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以张家口市某风电场作为实验场地,利用激光多普勒雷达(WindMast WP350和Wind 3D6000分别扫描风力机的来流和尾流)对风力机的尾流以及风场风况进行测量,并分析湍流强度变化以及探究湍流强度对风力机尾流特性的影响。研究发现,随时间改变的大气环境对湍流强度的影响较为明显,而高度对湍流强度的影响较小;湍流强度对风力机尾流有较大影响,湍流强度越大,则尾流恢复越快且尾流宽度和深度越小;随着沿轮毂中心轴向距离的增加,尾流速度衰减在尾流发展4D~6D(D表示风力机直径长度)后加速下降。 相似文献
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以台风烟花过境沿海陆上风电场期间,风电场内特别是风电机组位置的风速、风向和湍流强度的微尺度分布及其随时间的变化为研究对象,基于中尺度WRF模式的模拟结果建立CFD计算域的边界条件,建立台风大气边界层风速、风向廓线参数化模型,以及考虑中尺度热带气旋和台风边界层内卷效应的风场CFD计算模型。算例结果表明,所建立的台风大气边界层风场CFD计算模型可反映台风大气涡旋在风电场微尺度范围的流动特性,风电机组轮毂点的计算风速和实测的机舱风速符合较好,表明所研究的方法可进一步应用于台风影响地区风电场内风电机组台风风险的精细化评估,开展考虑台风风险的微观选址优化等。 相似文献
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收集了2003年以来88个测风塔29个热带气旋(TC)影响期间逐日10 min测风资料,研究发现:TC中心及附近湍流强度超过IEC标准A类,特别是风速达16~29 m/s时最大可超出标准0.04,IEC标准正常湍流模型(NTM)不能完全描述台风影响下中心及附近区域的情形。TC中心及附近湍流模型NTM表达式应为σ95%=Iref(0.884V)hub+8.172,湍流强度A、B、C类分别定义为0.18、0.16和0.14,更高级别的湍流强度类定义为0.20。 相似文献
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台风对风电场的影响有正面也有负面的,它给部分风电场带来良好发电效益的同时,也对直接登陆区域的风电场造成严重的危害。通过台风对风电场的危害分析,阐述了近海风电场在设计选型时必须考虑的问题,并提出了风电场生产阶段防范台风危害的对策。 相似文献
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实验研究5×3对齐式排布的风电场湍流积分长度(Λ)的演变规律,主流向和展向机组间距分别为10倍和2.5倍风力机直径(dT)。采用一维热线测速仪获得风电场不同位置的高分辨率流场数据。分析结果表明,Λ在水平面上呈近似对称分布,而在竖直方向上由于受边界层影响呈非对称分布。受旋转风力机的影响,Λ在风力机后方发生剧烈的衰减,而随着外部流场大尺度湍流微团的不断渗入,Λ随下游距离的增加逐步恢复。特别地,从第3排风力机尾流开始,风电场流场基本呈现稳定平衡状态,下游风力机前端位置的Λ约为整个风电场来流湍流积分长度的60%。在风电场上方约0.5 dT以上高度的流场结构受风电场影响较小。 相似文献
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结合制动盘理论与CFD方法,采用FLUENT软件对置于有限面积的风电场内的9台风力机尾流相互干扰情况进行数值模拟。风电场内风力机机组呈梅花型排布,考虑入流角分别为0°、15°和30°代表风力机的偏航现象,利用FLUENT提供的FAN边界将风力机风轮简化为无厚度的产生压力跃降的制动盘,采用N-S方程求解整个风电场的流场分布。该文给出流场的速度分布、涡量分布及风力机机组周围的风能密度与湍流强度分布,反映了上游风力机机组的尾流会对下游机组的流场产生干扰的现象。通过对风电场和风力机的成功模拟表明,制动盘理论结合CFD的方法适用于风电场和风力机的流场模拟,可为风电场微观选址和风力机排布提供参考,且计算量远小于完全数值模拟方法。 相似文献
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开发了风力机地震仿真平台SAF(Seismic Analysis Framework),以DTU 10 MW海上风力机为研究对象,建立其地震激励下的动力仿真模型,分析4种水深(20~50 m)时20组不同强度地震、额定风速湍流风与波浪流联合作用下风力机塔架动力响应。研究表明:地震作用对横向塔顶位移及横向平面内的塔基弯矩影响较大,来流方向塔顶位移及来流平面内的塔基弯矩主要受湍流风影响;在存在地震激励时,塔架不同高度处位移、剪切力及弯矩响应均大于湍流风与波浪流作用时;地震强度较弱时,不同水深处风力机塔顶位移与弯矩差距较小,但塔基弯矩随着水深的增大而增大;地震强度较大时,水深对风力机塔顶位移与塔基弯矩影响很大,相同地震强度的响应深水大于浅水。 相似文献
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Woody biomass in Finland and Sweden comprises mainly four wood species: spruce, pine, birch and aspen. To study the ash, which may cause problems for the combustion device, one tree of each species were cut down and prepared for comparisons with fuel samples. Well-defined samples of wood, bark and foliage were analyzed on 11 ash-forming elements: Si, Al, Fe, Ca, Mg, Mn, Na, K, P, S and Cl. The ash content in the wood tissues (0.2–0.7%) was low compared to the ash content in the bark tissues (1.9–6.4%) and the foliage (2.4–7.7%). The woods’ content of ash-forming elements was consequently low; the highest contents were of Ca (410–1340 ppm) and K (200–1310), followed by Mg (70–290), Mn (15–240) and P (0–350). Present in the wood was also Si (50–190), S (50–200) and Cl (30–110). The bark tissues showed much higher element contents; Ca (4800–19,100 ppm) and K (1600–6400) were the dominating elements, followed by Mg (210–2400), P (210–1200), Mn (110–1100) and S (310–750), but the Cl contents (40–330) were only moderately higher in the bark than in the wood. The young foliage (shoots and deciduous leaves) had the highest K (7100–25,000 ppm), P (1600–5300) and S (1100–2600) contents of all tissues, while the shoots of spruce had the highest Cl contents (820–1360) and its needles the highest Si content (5000–11,300). This paper presented a new approach in fuel characterization: the method excludes the presence of impurities, and focus on different categories of plant tissues. This made it possible to discuss the contents of ash element in a wide spectrum of fuel-types, which are of large importance for the energy production in Finland and Sweden. 相似文献
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《热能动力工程》2014,(5)
正1 ABSTRACT To reduce the effect of global warming on our climate,the levels of CO2emissions should be reduced.One way to do this is to increase the efficiency of electricity production from fossil fuels.This will in turn reduce the amount of CO2emissions for a given power output.Using US practice for efficiency calculations,then a move from a typical US plant running at 37%efficiency to a 760℃/38.5 MPa(1 400/5 580 psi)plant running at 48%efficiency would reduce CO2emissions by 170kg/MW.hr or 25%. 相似文献
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The purpose of this paper is to illustrate the advantages of the direct surface-curvature distribution blade-design method, originally proposed by Korakianitis, for the leading-edge design of turbine blades, and by extension for other types of airfoil shapes. The leading edge shape is critical in the blade design process, and it is quite difficult to completely control with inverse, semi-inverse or other direct-design methods. The blade-design method is briefly reviewed, and then the effort is concentrated on smoothly blending the leading edge shape (circle or ellipse, etc.) with the main part of the blade surface, in a manner that avoids leading-edge flow-disturbance and flow-separation regions. Specifically in the leading edge region we return to the second-order (parabolic) construction line coupled with a revised smoothing equation between the leading-edge shape and the main part of the blade. The Hodson–Dominy blade has been used as an example to show the ability of this blade-design method to remove leading-edge separation bubbles in gas turbine blades and other airfoil shapes that have very sharp changes in curvature near the leading edge. An additional gas turbine blade example has been used to illustrate the ability of this method to design leading edge shapes that avoid leading-edge separation bubbles at off-design conditions. This gas turbine blade example has inlet flow angle 0°, outlet flow angle −64.3°, and tangential lift coefficient 1.045, in a region of parameters where the leading edge shape is critical for the overall blade performance. Computed results at incidences of −10°, −5°, +5°, +10° are used to illustrate the complete removal of leading edge flow-disturbance regions, thus minimizing the possibility of leading-edge separation bubbles, while concurrently minimizing the stagnation pressure drop from inlet to outlet. These results using two difficult example cases of leading edge geometries illustrate the superiority and utility of this blade-design method when compared with other direct or inverse blade-design methods. 相似文献
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A chemical reactor for the steam-gasification of carbonaceous particles (e.g. coal, coke) is considered for using concentrated solar radiation as the energy source of high-temperature process heat. A two-phase reactor model that couples radiative, convective, and conductive heat transfer to the chemical kinetics is applied to optimize the reactor geometrical configuration and operational parameters (feedstock's initial particle size, feeding rates, and solar power input) for maximum reaction extent and solar-to-chemical energy conversion efficiency of a 5 kW prototype reactor and its scale-up to 300 kW. For the 300 kW reactor, complete reaction extent is predicted for an initial feedstock particle size up to 35 μm at residence times of less than 10 s and peak temperatures of 1818 K, yielding high-quality syngas with a calorific content that has been solar-upgraded by 19% over that of the petcoke gasified. 相似文献
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As part of a pilot study investigating the role of microorganisms in the immobilisation of As, Sb, B, Tl and Hg, the inorganic geochemistry of seven different active sinter deposits and their contact fluids were characterised. A comprehensive series of sequential extractions for a suite of trace elements was carried out on siliceous sinter and a mixed silica-carbonate sinter. The extractions showed whether metals were loosely exchangeable or bound to carbonate, oxide, organic or crystalline fractions. Hyperthermophilic microbial communities associated with sinters deposited from high temperature (92–94°C) fluids at a variety of geothermal sources were investigated using SEM. The rapidity and style of silicification of the hyperthermophiles can be correlated with the dissolved silica content of the fluid. Although high concentrations of Hg and Tl were found associated with the organic fraction of the sinters, there was no evidence to suggest that any of the heavy metals were associated preferentially with the hyperthermophiles at the high temperature (92–94°C) ends of the terrestrial thermal spring ecosystems studied. 相似文献
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The physical aspects of the activation energy, in higher and high temperatures, of the metal creep process were examined. The research results of creep-rupture in a uniaxial stress state and the criterion of creep-rupture in biaxial stress states, at two temperatures, are then presented. For these studies creep-rupture, taking case iron as an example the energy and pseudoenergy activation was determined. For complex stress states the criterion of creep-rupture was taken to be Sdobyrev's, i.e. σred = σ1 β + (1 − β)σi, where: σ1-maximal principal stress, σi-stress intensity, β-material constant (at variable temperature β = β(T)). The methods of assessment of the material ageing grade are given in percentages of ageing of new material in the following mechanical properties: 1) creep strength in uniaxial stress state, 2) activation energy in uniaxial stress state, 3) criterion creep strength in complex stress states, 4) activation pseudoenergy in complex stress states. The methods 1) and 3) are the relatively simplest because they result from experimental investigations only at nominal temperature of the structure work, however, for methods 2) and 4) it is necessary to perform the experimental investigations at least at two temperatures. 相似文献
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Jaime Massanet-Nicolau Alan Guwy Richard Dinsdale Giuliano Premier Sandra Esteves 《International Journal of Hydrogen Energy》2010
Hydrogen was produced from primary sewage biosolids via mesophilic anaerobic fermentation in a continuously fed bioreactor. Prior to fermentation the sewage biosolids were heated to 70 °C for 1 h to inactivate methanogens and during fermentation a cellulose degrading enzyme was added to improve substrate availability. Hydraulic retention times (HRT) of 18, 24, 36 and 48 h were evaluated for the duration of hydrogen production. Without sparging a hydraulic retention time of 24 h resulted in the longest period of hydrogen production (3 days), during which a hydrogen yield of 21.9 L H2 kg−1 VS added to the bioreactor was achieved. Methods of preventing the decline of hydrogen production during continuous fermentation were evaluated. Of the techniques evaluated using nitrogen gas to sparge the bioreactor contents proved to be more effective than flushing just the headspace of the bioreactor. Sparging at 0.06 L L min−1 successfully prevented a decline in hydrogen production and resulted in a yield of 27.0 L H2 kg−1 VS added, over a period of greater than 12 days or 12 HRT. The use of sparging also delayed the build up of acetic acid in the bioreactor, suggesting that it serves to inhibit homoacetogenesis and thus maintain hydrogen production. 相似文献