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通过手工计算和ANSYS有限元软件计算两种方法对安徽新源热电有限公司烟囱与吸收塔合一结构进行结构计算。分析了结构在风载荷、地震载荷作用下的应力和变形,比较了手工计算和有限元电算结果,可为类似工程的计算提供理论参考。 相似文献
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为了实现密相塔半干法脱硫工艺的精确加湿进一步提高系统脱硫效率,利用推导出的传热传质计算方法,得到烟气温度降低和加水量的关系.结合3组密相塔半干法工程实际数据,发现理论计算值和实测值误差区间仅为2.9% ~5.4%.通过选取河北某钢厂210 m2烧结烟气密相塔半干法脱硫项目实际在线检测数据,发现循环脱硫灰含湿量为3%的系统脱硫效率整体高于含湿量为5%和4%的样品,最大值达93.56%.通过粒度分析、扫描电镜、X射线衍射及差热-热重对2种不同含湿量的循环脱硫灰进行表征,结果表明,含湿量为3%的循环脱硫灰较含湿量为5%的样品粒径小、比表面积大,无团聚现象,物相分析还证实相对于含湿量为5%样品,其Ca(OH)2和结晶水含量少,几乎都是CaSO4和CaS03干态物质,因此脱硫反应进行彻底,脱硫效率较高. 相似文献
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Gabriel N. de O. Teixeira Arthur M. S. da Cruz Gisella R. L. Samanamud Alexandre B. França Luzia L. R. Naves Diego Melo 《Journal of environmental science and health. Part. B》2020,55(1):19-29
AbstractThe main objective of this study is the degradation of a synthetic solution of atrazine by a modified vermiculite catalyzed ozonation, in a rotating packed bed (RPB) reactor. A 0.5?L RPB reactor was used to perform the experiments, using a Central Composite Design (CCD) response surface to construct the quadratic model based on the factors: pH, catalyst concentration and reactor rotation frequency. The response variable was the removal of the organic load measured in terms of Chemical Oxygen Demand (COD). After the complete quadratic model was constructed through the response surface, the COD degradation process had an optimal removal of 41% under the following conditions: pH 8.0, rotation of 1150?rpm and catalyst concentration 0.66?g L?1. 相似文献
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李皓 《湖南环境生物职业技术学院学报》2006,12(4):408-411
在机械加工中采用近似法加工空间曲面,常常使加工过程变得简单可行,而且解决了部分机床力不能及的矛盾.在此介绍了在普通铣床上用椭圆曲线网络加工大半径浅圆弧的加工原理、加工方法及其误差分析. 相似文献
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Vikram J. Kaku Michel C. Boufadel Albert D. Venosa James Weaver 《Environmental Fluid Mechanics》2006,6(4):385-406
The evaluation of dispersant effectiveness used for oil spills is commonly done using tests conducted in laboratory flasks.
We used a Hot Wire Anemometer (HWA) to characterize mixing dynamics in the Swirling Flask (SF) and the Baffled Flask (BF),
the latter is being considered by the EPA to replace the prior to test dispersant effectiveness in the laboratory. Five rotation
speeds of the orbital shaker carrying the flasks were considered, Ω = 50, 100, 150, 175 and 200 rpm. The radial and azimuthal
water speeds were measured for each Ω. It was found that the flow in the SF is, in general, two-dimensional changing from
horizontal at low Ω to axi-symmetric at high Ω. The flow in the BF appeared to be three-dimensional at all rotation speeds.
This indicates that the BF is more suitable for representing the (inherently) 3-D flow at sea. In the SF, the speeds and energy
dissipation rates ɛ increased gradually as the rotation speed increased. Those in the BF increased sharply at rotation speeds
greater than 150 rpm. At 200 rpm, the Kolmogorov scale (i.e., size of smallest eddies) was about 250 and 50 μm in the SF and
BF, respectively. Noting that the observed droplet sizes of dispersed oils range from 50 to 400 μm (hence most of it is less
than 250 μm), one concludes that the mixing in the SF (even at 200 rpm) is not representative of the vigorous mixing occurring
at sea. 相似文献
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M. Lati S. Boughali D. Bechki H. Bouguettaia D. Mennouche N. Gana 《International Journal of Green Energy》2019,16(6):413-422
A passive flat-plate solar air collector was constructed in the laboratory of New and Renewable Energy in Arid Zones, Ouargla University, South East Algeria. The absorber of the passive flat-plate solar air collector was laminated with a thin layer of local sand. This acted as a thermal packed bed with a collecting area of 0.5 m2 (1 m × 0.5 m). Three series of experiments were performed. The first consisted of choosing the best sand brought from three different places of the Algerian desert. The second consisted of studying the effect of the thickness of the sand layer on the daily efficacy of the collector. The influence of the sand diameter was investigated in the third series. The experimental results showed that: All collectors covered with sand had higher efficiency than those without. It was noticed that, for a fixed mass of sand (given thickness of the sand layer), the improvement of the collector was inversely proportional to the sand particle diameters. The maximum efficiency approximates 62.1% for a particle diameter 0.063 mm, compared to 41.71% for a diameter 0.250 mm.The efficiency of the collector for a fixed particle diameter increases with the increase in the thickness of the sand layer. The collector with thickness sand layer 0.84 mm gave the best efficiency of 46.14% compared to 27.8% for 0.28 mm of thickness sand layer. 相似文献