prosessin tarvitsemia määriä.

Moisture sorption isotherms and isosteric heat determination in Chilean papaya (Vasconcellea pubescens)

The moisture sorption isotherms of Chilean papaya were determined at 5, 20, and 45 ºC, over a relative humidity range of 10-95%. The GAB, BET, Oswin, Halsey, Henderson, Smith, Caurie and Iglesias-Chirife models were applied to the sorption experimental data. The goodness of fit of the mathematical models was statistically evaluated by means of the determination coefficient, mean relative percentage deviation, sum square error, root-mean-square error, and chi-square values. The GAB, Oswin and Halsey models were found to be the most suitable for the description of the sorption data. The sorption heats calculated using the Clausius-Clapeyron equation were 57.35 and 59.98 kJ·mol-1, for adsorption and desorption isotherms, respectively.

Improving demand forecasting practices in the industrial context

Demand forecasting is one of the fundamental managerial tasks. Most companies do not know their future demands, so they have to make plans based on demand forecasts. The literature offers many methods and approaches for producing forecasts. When selecting the forecasting approach, companies need to estimate the benefits provided by particular methods, as well as the resources that applying the methods call for. Former literature points out that even though many forecasting methods are available, selecting a suitable approach and implementing and managing it is a complex cross-functional matter. However, research that focuses on the managerial side of forecasting is relatively rare. This thesis explores the managerial problems that are involved when demand forecasting methods are applied in a context where a company produces products for other manufacturing companies. Industrial companies have some characteristics that differ from consumer companies, e.g. typically a lower number of customers and closer relationships with customers than in consumer companies. The research questions of this thesis are: 1. What kind of challenges are there in organizing an adequate forecasting process in the industrial context? 2. What kind of tools of analysis can be utilized to support the improvement of the forecasting process? The main methodological approach in this study is design science, where the main objective is to develop tentative solutions to real-life problems. The research data has been collected from two organizations. Managerial problems in organizing demand forecasting can be found in four interlinked areas: 1. defining the operational environment for forecasting, 2. defining the forecasting methods, 3. defining the organizational responsibilities, and 4. defining the forecasting performance measurement process. In all these areas, examples of managerial problems are described, and approaches for mitigating these problems are outlined.