The regular transmittance of light or similar radiation through a flowing suspension of particles fluctuates because of the random occurrence of particles in the beam.In the work presented here, a theory for this fluctuating behaviour with the emphasison dispersions of mm-length slender cylindrical particles having circular crosssections is given. The particles in question are wood pulp fibres, which as a first approximation are considered to have a cylinder shape. Four possible measurementprinciples are described theoretically and experimentally. The four principles are for the measurement of concentration, length distribution characterized as lengthclasses, mean length, and mean width. The usefulness in industrial process monitoring of two of these principles is exemplified with pulp measurements. In order to estimate model errors, numerical simulations were used. Although other techniques such as image analysis may compete, the technique presented here is attractive because of the simplicity of the measurement device used. / QC 20100806

Particle-laden turbulent flow through a straight square duct at Reτ = 300 is studied using direct numerical simulation (DNS) and Lagrangian particle tracking. A parallelized 3-D particle tracking direct numerical simulation code has been developed to perform the large-scale turbulent particle transport computations reported in this thesis. The DNS code is validated after demonstrating good agreement with the published DNS results for the same flow and Reynolds number. Lagrangian particle transport computations are carried out using a large ensemble of passive tracers and finite-inertia particles and the assumption of one-way fluid-particle coupling. Using four different types of initial particle distributions, Lagrangian particle dispersion, concentration and deposition are studied in the turbulent straight square duct. Particles are released in a uniform distribution on a cross-sectional plane at the duct inlet, released as particle pairs in the core region of the duct, distributed randomly in the domain or distributed uniformly in planes at certain heights above the walls. One- and two-particle dispersion statistics are computed and discussed for the low Reynolds number inhomogeneous turbulence present in a straight square duct. New detailed statistics on particle number concentration and deposition are also obtained and discussed.

Most companies that have any type of combustion or other pollution process via emission to air needs to measure their emissions to ensure they are within legal boundaries. Among the different types of pollution measurements, one of the most common is dust concentration, also known as particle concentration. An important factor in dust concentration measurements is to ensure that the concentration of the measured dust is representative to the dust concentration in the emissions. This is measured in isokinetic deviation, defined as (vn 􀀀 vd)=vd, where vn is the velocity in the entry nozzle and vd the velocity in the duct. Methods of dust concentration measurements used today are dependent on manual tuning and sensor readings, and the isokinetic deviation is calculated after a test. The focus of this project was therefore to investigate how the process of dust concentration measurements using standard reference methods could be automated in the way that isokinetic sampling is controlled and regulated by an automated control system in real time. Pressures, temperatures and sampled gas volume were quantized. A PIDcontroller was designed, implemented and tested. The PID-controller took the differential pressure between the inside of the entry nozzle and the duct, called zero pressure, as input. The system was tested in a laboratory environment by letting a radial fan create a flow, and thus create a zero pressure of -60 Pa, meaning that the pressure in the duct was 60 Pa greater than the pressure inside the entry nozzle. The PID-controller was then enabled and ran for five minutes. The result showed that the PID-controller managed to control the system to the reference point in less than 50 seconds for entry nozzles of diameters 6 mm, 8 mm, 10 mm and 12 mm. The results of the isokinetic deviations were -12 %, -5 %, -6 % and -4 % for entry nozzles with diameters 6 mm, 8 mm, 10 mm and 12 mm respectively. This is higher than the accepted values according to the European standard, which allows deviations in the interval -5%to 15%. However, these tests ran for relatively short time periods and started with large deviations which made it difficult to reach an isokinetic deviaiton in the accepted interval. Possible improvements could be to include the real time isokinetic deviation in the PID-controller, this would make it possible to change the reference value of the zero pressure in real time and guarantee isokinetic deviations in the accepted interval, even in extraordinary situations. / EU-regler ställer krav på anläggningar att kontrollera och begränsa sina utsläpp av stoft enligt EU standard 13284-1:2017. Vid en stoftmätning måste det tas hänsyn till många parametrar, där en av de viktigaste parametrarna är att provtagningen ska utföras isokinetiskt. Isokinetisk provtagning innebär att hastigheten i kanalen (skorstenen) är samma som i sonden där provgasen sugs ut. Dagens metoder för stoftmätning förlitar sig på manuella inställningar och den isokinetiska avvikelsen beräknas efter ett test. Det resulterade i frågeställnigen hur en automatiserad metod för bestämning av masskoncentration av stoft kan utformas så att den isokinetiska avvikelsen beräknas i realtid. Tryck, temperatur och gasvolym kvantiserades från analoga sensorer och kommunicerades till en mikrokontroller med det seriella protokollet I2C. En PID-reglator designades, implementerades och testades. PID-regulatorn tog tryckskillnaden mellan kanal och sond som insignal. Utsignalen från PID-regulatorn var en spänning som via en motordriven ventil kontrollerade inflödet i munstycket. Systemet testades i laborativ miljö genom att låta en fläkt skapa ett flöde tills den uppmätta tryckskillnaden mellan sond och kanal var -60 Pa. Därefter aktiverades PID-regulatorn och testet pågick sedan i fem minuter. Testet utfördes för munstycken med diameterna 6 mm, 8 mm, 10 mm och 12 mm. Resultatet visade att PID-regulatorn styrde systemet till referenspunkten på mindre än 50 sekunder för samtliga diametrar på munstyckena. De isokinetiska avvikelserna (skillnaden i hastighet mellan munstycke och kanal) beräknades till -12 %, -5 %, -6 % och -4 % för munstyckena 6 mm, 8 mm, 10 mm och 12 mm. I två av fallen var det högre än det accepterade värdet enligt EU standarden som tillåter avvikelser inom intervallet -5 % till 15 %. Det kan förklaras av att testen utfördes under en relativ kort tidsperiod och startades med stora avvikelser. Regulatorn skulle dock kunna förbättras genom att använda testets aktuella isokinetiska avvikelse och med den informationen bestämma systemets referenspunkt. Det skulle göra det möjligt att kompensera för tidigare avvikelser och på det sättet uppnå isokinetiska avvikelser inom tillåtet intervall även för extremfall.