scholarly journals Prediction of Pollution State of Heating Surface in Coal-Fired Utility Boilers

IEEE Access ◽  
2020 ◽  
Vol 8 ◽  
pp. 206132-206145
Author(s):  
Qiang Li ◽  
Peigang Yan ◽  
Jinfu Liu ◽  
Yuanhao Shi ◽  
Daren Yu
Keyword(s):  
Heating Surface ◽  
Utility Boilers

scholarly journals On Line Dirt Based Soot Blowing System using Fuzzy Logic for Utility Boilers

2019 ◽  
Vol 8 (2) ◽  
pp. 1669-1671
Keyword(s):  
Power Plants ◽  
Intelligent System ◽  
Thermal Power ◽  
Heating Surface ◽  
Boiler Tube ◽  
Heating Efficiency ◽  
Utility Boilers ◽  
On Line ◽  
Simulation Results ◽  
Burning Coal

Soot is a byproduct of burning coal in thermal power plants. The soot accumulates in the boilers tubes. It gradually spoils the heating surface which reduces the heating efficiency. Hence it has to be cleaned. This process is called soot blowing. The existing soot blower control system in the old boiler is composed of relays, timers and contactors which are not efficient. In order to improve the efficiency, an intelligent system is proposed which estimates the dirt in the boiler tube periodically and initiates soot blowing process to improve the thermal efficiency. Simulation results demonstrate the superiority of the proposed scheme when compared to relay logics.

Prediction of Performance From PRB Coal Fired in Utility Boilers With Various Furnace and Firing System Arrangements

2009 ◽  
Author(s):  
B. Chudnovsky ◽  
A. Talanker ◽  
Y. Berman ◽  
R. Saveliev ◽  
M. Perelman ◽  
...  
Keyword(s):  
Heat Transfer ◽  
Power Plants ◽  
Heating Surface ◽  
Heat Rate ◽  
Low Rank ◽  
Gas Temperature ◽  
Retention Capacity ◽  
Utility Boilers ◽  
Bituminous Coals ◽  
Firing System

Present regulatory requirements enforces the modification of the firing modes of existing coal-fired utility boilers and the use of coals different from those originally designed for these boilers. The reduction of SO2 and NOx emissions were the primary motivation for these changes. However, economic considerations played a major role too. Using sub-bituminous coals has become an important solution for emissions compliance due to their unique constituents and combustion characteristics; these coals are often referred to as enviro coals. Powder River Basin (PRB) Coals are classified as sub-bituminous ranked coals. Unlike higher ranked bituminous coals, which have tight pore structures that limit the amount of moisture they could hold, low rank coals, such as PRB coals, have looser pore structure and additional moisture retention capacity. PRB coals differ in many properties from those of the commonly burned bituminous coals, including low heating value, low fusion temperature, and high moisture content. However, PRB coals have low sulfur content and are relatively low cost. They can also lower NOx emission from power plants due to higher volatile content. When power plants switch from the designed coal to a PRB coal, operational challenges, including transportation, handling, storage, and combustion, were encountered. A major problem faced when using PRB coals is severe slagging and excess fouling on the heating surface. Not only is there an insulating effect from deposit, but there is a change in reflectivity of the surface. Excess furnace fouling and high reflectivity ash may cause reduction of heat transfer in the furnace, which results in higher furnace exit gas temperatures (FEGT), especially with opposite wall burners and with single backpass. Higher FEGT usually result in higher stack gas temperature and increasing in the reheater spray flow and therefore decreasing the boiler efficiency with higher heat rate of the unit. The modification of an existing unit for firing of PRB coals is confined to — and constrained by — existing equipment. All successful conversions happen when in the design phase of a project the following parameters are evaluated: (1) capacities or limitations of furnace size, (2) firing system type and arrangement, (3) heat transfer surface, (4) pulverizers, (5) sootblowers, (6) fans, and (7) airheaters. In the present study we used a comprehensive methodology to predict the behavior of three PRB coals fired in a 575MW T-fired boiler.

THE MECHANISM OF RAISING AND QUANTIFICATION OF SPECIFIC HEAT FLUX AT BOILING OF NANOFLUIDS IN FREE CONVECTION CONDITIONS

2017 ◽  
pp. 25-34
Author(s):  
V.N. Moraru
Keyword(s):  
Heat Transfer ◽  
Heat Flux ◽  
Heat Capacity ◽  
Specific Heat ◽  
Chemical Properties ◽  
Heating Surface ◽  
Physical Models ◽  
Superheated Liquid ◽  
Two Phase ◽  
Boiling Process

The results of our work and a number of foreign studies indicate that the sharp increase in the heat transfer parameters (specific heat flux q and heat transfer coefficient _) at the boiling of nanofluids as compared to the base liquid (water) is due not only and not so much to the increase of the thermal conductivity of the nanofluids, but an intensification of the boiling process caused by a change in the state of the heating surface, its topological and chemical properties (porosity, roughness, wettability). The latter leads to a change in the internal characteristics of the boiling process and the average temperature of the superheated liquid layer. This circumstance makes it possible, on the basis of physical models of the liquids boiling and taking into account the parameters of the surface state (temperature, pressure) and properties of the coolant (the density and heat capacity of the liquid, the specific heat of vaporization and the heat capacity of the vapor), and also the internal characteristics of the boiling of liquids, to calculate the value of specific heat flux q. In this paper, the difference in the mechanisms of heat transfer during the boiling of single-phase (water) and two-phase nanofluids has been studied and a quantitative estimate of the q values for the boiling of the nanofluid is carried out based on the internal characteristics of the boiling process. The satisfactory agreement of the calculated values with the experimental data is a confirmation that the key factor in the growth of the heat transfer intensity at the boiling of nanofluids is indeed a change in the nature and microrelief of the heating surface. Bibl. 20, Fig. 9, Tab. 2.

scholarly journals Intensifying the Charging Response of a Phase-Change Material with Twisted Fin Arrays in a Shell-And-Tube Storage System

Energies ◽  
2021 ◽  
Vol 14 (6) ◽  
pp. 1619
Author(s):  
Mohammad Ghalambaz ◽  
Hayder I. Mohammed ◽  
Jasim M. Mahdi ◽  
Amir Hossein Eisapour ◽  
Obai Younis ◽  
...  
Keyword(s):  
Phase Change ◽  
Phase Change Material ◽  
Storage System ◽  
Heating Surface ◽  
Superior Performance ◽  
Three Dimensional Model ◽  
Reference Case ◽  
Storage Rate ◽  
Shell And Tube ◽  
Change Material

A twisted-fin array as an innovative structure for intensifying the charging response of a phase-change material (PCM) within a shell-and-tube storage system is introduced in this work. A three-dimensional model describing the thermal management with charging phase change process in PCM was developed and numerically analyzed by the enthalpy-porosity method using commercial CFD software. Efficacy of the proposed structure of fins for performing better heat communication between the active heating surface and the adjacent layers of PCM was verified via comparing with conventional longitudinal fins within the same design limitations of fin material and volume usage. Optimization of the fin geometric parameters including the pitch, number, thickness, and the height of the twisted fins for superior performance of the proposed fin structure, was also introduced via the Taguchi method. The results show that a faster charging rate, higher storage rate, and better uniformity in temperature distribution could be achieved in the PCMs with Twisted fins. Based on the design of twisted fins, it was found that the energy charging time could be reduced by up to 42%, and the energy storage rate could be enhanced up to 63% compared to the reference case of straight longitudinal fins within the same PCM mass limitations.

scholarly journals Analysis of oxide scale thickness and pores position of HCM12A steel in supercritical water

2021 ◽  
Vol 40 (1) ◽  
pp. 53-65
Author(s):  
Li Sun ◽  
Weiping Yan
Keyword(s):  
Diffusion Coefficient ◽  
Oxide Scale ◽  
Supercritical Water ◽  
Heating Surface ◽  
Oxidation Mechanism ◽  
Oxygen Activity ◽  
Oxide Scales ◽  
Spinel Layer ◽  
Magnetite Layer ◽  
Iron Diffusion

Abstract More attention has been paid to the exfoliation of oxide scale on high-temperature heating surface of utility boiler. The oxidation mechanism of HCM12A steel in supercritical water is proposed and the growth of oxide film is simulated. The duplex scale contains an outer magnetite layer and an inner Cr-rich spinel layer. According to the data of Backhaus and Töpfer, the diffusion coefficient values of iron in magnetite layer are discussed and the function of R V, R I {R}_{\text{I}} for oxygen activity can be used for calculation of iron diffusion coefficients in Cr-rich spinel layer. Based on Wagner’s oxidation theory, the oxidation rate constants of HCM12A are calculated at 500 and 600°C in supercritical water, compared with experimental data of the relevant literatures. The oxygen activities at the interfaces of alloy/Cr-rich spinel oxide and magnetite/supercritical water are estimated. The simulation results of weight gain are matched with the test data. The iron diffusion mechanisms inside the magnetite layer and the Cr-rich spinel layer are analyzed. The iron diffusion coefficient at the interface of Cr-rich spinel/magnetite is discontinuous, while the oxygen activity is continuous in the whole double layer. The thickness of oxide scale on inner tube walls of the final superheater coils (T91) of a 600 MW supercritical boiler is calculated by using the calculation method provided by the paper. The modeling results, the measured data, and the calculation results by the method are compared. Accurate calculation of the thickness of the inner and outer oxide scales can provide a necessary basis for predicting the stress and exfoliation of oxide scales.

Effects of ultrasonic waves on subcooled pool boiling on a small plain heating surface

2019 ◽  
Vol 201 ◽  
pp. 274-287 ◽  
Author(s):  
Jiguo Tang ◽  
Licheng Sun ◽  
Dan Wu ◽  
Min Du ◽  
Guo Xie ◽  
...  
Keyword(s):  
Pool Boiling ◽  
Heating Surface ◽  
Ultrasonic Waves

Experimental and Mechanism Investigation on Boiling Heat Transfer Characteristics of Alumina/Water Nanofluid on a Cylindrical Tube

NANO ◽  
2019 ◽  
Vol 14 (10) ◽  
pp. 1950124
Author(s):  
Hao Zhang ◽  
Zeng-en Li ◽  
Shan Qing ◽  
Zhuangzhuang Jia ◽  
Jiarui Xu ◽  
...  
Keyword(s):  
Heat Transfer ◽  
Boiling Heat Transfer ◽  
Particle Deposition ◽  
Heat Transfer Performance ◽  
Pool Boiling ◽  
Heating Surface ◽  
Cylindrical Tube ◽  
Influential Factors ◽  
Transfer Performance ◽  
Pool Boiling Heat Transfer

Nucleate pool boiling heat transfer experiments have been conducted to nanofluids on a horizontal cylinder tube under atmospheric pressure. The nanofluids are prepared by dispersing Al2O3 nanoparticles into distilled water at concentrations of 0.001, 0.01, 0.1, 1 and 2[Formula: see text]wt.% with or without sodium, 4-dodecylbenzenesulfonate (SDBS). The experimental results showed that: nanofluids at lower concentrations (0.001[Formula: see text]wt.% to 1[Formula: see text]wt.%) can obviously enhance the pool boiling heat transfer performance, but signs of deterioration can be observed at higher concentration (2[Formula: see text]wt.%). The presence of SDBS can obviously enhance the pool boiling heat transfer performance, and with the presence of SDBS, a maximum enhancement ratio of BHTC of 69.88%, and a maximum decrease ratio of super heat of 41.12% can be found in Group NS5 and NS4, respectively. The tube diameter and wall thickness of heating surface are the influential factors for boiling heat transfer coefficient. Besides, we find that Rohsenow formula failed to predict the characteristics of nanofluids. The mechanism study shows that: the decrease of surface tension, which leads to the decrease of bubble departure diameter, and the presence of agglomerates in nanofluids are the reasons for the enhanced pool boiling heat transfer performance. At higher concentration, particle deposition will lead to the decrease of distribution density of the vaporization core, and as a result of that, the boiling heat transfer performance will deteriorate.

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