Biokaasun syöttö maakasuverkostoon

Biokaasua syntyy mm. kaatopaikoilla, jätevedenpuhdistamoilla ja biokaasureaktoreissa, kun bakteerit hajottavat orgaanista ainesta hapettomissa olosuhteissa. Biokaasun tärkein ainesosa on metaani, jota biokaasussa on tyypillisesti hieman yli puolet. Muu osa biokaasusta on pääosin hiilidioksidia, mutta se sisältää myös paljon erilaisia epäpuhtauksia, jotka vaikeuttavat biokaasun hyötykäyttöä. Suomeen tuotava maakaasu puolestaan on lähes puhdasta metaania. Tämä diplomityö suoritettiin Gasum Oy:lle ja sen tarkoituksena oli tutkia millaisia toimenpiteitä vaaditaan, jotta biokaasua voidaan syöttää Suomen maakaasuverkostoon. Työssä suoritettiin katsaus biokaasun puhdistus- ja jalostusmenetelmiin, joilla biokaasun sisältämät epäpuhtaudet poistetaan ja metaanipitoisuus nostetaan lähes maakaasun tasolle hiilidioksidia poistamalla. Lisäksi työssä simuloitiin biokaasun syöttöä maakaasuverkostoon eri koostumuksin ja maakaasuverkoston eri osista näin syntyvän seoskaasun ominaisuuksien määrittämiseksi simulointiohjelma Simonen avulla. Työssä myös etsittiin parasta keinoa jäljittää maakaasuverkoston kaasun laatua ja hallita energiatasetta, kun kaasun laatu ei enää ole kaikkialla sama. Lisäksi suoritettiin lyhyt katsaus biokaasusyötön vaikutuksista päästökauppaan ja maakaasuverkoston järjestelmävastaavan tehtävään. Työssä tultiin siihen tulokseen, että biokaasun syöttö maakaasuverkostoon on mahdollista vain, kun biokaasu puhdistetaan ja jalostetaan. Tällöin biokaasun ja maakaasun seos täyttää maakaasuverkoston kaasulle asetetut laatukriteerit, vaikka yksin biokaasu ei sitä tee. Parhaaksi keinoksi hallita maakaasun ja biokaasun laatua todettiin kaasukromatografien käyttö.

CFD Simulation of Two-phase and Three-phase Flows in Internal-loop Airlift

Airlift reactors are pneumatically agitated reactors that have been widely used in chemical, petrochemical, and bioprocess industries, such as fermentation and wastewater treatment. Computational Fluid Dynamics (CFD) has become more popular approach for design, scale-up and performance evaluation of such reactors. In the present work numerical simulations for internal-loop airlift reactors were performed using the transient Eulerian model with CFD package, ANSYS Fluent 12.1. The turbulence in the liquid phase is described using κ- ε the model. Global hydrodynamic parameters like gas holdup, gas velocity and liquid velocity have been investigated for a range of superficial gas velocities, both with 2D and 3D simulations. Moreover, the study of geometry and scale influence on the reactor have been considered. The results suggest that both, geometry and scale have significant effects on the hydrodynamic parameters, which may have substantial effects on the reactor performance. Grid refinement and time-step size effect have been discussed. Numerical calculations with gas-liquid-solid three-phase flow system have been carried out to investigate the effect of solid loading, solid particle size and solid density on the hydrodynamic characteristics of internal loop airlift reactor with different superficial gas velocities. It was observed that averaged gas holdup is significantly decreased with increasing slurry concentration. Simulations show that the riser gas holdup decreases with increase in solid particle diameter. In addition, it was found that the averaged solid holdup increases in the riser section with the increase of solid density. These produced results reveal that CFD have excellent potential to simulate two-phase and three-phase flow system.

Doubly fed wind turbine performance in variable grid conditions

Wind turbines based on doubly fed induction generators (DFIG) become the most popular solution in high power wind generation industry. While this topology provides great performance with the reduced power rating of power converter, it has more complicated structure in comparison with full-rated topologies, and therefore leads to complexity of control algorithms and electromechanical processes in the system. The purpose of presented study is to present a proper vector control scheme for the DFIG and overall control for the WT to investigate its behavior at different wind speeds and in different grid voltage conditions: voltage sags, magnitude and frequency variations. The key principles of variable-speed wind turbine were implemented in simulation model and demonstrated during the study. Then, based on developed control scheme and mathematical model, the set of simulation is made to analyze reactive power capabilities of the DFIG wind turbine. Further, the rating of rotor-side converter is modified to not only generate active rated active power, but also to fulfill Grid Codes. Results of modelling and analyzing of the DFIG WT behavior under different speeds and different voltage conditions are presented in the work.

A game theoretic simulation model for quality oriented timber supply to sawmills

Summary

Comparison of thinning methods in a Scots pine stand on drained peatland : a simulation study

Tiivistelmä: Harvennusmenetelmien vertailu ojitetun turvemaan männikössä. Simulointitutkimus

Comparing simulation methods for modelling the errors of stand inventory data

Abstract

Simulation of spring wheat responses to elevated CO‚́‚ and temperature by using CERES-wheat crop model

Selostus: Kohotettujen CO‚́‚:n ja lämpötilan vaikutukset kevätvehnän fenologiseen kehitykseen ja sadontuottomahdollisuuksiin

Computational and Experimental Analysis of Flow Field in the Diffusers of Centrifugal Compressors

Centrifugal compressors are widely used for example in process industry, oil and gas industry, in small gas turbines and turbochargers. In order to achieve lower consumption of energy and operation costs the efficiency of the compressor needs to be improve. In the present work different pinches and low solidity vaned diffusers were utilized in order to improve the efficiency of a medium size centrifugal compressor. In this study, pinch means the decrement of the diffuser flow passage height. First different geometries were analyzed using computational fluid dynamics. The flow solver Finflo was used to solve the flow field. Finflo is a Navier-Stokes solver. The solver is capable to solve compressible, incompressible, steady and unsteady flow fields. Chien's k-e turbulence model was used. One of the numerically investigated pinched diffuser and one low solidity vaned diffuser were studied experimentally. The overall performance of the compressor and the static pressure distribution before and after the diffuser were measured. The flow entering and leaving the diffuser was measured using a three-hole Cobra-probe and Kiel-probes. The pinch and the low solidity vaned diffuser increased the efficiency of the compressor. Highest isentropic efficiency increment obtained was 3\% of the design isentropic efficiency of the original geometry. It was noticed in the numerical results that the pinch made to the hub and the shroud wall was most beneficial to the operation of the compressor. Also the pinch made to the hub was better than the pinchmade to the shroud. The pinch did not affect the operation range of the compressor, but the low solidity vaned diffuser slightly decreased the operation range.The unsteady phenomena in the vaneless diffuser were studied experimentally andnumerically. The unsteady static pressure was measured at the diffuser inlet and outlet, and time-accurate numerical simulation was conducted. The unsteady static pressure showed that most of the pressure variations lay at the passing frequency of every second blade. The pressure variations did not vanish in the diffuser and were visible at the diffuser outlet. However, the amplitude of the pressure variations decreased in the diffuser. The time-accurate calculations showed quite a good agreement with the measured data. Agreement was very good at the design operation point, even though the computational grid was not dense enough inthe volute and in the exit cone. The time-accurate calculation over-predicted the amplitude of the pressure variations at high flow.