This diploma thesis deals with the control calculation of fluid biomass boilers with circulating fluidized bed. The introduction briefly introduced fluidized bed boilers and explained what biomass is. Furthermore there is a stoichiometric calculation of combustion. The calculation of the losses and the efficiency of the boiler is following. Desulphurization is calculated briefly. The main part is devoted to the design and calculation of individual heat exchanging surfaces: superheater P1, superheaters 2 and 3, the wall superheater, the return chamber, hanging tubes, economizer and air heater. At the end is calculated total tolerance boiler. Work is completed with a diagram of temperature of working media and combustion.

Aim of this thesis is to design a technology of a flue gas desulphurization of fluidized bed boiler. Currently, the state of technology is not able to provide flue gas desulphurisation to required level. For this reason it is necessary to build additional device for the desulphurisation. Theoretical part of the thesis deals with the emission limits of sulphur dioxide, available methods of desulphurization and sorbents suitable for the desulfurization. In practical part conditioned dry sorption method is chosen for the specified source, technological and structural design for suggested desulphurization technology including design of all device is proposed. The thesis also includes a technology design and a 3D model.

Due to the continuous growth of energy consumption it is required that development in the energy sector is focused on renewable energy sources. Another possibility how to reduce the consumption of primary energy resources is also searching for new and non-traditional fuels. The biomass is the best and potentially expandable renewable energy source in geographic conditions in the Czech Republic. The energy usage of biomass has experienced a significant increase in recent years, however, even in the big energy power plant. This increase in consumption made mainly from wood biomass a shortage fuel, and it began to raise its price. The consumers of biomass fuel are starting to look for a different type of fuel at this time. Stalk and slightly contaminated biomass are representatives of these non-traditional fuels. Stalks are mostly annual plants grown primarily for subsistence. Waste parts of these plants can be utilized for production of energy. The characteristic temperatures of stalk ash have relatively low values. Sintering of ash in a device is one of the obstacles for energy usage of stalk. Sintering of ash brings a number of operational problems at power facilities. Therefore, the part of a research is dedicated to the melting of ash. The thermal gasification is one of the possibilities how to use biomass efficiently. Gasification can be understood as the thermo-chemical conversion of solid fuel into a different state, in this case the gaseous state. The combustion process is generally more manageable for gaseous fuels. Due to this process ower emissions of undesirable compounds at the output of the combustion device can be achieved. Thermal gasification process takes place under stochiometric access of oxidant. The gas with low heating value is on the outlet from gasification process. The main components of produced gas are hydrogen, carbon monoxide and methane. The final gas contains also a lot of undesirable constituents, which make this gas disadvantaged in energy. These constituents are neutral components that dilute gas only, and pollutants as dust, tar and compounds of sulfur and chlorine. These pollutants complicate further use of the generated gas. The tar compounds together with dust causing build-up on the conveyor pipe and also on the combustion equipment, which are using this generated gas. The quality of produced gas is increases by another reprocessing and cleaning. The purified gas can be used for cogeneration of energy and burn it in internal combustion engines or gas turbines. Other possibility is typical usage for heating according to the needs of technology. The atmospheric fluidized bed gasification reactor Biofluid 100th was built for experimental purposes in the laboratories of the Energy Institute. The thesis is focused on thermal gasification of stalk and other non-traditional fuels in Biofluid device. The aim is to achieve a stable gasification process of stalk and thereby verify the possibility of stalk use as fuel for technology Biofluid. Subsequent aim is design of methods for cleaning the raw gas from the tar compounds. The research is focused on the secondary gas cleaning methods due to the requirements of high purity of the resulting gas.

The multi zone fluidized bed reactor instantaneously creates several chemical/physical environments in a single reactor vessel. Effective solid circulation across zones can be achieved by tuning the reactor geometries, solid properties, and operating conditions. However, there is limited research for this innovative reactor concept beyond the laboratory scale, among which a better understanding of the complex fluid dynamics, dominating the solid circulation in different zones, is a basis. This work aims to propose a new method to capture the fluid dynamics of a pilot MZFBR by laboratory measurements with validation from theoretical analysis and simulation. Toward this goal, we first performed particle characterizations, and fluidization testing experiments in a laboratory scale fluidized bed reactor and a pilot scale multi zone fluidized bed reactor at ambient conditions to study the development of fluidization regimes. Then we compared the minimum fluidization velocity with argon and air between the experimental measurements and theoretical calculation results and proposed a modified Ergun equation, which better fits our system. Finally, we conducted computational particle fluid dynamics simulations for the pilot multi zone fluidized bed reactor with the Ergun equation and our modified equation and compared the results against previous experimental observations. Simulations display that the prediction of pressure drop in the pilot scale multi zone fluidized bed reactor with the proposed Ergun equation is similar to that of the original equation, with a relative deviation of around 3%. However, the modified equation captured the bubbling fluidization behavior as the experiment, while the Ergun equation predicted a smooth fluidization without any bubbles. The better agreements validated both our workflow of estimating the fluidization behavior in a pilot multi zone fluidized bed reactor from laboratory measurements and the simulation strategy.

The objective of this study is to investigate the eect of dierent fuels on two uidized bed boiler systemsat the energy company Soderenergi's site in Igelsta, called IKV and IGV P3. Today, recovered wastewood (RWW) is the major fuel share fed into the boilers. However, with an insecure fuel supply in thefuture, other fuel types must be considered. Based on knowledge from previous fuel usage in the boilers,an evaluation of how other potential fuel mixtures may eect the operation is conducted. The additionalfuels considered in the fuel blends are; stem wood chips, cutter shavings, solid recycled fuel (SRF) andrubber.With elemental analysis of the fuels and established key numbers, the previous fuel mixtures are evaluated.The indications by the guiding parameters are compared with experienced problems and the formercondition of the boilers, and the risk limits for the key numbers are adjusted to a suitable level. Thepotential mixtures are evaluated with the key numbers and the updated limits. In addition to the keynumbers, the heavy metal concentration, the heating value, the moisture content and the ash content ofthe fuel blends are included in the evaluation. The considered damages in the boilers caused by the fuelblends are corrosion, sintering and fouling.The damage level from the current fuel usage for IKV and IGV P3 is fairly low. The results from theanalyzed fuel mixtures show an increased damage risk in the boilers. Additionally, adjustments of theboiler systems are required by some of the analyzed fuel mixtures. In general, the corrosion risk andthe heavy metal content will increase in comparison with today's fuel. The fouling and slagging are aswell expected to increase for the assessed fuel mixtures. Moreover, the result illustrates an increased ashgeneration, which demands a reconstruction of the ash cooling system for IKV. Furthermore, the increaseof LHV in the assessed fuel mixtures to IGV P3, is likely to require an increased capacity of the ue gasrecirculation pump.In the analysis of the potential fuel mixtures it is found that the corrosion risk expressed by the keynumbers is reduced with a higher share of rubber. The heavy metal content is, however, increased,leading to e.g. an enhanced risk for formation of eutectic salts, which as well are corrosive. On thecontrary, the fuel mixtures with a high risk expressed by the key numbers, have the lowest concentrationsof heavy metals. Due to the results are con icting, a balance between the risk indicated by the keynumbers and the heavy metal concentration must be considered in the evaluation. The fuel mixturesconsidered causing least damage to IKV are a mixture of 42% RWW, 48% wood fuel and 15% SRF, and amixture of 70% wood fuel, 20% SRF and 10% rubber. The fuel mixtures considered causing least damageto IGV P3 are a mixture of 85% RWW and 15% rubber and a mixture of 70% RWW and 30% SRF. / Syftet med studien var att undersoka branslets paverkan pa tva uidbaddpannor, IKV och IGV P3, hos energiforetaget Soderenergi. Idag ar det huvudsakliga branslet i dessa pannor returtra (RT). Med en standigtrorlig branslemarknad kravs kunskap av alternativa branslen. Baserat pa tidigare bransleanvandning,har paverkan fran potentiella bransleblandningar pa pannan undersokts. Utover returtra ar stamveds is,span, papper-plast-tra (SRF) och gummi med i de analyserade blandningarna.Med elementaranalyser pa branslen och etablerade nyckeltal utvarderades de tidigare anvanda branslena.Indikationen fran nyckeltalen ar jamford med upplevda problem och risknivaerna for nyckeltalen arandrade till passande nivaer. De framtida bransleblandningarna analyserades med hjalp av nyckeltalenoch de uppdaterade risknivaerna. Utover nyckeltalen analyserades tungmetallhalten, varmevardet, fukthaltenoch askhalten i bransleblandningarna. De pannskador orsakade av bransleblandningarna somundersokts ar korrosion, sintring och paslag.Det nuvarande branslet till IKV och IGV P3 ger en relativt lag skadeniva. Resultaten fran de analyseradebransleblandningarna visar att skaderisken i pannorna kommer att oka och forandringar av pannan kankomma att kravas. Generellt kommer korrosionsrisken och tungmetallinnehallet att oka i jamforelse meddagens bransle. Okat paslag och slaggning ar ocksa forvantat. Vidare visar resultatet att askproduktionenkommer att oka, vilket gor att IKVs kylsystem for bottenaskan kommer behovas byggas ut. LHV for deanalyserade bransleblandningarna for IGV P3 okar, vilket innebar att kapaciteten for returgas aktarnatroligen maste okas.I jamforelsen av de olika bransleblandningarna visas att korrosionsrisken, forutspadd av nyckeltalen,minskar med en hogre andel gummi. Daremot okar tungmetallinnehallet, vilket leder till en okad riskfor bildning av eutektiska salter, vilka ocksa ar korrosiva. Bransleblandningarna med en indikerad hogrisk av nyckeltalen, har tvartemot den lagsta koncentrationen av tungmetaller. Eftersom resultatenar motsagande, kravs en avvagning mellan riskerna indikerade av nyckeltalen och tungmetallshalten.De bransleblandningar som ar ansedda att vara minst skadliga for IKV ar en blandning av 42% RT,48% tradbransle och 15% SRF, och en blandning av 70% tradbransle, 20% SRF och 10% gummi. Debransleblandning som ar ansedda att vara minst skadliga for IGV P3 ar en blandning av 85% RT och15% gummi, och en blandning av 70% RT och 30% SRF.

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Fluidized beds have widespread industrial applications ranging from chemical industries to power plants. The flow inside a fluidized bed system consists of two main phases, a particle phase and the fluid phase. The two phases are strongly coupled to each other through various forces like drag and pressure. Capturing this multiphase phenomenon requires modeling strategies that possess good fidelity over a range of scales. Discrete Element Modeling (DEM) coupled with Computational Fluid Dynamics (CFD) provides a good platform to analyze the complex coupled multiphase hydrodynamics inside fluidized bed systems. Conventional DEM-CFD framework suffers from contradictory spatial resolution requirements for the particle and fluid phases, respectively. This prevents the conventional DEM-CFD method to be applied to geometries that have features comparable to the particle diameter of the solid phase. The novelty of this work lies in the development and validation of a two-grid formulation that removes the resolution restrictions of the conventional DEM-CFD framework. The results obtained from this new framework agree reasonably well with the experiments showing the capability of the new scheme to simulate conditions not possible with conventional DEM-CFD framework. In addition, this research also focuses on performing both 2D and 3D jetting fluidized bed simulations having millions of particles; validate/compare results with experiments and to perform heat transfer studies in a jetting fluidized bed system. The results suggest convective and diffusive mixing for a single jet at higher superficial velocity to be better than the mixing obtained in a multiple jet framework. The comparison with experimental results obtained in a multiple jetting setup shows that a 2D simulation captures the essential jet characteristics near the distributor plate reasonably well while a 3D simulation is needed to capture proper bubble dynamics near the freeboard of the bed. These results give insight into the detailed dynamics of fluidized bed systems and provide a foundation for a better design of these systems. / Ph. D.