Abstract:In this paper, a mathematical model is developed to describe the dynamics of the drum-level of a natural circulation boiler. A boiler-drum is divided into two parts; the upper part contains saturated steam while the lower part contains a steam/water mixture. The ratio of the steam in that mixture is defined in this work as the steam volumetric ratio. On the other hand, balance equations are applied to the drum. The resulting equations are used to model the drum-level. The importance of the resulting model come… Show more
“…The other variables of interest here include the drum pressure ( P ) and drum water level ( l dr ). The original modeling work including detailed descriptions, parameters, and further simplifications of these equations into a more compact system of equations is available in the literature. − …”
Section: Process Configuration and
Modeling Approachmentioning
“…The other variables of interest here include the drum pressure ( P ) and drum water level ( l dr ). The original modeling work including detailed descriptions, parameters, and further simplifications of these equations into a more compact system of equations is available in the literature. − …”
Section: Process Configuration and
Modeling Approachmentioning
“…All of these models use a steady‐state momentum equation for downcomer flow analysis. Tawfeic 9 presents a generalized approach for boiler drum level modeling by introducing pressure, water volume, dryness fraction, water level, downcomer flow, and steam volumetric fraction as variables. The model uses a transient momentum conservation equation for downcomer flow analysis.…”
The present work aims to develop an integrated heat transfer and hydrodynamic model for the study of boiler dynamics in fluctuating load conditions. A transient heat transfer model has been developed to estimate water side heat transfer and it is directly integrated with the hydrodynamic model. Two independent natural circulation circuits for furnace water wall and convection tube bank have been considered due to differences in heat transfer, dryness fraction, and void fraction. The transient heat transfer model calculates the heat transfer and water wall temperature of the various sections to calculate total gas side heat transfer, gas temperature profile, and waterside heat transfer in the furnace water wall and convection tube bank. Mass momentum and energy conservation equations are generated for both natural circulation circuits using the estimated value of waterside heat transfer of the transient heat transfer model. These equations are integrated with mass and energy conservation equations for the drum below water level and drum above water level to generate a system of equations to estimate drum pressure and water level fluctuation. This model has been extended for boiler feedback control systems, including the load management and the water level control system.
“…The furnace of a boiler can convert the chemical energy in the fuel to heat, and it is the function of the boiler to transfer this heat to the contained water in the most efficient technique. This heat is transferred by radiation, conduction, and convection to the water in the boiler [1]. The relative percentage of each depends on the type of boiler, the heat transfer surface built for, and the type of fuel.…”
Rapid rise in the steam mass flow rate causes the increase in dynamic effects. The pressure disturbance in the boiler's upper drum cause mechanical effects. Drum level fluctuations cause interactions with the controls of boiler combustion. Interactions with the controls, resulting inefficient and dangerous operations.The dynamic effects in the "upper" drum of the boiler (mechanical's effects) are very complex problems and critical due to the pressure disturbance in the upper drum of the boiler. This work deals with an experimental investigation of the dynamic behavior of the boiler drum level system is reported from plant data (Al-Quds power plant) in Baghdad / Iraq under a particular condition of operating, and the mathematical equations of the boiler model variables explained and defined. The dynamic effects are investigated with increasing steam mass flow rate (10% and 20%) at the outlet of the boiler. The results showed that the rapid rise in the rate of steam mass flow causes the dynamic effects to increase (shrink and swell) by 15%, rates of evaporation and thus causes an increase in the volume of water inside the upper drum boiler that causes overheating in the tubes.
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