共查询到20条相似文献,搜索用时 46 毫秒
1.
《内燃机工程》2014,(4)
针对某发动机设计了冷却水套并运用三维数值仿真技术对该水套冷却性能进行仿真分析发现,缸盖排气侧高温区的流场分布极不均匀,冷却液未能实现对缸体的完全绕流冷却,缸体水套存在局部低流速区。进一步分析发现,分水孔对流场分布具有很大的影响,并据此修改分水孔方案。仿真结果表明:改进方案缸盖高温区流场分布比较均匀,冷却液也实现了对缸体的完全绕流冷却,消除了原水套中的低流速区,高温区局部平均流速1.7 m/s,传热系数12 000 W/(m~2·K),水套平均流速大于0.5 m/s,冷却性能得到了改善。最后分析了金属纳米流体的强化换热效果,结果表明:浓度5%的铜水纳米流体局部传热系数比纯水提高了41%,效果明显的同时所需泵功也有所增加。 相似文献
2.
3.
车用柴油机冷却水套的CFD分析与优化 总被引:1,自引:0,他引:1
利用三维造型软件Pro/E对某一六缸柴油机冷却水套建立模型,并用CFD软件Fluent进行模拟计算,得到整机冷却水套内冷却液速度分布、压力损失以及各缸流量分布等信息。分析结果表明:缸盖水套虽满足设计要求,但缸体水套存在冷却不足、均匀性差的缺陷。改进方案的模拟分析表明,改进后缸体水套冷却更为均匀,流动性能比原机水套有明显的改善。 相似文献
4.
5.
6.
7.
发动机冷却水套的CFD分析是目前发动机缸体开发有效计算分析手段,具有开发准确性高、速度快的特点。在设计开发过程中,可以先不用制造实体样机,而是先通过CFD分析,进行缸盖水套的优化。尤其是在处理发动机热负荷较高的燃烧室及排气道周围有良好的冷却液流动。尤其在设计开发过程中,在没有样机水流试验数据的条件下,手段为发动机结构设计提供了强大的技术支持。本文利用CFD分析设计4102型柴油机发动机冷却水套,成功分析并优化了发动机缸盖的水套结构,保证在发动机热负荷,而压力损失相对较低。确定出了流动性较好且压降低的水套,确保了发动机有良好的机内冷却。 相似文献
8.
基于CFD的船用柴油机缸体水套设计 总被引:8,自引:0,他引:8
利用数值模拟对6170型船用柴油机的冷却水套进行了冷却性能研究,优化设计了缸体冷却水套.对原机缸体冷却水套内冷却水的流场分布、冷却水套内壁面换热系数、各缸冷却均匀性和压力损失进行了分析.计算结果表明:原机缸体水套上部存在冷却强度不足、冷却均匀性差的缺陷,不能满足缸套冷却要求.通过计算提出了提高缸体上部冷却强度及改善冷却均匀性的优化设计方案,从而满足了气缸套的冷却需要,确保了发动机工作的可靠性. 相似文献
9.
本文利用CFD和FEM耦合计算的方法,较准确的确定缸盖冷却水腔的热边界条件,对普及型欧-Ⅲ排放柴油机的冷却水腔和缸盖温度场进行了模拟。文章对冷却水腔的整体流动均匀性和整机压力损失进行了分析评估,并对缸盖火力面、喷油器安装孔和排气道周围冷却水腔的冷却情况进行了详细分析。模拟计算结果表明:冷却水腔的流动均匀性和压力损失可以满足使用要求;流经火力面和排气道周围水腔的冷却液流量分配合理;缸盖火力面、喷油器安装孔和排气道周围水腔冷却良好。 相似文献
10.
针对卧式柴油机强制冷却闭式循环系统水套结构,试验研究了不同工况下水套入口流量及关键点的温度和压力。采用计算流体动力学(CFD)三维模拟的方法建立了冷却水流动仿真模型,并进行了试验验证。设计了冷却水套结构参数正交方案,通过CFD模拟分析了水泵出水流量、公共水腔截面形状和面积、缸体及缸盖入水孔的设置和分布等水套结构参数对冷却水流动的影响关系。研究结果表明:卧式柴油机缸体入水孔截面积和布置对缸体水套冷却水流动、冷却效果和冷却均匀性有很大的影响;卧式柴油机缸盖入水孔的位置、孔数和截面积等结构参数对缸盖水套的冷却水流动、冷却效果、冷却均匀性及进/排气侧的冷却分布等均有很大的影响。 相似文献
11.
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
12.
《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
13.
14.
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
15.
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
16.
17.
18.
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
19.
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
20.
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