M.Sc Tezi Görüntüleme

Student: Ebru ÖZTEKİN
Supervisor: Prof. Dr. Tahir YAVUZ
Department: Mechanical Engineering
Institution: Graduate School of Natural and Applied Sciences
University: Karadeniz Technical University, Turkey
Title of the Thesis: The Effects of Material Caracteristics on Pressure Drop
Level: M.Sc
Acceptance Date: 26/8/2003
Number of Pages: 71
Registration Number: i1415
Summary:

      SUMMARY

      

      In recent years, pneumatic conveying systems have been widely used in industries to handle powdered an granular materials because of a series of advantages such as the absence of envorimental pollution, flexible installation, optimum dimensions, progressive reduction of capital and installation cost. Unfortunately, the experimental and theoretical explorations done to increase system performance are still not maintained sufficiently achievements. Therefore, in this study, it is purposed mainly to investigate of the effects of variety bed material caracteristics, such as partical diameter, density, bed material temperature and quantity, on pressure drop and minimum fluidizing velocity which are important at the performance of pneumatic transportation.

This study consists of five chapters. In the first chapter, general information is presented. In the second chapter, experimental set-up and material caracteristics used at the experiments are given. The results of experimental studies obtained for Carborundum powders and sea sands, which have variety grit sizes and densities are given in the chapter three. The conclusions drawn from the results of this study and suggestion are summerized in the chapter four. The last chapter includes the list of references and appendices are followed.

      The conclusions obtained from this study showed that particle diameter, density, bed material concentration, bed void rate and bed temperature at the high temperature differences have a considerable effect on the pressure drop and minimum fluidizing velocity. However, It is found that the experimental results for fixed pressure drop measured in fluidised bed are smaller than that of fixed pressure drop variables calculated with the weight per unit area and these differences between the two values are due to the particle-chamber wall interactions and inaccuracies in the experiments.

      

Key Words: Pneumatic Conveying, Two-Phase Flow, Gas- solid, Pressure drop, Vertical pipelines, Particulate solids,