No description available.

No / A computational fluid dynamics (CFD) model is used to investigate the droplet formation and deformation under the influence of different parameters. Droplet breakup phenomenon depends on several factors such as viscosity, velocity, pressure difference, and geometry. The most important parameter for droplet breakup is the Weber number (We) which is the ratio of disrupting aerodynamics forces to the surface tension forces. Volume of fluid (VOF) model is used in present work to simulate the droplet breakup. This work presents the effect of liquid velocity, viscosity, and orifice diameters on droplet formation and breakup.

No / In this paper, a model for urea prilling tower with co-current flow of cooling air and urea prills (particles) is presented. The process is modelled by simultaneous solution of the differential equations for hydrodynamics, heat and mass transfer between the air and prills. The process variables such as temperature, absolute and relative humidity of air along the height of the tower were obtained from this model. Temperature and moisture distribution of urea prills and their radial and vertical velocities were also calculated. The results of the present model were compared with the counter-current operation model available in the literature. The simulation results show that heat transfer performance for co-current operation is significantly less than that of the counter-current scenario. This is more pronounced for small prills, i.e. 1.0 mm than that of the large prills. The advantage of the model is that it can be used to investigate influence of operating parameters on efficiency of the co-current process. This also helps us to set the process control strategies for design and quality control purposes of the process.

No / A comprehensive study of the internal flow field for the prilling application in a perforated rotating bucket has been carried out. Computational Fluid Dynamics (CFD) is used to investigate the flow field of urea melt inside the perforated rotating bucket. The bucket is mounted at the top of the prilling tower. In prilling process, urea melt is sprayed by the perforated rotating bucket to produce the urea droplets, which falls down due to gravity. These drops fall down through a cooling medium and solidify into prills. The velocity field in the bucket is very important to study, as it has great effect on the heat and mass transfer performance in prilling process. ANSYS 14.0 CFD package is used to simulate and Design Modeler and Catia V5 are used for geometrical model of the perforated prilling bucket. Velocity distribution on different planes are obtained and discussed.

The nitrogenous metabolite urea is an important biomarker that indicates cows’ nutritional intake. Today, determining the urea concentration from milk samples requires analysis techniques in a lab which is time-consuming and expensive. It would be favourable to have an on-site measurement method to achieve a fast detection allowing farmers to quickly adjust the feed of individual cows, which might make it possible to reduce costs, increase milk production, and/or reduce the amount of nitrogen emission to the environment. This thesis is a part of a collaboration project between Linköping University and the Swedish University of Agricultural Sciences named “On-farm measurement of milk urea - development of a sensor”. The thesis investigated the activity and stability of the urease in an electrochemical biosensor, in which the urease is immobilised via encapsulation in a gel of poly(carbamoyl sulfonate) on a screenprinted electrode coated with a metal catalyst (copper), a cation exchanger (Nafion) and a conductive polymer (polyaniline). The linear range of the biosensor was successfully extended up to 2500 μM urea with a diffusion barrier composed of chitosan and polyvinyl butyral, enabling higher urea concentrations measurement than without the barrier (680 μM). Reproducibility, reusability, and storage stability measurements of the urease immobilised electrodes were performed and evaluated. A comparison between free enzyme, immobilised enzyme on the electrode surface and immobilised enzyme on an electrode surface that had been stored for a few days, was conducted to determine urease activity and stability. In addition, five components of milk (casein, lactose, ammonium, iron, and ascorbic acid) were measured separately to evaluate their interferences during milk urea detection. Interference was observed in several cases. A final evaluation of the present electrochemical biosensor was done by analysis of real milk samples giving promising results for future development. / On-farm measurement of milk urea - development of a sensor

In this work, crystallization experiments were carried out on four separate aqueous solutions of adipic acid, ammonium sulfate, urea and L-glutamic acid to measure the growth rate of these crystals under varying values of temperature, stirrer speed, cooling rate and holding time. All experiments were carried out in the Mettler Toledo LabMax, which is an automated laboratory reactor. A polarized light microscope was used to capture the images of the crystals and Image Pro Plus software was used for the analysis of crystal samples. Due to technical difficulties, the data could not be measured for adipic acid, ammonium sulfate or urea. L-Glutamic acid was much easier to work with and it was possible to obtain data. The growth rate for the b form of L-glutamic acid was estimated from the experimental data using a numerical simulation

No description available.

No description available.

No description available.

No description available.