The 3D flow characteristics in SG can provide input for the analysis of flow induced vibration (FIV). The secondary side flow field was simulated based on the porous media model with FLUENT solver. The flow resistance...
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The 3D flow characteristics in SG can provide input for the analysis of flow induced vibration (FIV). The secondary side flow field was simulated based on the porous media model with FLUENT solver. The flow resistances of flow along and cross tubes as well as flow resistances of downcomer, support plates and separators were added to the momentum equation. The 3D heat transfer from primary to secondary side fluid was calculated during iteration and set as the energy source of secondary side fluid, and the calculation results agree well with the design values. Meanwhile, the results show that the resultant localized thermal-hydraulic characteristics were unevenly distributed. The maximum and minimum flow vapor qualities flowing into the primary separators are 0.75 and 0.07, respectively. The average heat transfer coefficients of primary and secondary sides are 15 856.5 and 63 623.0 W/(m2·K), respectively. The maximum heat transfer coefficient of secondary side is 122 862.9 W/(m2·K). The average heat flux of U-tube is 149.9 kW/m2. The maximum cross flow velocity and cross flow energy (ρu2) through the U-bend region are 4.06 m/s and 1 145 J/m3, respectively.
In this study, Laser-Induced Breakdown Spectroscopy (LIBS) technology was applied to detect iodine, an essential element for human body. Iodine in buffer gases of N2 and air was detected using nanosecond and picosecon...
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The real-time dynamic simulation model of a 600MW lignite-fired pulverized boiler, which is a supercritical once-through boiler with fan mill three drying media direct fired system, was established. The step reduction...
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The real-time dynamic simulation model of a 600MW lignite-fired pulverized boiler, which is a supercritical once-through boiler with fan mill three drying media direct fired system, was established. The step reduction of hot flue gas flow rate was simulated. The dynamic responses of live and reheat steam temperatures were obtained and analyzed. Results show that the response of steam temperature is an oscillation process. The superheat and reheat steam overtemperature values are influenced by the boiler load, the hot flue gas extracting percent and the inertia time of pulverizing system.
Solar energy is clean without pollution,rich and free,so solar thermal power has the huge potential for future energy *** type concentrating technology can be used for large-scale solar power *** the power tower syste...
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Solar energy is clean without pollution,rich and free,so solar thermal power has the huge potential for future energy *** type concentrating technology can be used for large-scale solar power *** the power tower system,the heat receiver is the key equipment for sunlightheat *** thermal performance of the receiver will affect the efficiency of the entire power *** is no rich experience on the design of receiver,which is mainly based on the coal-fired *** to the non-uniform and instantaneous characteristics of sunlight,the receiver should differ greatly from the conventional coal-fired *** it is necessary to study the receiver according to the sunlight *** experiment platform for testing the thermal performance of a water/steam cavity receiver was firstly designed and *** start-up curves under different operating pressures were obtained and the receiver has low thermal efficiency of only about 55-70%.The low thermal efficiency is attributed to the low mass flow rate.A combined method was proposed to evaluate the thermal performance of the cavity receiver for start up and *** numerical results are in good agreement with the *** results suggested that an appropriate mass flow rate of 200 kg/h should be chosen for the design and operation of the experiment *** thermal performance of a solar cavity receiver under windy conditions was numerically *** heat flux and temperature distributions on boiling tubes in the cavity were *** convective and radiative heat losses were analyzed in *** the wind flow angle or velocity can obviously affect the air velocity inside the cavity,which reaches the maximum value for side on wind,resulting in a large convective heat *** on the experimental and numerical studies,a water/steam cavity receiver was designed and *** receiver is now being used in 1MW power tower plant in China with a
Amorphe Zwischenphasen sind wichtige Vorstufen bei der Kristallisation vieler biogener Minerale. Obwohl bereits gezeigt werden konnte, dass amorphe Calciumcarbonate (ACC) eine inhärente Nahordnung aufweisen, die ...
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Amorphe Zwischenphasen sind wichtige Vorstufen bei der Kristallisation vieler biogener Minerale. Obwohl bereits gezeigt werden konnte, dass amorphe Calciumcarbonate (ACC) eine inhärente Nahordnung aufweisen, die unterschiedlichen kristallinen Formen zugeordnet werden kann, wurde bisher noch nie experimentell bestätigt, ob solche Nahordnungen bereits in sehr kleinen Clustern (<2 nm) vorkommen. Hier wurde die Stabilität und Struktur von 10,12‐Pentacosadiinsäure(PCDA)‐geschützten ACC‐Clustern untersucht, die eine Kerngröße von ca. 1.4 nm aufweisen und aus nur 7 CaCO 3 ‐Einheiten bestehen. Die Ligandenkonzentration und ‐struktur spielt eine Schlüsselrolle bei der Stabilisierung dieser ACC‐Cluster. Schon solch kleine CaCO 3 ‐Einheiten weisen eine Proto‐Calcit‐Nahordnung auf, wenn auch mit relativ hoher Unordnung. Dies legt nahe, dass ein struktureller Zusammenhang zwischen Pränukleationsclustern, amorphen Zwischenstufen und dem fertigen kristallinen Polymorph besteht.
Pre-drying is a potential way to improve the electric generation efficiency of lignite-fired power plant, and steam is a main kind of drying heat source. In conventional pre-dried lignite-fired power system, the steam...
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Pre-drying is a potential way to improve the electric generation efficiency of lignite-fired power plant, and steam is a main kind of drying heat source. In conventional pre-dried lignite-fired power system, the steam extraction of regenerative system is led to the dryer directly. The steam extraction must be used by the dryer after throttling, if the energy mismatch exists between the supply of steam extraction and the need of dryer. Two systems of energy supply for the dryer, that the energy of the steam extraction is supplied to the dryer via compressor or ejector, were proposed in this paper to further increase the energy utilization efficiency. These systems were thermodynamic analyzed, and the electric generation efficiencies of these systems were compared. The energy saving boundary was gotten.
For a cone-beam three-dimensional computed tomography (3D-CT) scanning system, voxel size is an important indicator to guarantee the accuracy of data analysis and feature measurement based on 3D-CT images. Meanwhile...
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For a cone-beam three-dimensional computed tomography (3D-CT) scanning system, voxel size is an important indicator to guarantee the accuracy of data analysis and feature measurement based on 3D-CT images. Meanwhile, the voxel size changes with the movement of the rotary stage along X-ray direction. In order to realize the automatic calibration of the voxel size, a new and easily-implemented method is proposed. According to this method, several projections of a spherical phantom are captured at different imaging positions and the corresponding voxel size values are calculated by non-linear least-square fitting. Through these interpolation values, a linear equation is obtained that reflects the relationship between the voxel size and the rotary stage translation distance from its nominal zero position. Finally, the linear equation is imported into the calibration module of the 3D-CT scanning system. When the rotary stage is moving along X-ray direction, the accurate value of the voxel size is dynamically exported. The experimental results prove that this method meets the requirements of the actual CT scanning system, and has virtues of easy implementation and high accuracy.
Cigarette cut tobacco mildew will cause tremendous economic loss and human health. An improved electronic nose was developed to detect cigarette cut tobacco mildew at early stages. After storing 96 h at 30 °C and...
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Presented is a 3D simulation of the air flow and temperature variation in an ice drink refrigeration cabinet, during an automated dynamic cycle of switching on and switching off. To correctly model the effect of perfo...
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Presented is a 3D simulation of the air flow and temperature variation in an ice drink refrigeration cabinet, during an automated dynamic cycle of switching on and switching off. To correctly model the effect of perforated plate separating evaporator and storage compartments, a benchmark problem is designed, and used as a reference to determine the parameters in the porous-jump model by parameter optimization. Subsequently, the dynamic cycle of initial switch on, automated switch off and automated switch on is simulated. Both the flow field distribution and temperature profile are analyzed and the time required for these three stages is obtained. Full 3D CFD simulation of refrigeration system provides not only detailed temperature distribution in the cabinet but also operational parameters of the system such as for switch on-off cycle. Those output from simulation are important for cabinet design to improve the storage quality of products while reducing the energy use.
A DEM-CFD coupled approach were proposed to joint the advantage of discrete models of providing detailed packing information and continuous models of realizing macro-scale simulations. DEM simulation of particle packi...
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ISBN:
(纸本)9788874317271
A DEM-CFD coupled approach were proposed to joint the advantage of discrete models of providing detailed packing information and continuous models of realizing macro-scale simulations. DEM simulation of particle packing in a small-scale fixed bed was first validated, then the model was used on particle packing in a lab-scale fixed bed with internals, statistics voidage distribution was obtained and coupled with Eulerian Granular multiphase Model, realized the maro-scale simulation of fixed beds of considering the meso-scale packing structure.
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