Abstract

In Europe, 3 % of the electricity consumed by industry is spent on the production of compressed air. At the same time, the payment for electricity consumed by the compressor is the largest share in the structure of the factorys costs. In modern production, compressed air requires drying to meet the requirements of the equipment and for various technological processes. In this case, a large amount of compressed air is lost thus, improving the design of air dryers is an important step for improving energy efficiency. In this paper is developing a method for reducing the energy costs of the heated desiccant dryers is developed by mean of regenerating adsorbents using microwave energy.In the process of developing heaters using microwave energy, the main problem is the achievement of a uniform heating of the material. The same problem also arises when using microwave energy to regenerate the adsorbent in the adsorption dryer. Due of above-mentioned, the problem by dynamically changing the configuration of the heater chamber and waveguide systems is solved by using of increasing the uniformity of heating and two opposite waveguides in the heater design with a variable phase of one of them. A specific condition for conducting experiments is obtained. Particularly the adsorption dryer chamber is a cylindrical vessel that is filled with an adsorbent and has predetermined proportions. A significant change of these proportions adversely affect at the adsorption process during the operation of the desiccant.

Highlights

  • Modern adsorption dryers during the process of regenerating the adsorbent uses hot air, which is heated by external heaters and transported to the cavity of the adsorption column [1]

  • In the process of developing heaters using microwave energy, the main problem is the achievement of a uniform heating of the material

  • Preventing silica gel overheating during heating is an important task that can be solved through the rotation of the phases, by means of moving the material

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Summary

Introduction

Modern adsorption dryers during the process of regenerating the adsorbent uses hot air, which is heated by external heaters and transported to the cavity of the adsorption column [1]. Heating the moisture directly in adsorbent pores is a useful step towards improving the energy saving of the regenerative drying of the adsorbent. This is possible if microwave energy is used to heat the adsorbed moisture in the desorption process. Drying with the use of microwave heating is characterized by ecological purity [2], absence of thermal inertia and high coefficient of efficiency [3,4,5]. Heating by using the microwave energy has some positive side effects. The effect of reducing the surface tension coefficient of water [6,7,8,9] accelerates evaporation [10]

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