Cold Water Model Simulation of Aluminum Liquid Fluctuations Induced by Anodic Gas in New Type of Cathode Structure Aluminum Electrolytic Cell

2011 ◽  
pp. 1155-1160
Author(s):  
Yan Liu ◽  
Ting’an Zhang ◽  
Zhihe Dou ◽  
Hongxing Wang ◽  
Guozhi Lv ◽  
...  
2012 ◽  
pp. 949-953
Author(s):  
Liu Yan ◽  
Zhang Ting’an ◽  
Li Chong ◽  
Zhao Qiuyue ◽  
Wang Shuchan ◽  
...  

2012 ◽  
pp. 949-953
Author(s):  
Liu Yan ◽  
Zhang Ting'an ◽  
Li Chong ◽  
Zhao Qiuyue ◽  
Wang Shuchan ◽  
...  

2020 ◽  
Vol 92 (1) ◽  
pp. 10906
Author(s):  
Jeroen Schoenmaker ◽  
Pâmella Gonçalves Martins ◽  
Guilherme Corsi Miranda da Silva ◽  
Julio Carlos Teixeira

Organic Rankine Cycle (ORC) systems are increasingly gaining relevance in the renewable and sustainable energy scenario. Recently our research group published a manuscript identifying a new type of thermodynamic cycle entitled Buoyancy Organic Rankine Cycle (BORC) [J. Schoenmaker, J.F.Q. Rey, K.R. Pirota, Renew. Energy 36, 999 (2011)]. In this work we present two main contributions. First, we propose a refined thermodynamic model for BORC systems accounting for the specific heat of the working fluid. Considering the refined model, the efficiencies for Pentane and Dichloromethane at temperatures up to 100 °C were estimated to be 17.2%. Second, we show a proof of concept BORC system using a 3 m tall, 0.062 m diameter polycarbonate tube as a column-fluid reservoir. We used water as a column fluid. The thermal stability and uniformity throughout the tube has been carefully simulated and verified experimentally. After the thermal parameters of the water column have been fully characterized, we developed a test body to allow an adequate assessment of the BORC-system's efficiency. We obtained 0.84% efficiency for 43.8 °C working temperature. This corresponds to 35% of the Carnot efficiency calculated for the same temperature difference. Limitations of the model and the apparatus are put into perspective, pointing directions for further developments of BORC systems.


2021 ◽  
Author(s):  
Gordana Beg Paklar ◽  
Zoran Pasaric ◽  
Mirko Orlic ◽  
Antonio Stanesic

<p>Strong upwelling driven by the NNW winds was detected off the eastern middle Adriatic coast in May 2017. High resolution CTD data revealed thermocline doming by about 20 m at approximately 20 km from the coast. Main characteristics of the upwelling event are reproduced in the realistic ROMS model simulation. Adriatic scale ROMS model having 2.5 km horizontal resolution, forced by the air-sea fluxes calculated using surface fields from operational weather forecast model ALADIN-HR (Tudor et al., 2013; Termonia et al., 2018), river discharges, tides and water mass exchange through the Strait of Otranto, reproduces cold water dome and two-layer offshore flow in accordance with CTD and shipborne ADCP measurements. Significant improvement in the upwelling simulations is obtained using increased drag coefficient. The location of upwelling is correctly modelled, although with somewhat lower upper layer temperatures if compared with measurements. Moreover, the surface cyclonic circulation indicated by ADCP measurements along the cross-Adriatic transect is also evident in the model results. In order to improve understanding of the upwelling mechanism, several schematized numerical experiments are conducted. Wind fields from dynamical adaptation (Zagar and Rakovec, 1999; Ivatek-Sahdan and Tudor, 2004) of ALADIN-HR8 (8 km horizontal grid spacing) wind forecast to 2 km grid, are decomposed by the Natural Helmholtz-Hodge Decomposition (HHD) into divergence-free (incompressible), rotation-free (irrotational), and harmonic (translational) component (Bhatia et al., 2014). The components thus obtained and their combinations are used for calculation of the wind stress instead of the total wind field. Simulations with decomposed wind stress are conducted in the Adriatic domains with both flat bottom and realistic topography. Schematized simulations reveal that the positive rotational wind component is responsible for the rising of thermocline through Ekman pumping and it is more pronounced in the flat bottom basin. In the simulations with divergent wind component, the thermocline doming disappears and only coastal upwelling is reproduced. Additional idealised simulations with homogeneous NW wind stress are performed assuming both two-layer and uniform initial density field.</p>


2015 ◽  
pp. 795-800 ◽  
Author(s):  
Are J. Simonsen ◽  
Kristian Etienne Einarsrud ◽  
Ingo Eick

In the preceding paper on “Metal Overvoltage” it has been shown that a defect in the design of the electrolytic cell used in previous work gave rise to erroneous values for transfer resistance. It is necessary, therefore, to examine to what extent, if any, the theory of transfer resistance must be modified in order to adapt itself to the new values obtained when the above defect is remedied. A number of experiments have been repeated with the various electrodes, using the new type of cell, but since the conclusions arrived at were the same in all cases, it will be sufficient to give results for a single electrode. The following values were obtained with a silver cathode in an electrolyte of N sulphuric acid at room temperature.


2016 ◽  
Vol 2016 ◽  
pp. 1-8 ◽  
Author(s):  
Dongxing Wang ◽  
Yan Liu ◽  
Zimu Zhang ◽  
Pin Shao ◽  
Ting’an Zhang

Average diameter of bubbles is important in copper furnace. Based on the principle of similarity, a slice water model of a furnace with bottom-blown oxygen in matte-smelting process was established. A high-speed camera was used to record images continuously and clearer pictures were selected for treatment. Finally, image processing software was used for obtaining the average diameter of the bubbles. The effects of different injection conditions and equipment factors such as the diameter of nozzle, the nozzle installing angle, and gas velocity on the average diameter of bubbles were studied with cold water model experiment, exploring the dispersion and disintegration rules of bubbles. According to experimental data and Buckingham’s theorem, by using dimensional analysis method, an empirical formula on average diameter of bubbles was established (dB=0.41666d0.29374θ-0.46572v-0.16725). It can be seen from the formula that nozzle installing angle and diameter of nozzle make the most impact on the average diameter of bubbles in bottom blown oxygen copper furnace.


1973 ◽  
Vol 187 (1) ◽  
pp. 207-214 ◽  
Author(s):  
G. C. Gardner ◽  
I. G. Crow ◽  
P. H. Neller

The results of several experimental programmes defining the various mechanisms of importance in determining the carry-under of steam in boiler drums are described. One programme examined the performance of cyclones and the natural separation of steam in the water pool in a full-size section of drum by employing Freon 12 liquid and vapour as the working fluids. Another programme studied the drawdown of the main liquid-vapour interface into the downcomers in a fifth-scale cold water model and theoretically described the critical conditions. Also discussed is a programme concerning heat transfer by the subcooled feed.


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