共查询到16条相似文献,搜索用时 140 毫秒
1.
采用SST k-w湍流模型对超临界CO2/丙烷混合工质水平管内的传热特性进行数值模拟研究。管径d=4 mm,加热段L2=800 mm;混合工质浓度配比为100/0、95/5、90/10、85/15、80/20、75/25;质量流速为150~250 kg·m?2·s?1;热流密度为30~40 kW·m?2,入口温度293 K,入口压力7.5~30 MPa。随着丙烷浓度的增加,CO2/丙烷二元混合工质的临界压力降低,临界温度升高,丙烷浓度从5%增加到25%,换热系数峰值降低6.19%~31.45%,但增加丙烷浓度可提高拟临界温度后的换热效果。P=7.5~8.5 MPa,换热系数有明显峰值;P=20~30 MPa,换热系数变化规律无明显峰值,并随压力的升高而减小。混合工质的换热系数随质量流速的增大而增大。同一流体温度所对应的换热系数,随着热流密度的增加而减小。 相似文献
2.
采用SST k-w湍流模型对超临界CO2/丙烷混合工质水平管内的传热特性进行数值模拟研究。管径d=4 mm,加热段L2=800 mm;混合工质浓度配比为100/0、95/5、90/10、85/15、80/20、75/25;质量流速为150~250 kg·m?2·s?1;热流密度为30~40 kW·m?2,入口温度293 K,入口压力7.5~30 MPa。随着丙烷浓度的增加,CO2/丙烷二元混合工质的临界压力降低,临界温度升高,丙烷浓度从5%增加到25%,换热系数峰值降低6.19%~31.45%,但增加丙烷浓度可提高拟临界温度后的换热效果。P=7.5~8.5 MPa,换热系数有明显峰值;P=20~30 MPa,换热系数变化规律无明显峰值,并随压力的升高而减小。混合工质的换热系数随质量流速的增大而增大。同一流体温度所对应的换热系数,随着热流密度的增加而减小。 相似文献
3.
针对超临界CO2空冷换热器中存在的非均匀传热问题,本文利用数值模拟计算了水平空冷翅片管中管壁热流分布规律及超临界CO2在非均匀冷却时的换热特性,同时分析了非均匀冷却工况下不均匀度、质量流量和浮升力等因素对换热规律的影响。结果表明:翅片管热流密度沿周向管壁位置呈现显著的不均匀分布,且不均匀度随风速增大而增大;超临界CO2非均匀冷却的平均换热系数在远离准临界点时高于均匀冷却,靠近准临界点时低于均匀冷却;非均匀冷却与均匀冷却的差异随不均匀度、质量流量增大而增大。CO2在准临界点处的非线性物性变化与浮升力作用是造成两者差异的主要原因。 相似文献
4.
5.
《工程热物理学报》2020,(7)
CO_2/DME(Dimethyl ether二甲醚)混合工质作为制冷剂既可以降低CO_2单独使用时过高的工作压力,又可抑制二甲醚的可燃性。针对跨临界热泵系统中制冷剂在超临界压力下放热时复杂的传热性能,本文对超临界CO_2/DME混合工质和超临界CO_2在螺旋管内流动冷却的换热过程进行了数值模拟研究。结果表明,与纯CO_2相比,在高温区CO_2/DME混合工质的换热性能更优;通过比较不同配比的CO_2/DME混合工质的换热特性,得到了不同温度范围对应的换热性能最优的CO_2/DME混合工质配比。此外,对固定质量比的CO_2/DME混合工质,分别分析了不同质量流速和热流密度下的流体温度、壁面温度及传热系数的变化规律,并与纯CO_2传热系数的变化进行了对比。该研究为制冷剂选取及热泵系统中气冷器的优化设计提供了理论依据。 相似文献
6.
7.
非均匀加热条件下内插扭带管强化传热模拟分析 总被引:2,自引:0,他引:2
以水为工作介质,采用欧拉多相流模型和非平衡沸腾模型,当流速在0.3~0.7m·s-1范围内、工作压力为4.5MPa、热流密度为2MW·m-2时,数值模拟了内插扭带管和光管管内流动过冷沸腾传热。对比了两种管道的换热系数、气泡份额、流动速度、流场流线、固体组件温度和压降,分析了内插扭带管的综合性能。结果表明,与光管相比较,内插扭带管的换热系数提高约6%~90%,压降增大约200%~250%,得到流速在0.4~0.6m·s-1范围内时内插扭带管的综合性能评价因子η为1.1~1.3。 相似文献
8.
9.
10.
为了研究超临界CO2(SCO2)在螺旋槽管式换热器中的冷却换热特性,采用数值模拟方法对比研究了不同热流密度下,SCO2在不同通道内流动时冷却换热系数和湍流动能。为了更合理地评价各工况下冷却换热的综合性能,从压降和传热系数角度,提出一个综合评价因子EF。研究结果表明:在SCO2进行冷却换热时,其换热系数主要受定压比热容和湍流动能的影响。当SCO2在内管通道内流动时,换热系数低,但压降更小,故综合评价因子EF较大。同时,在所研究工况中,存在最佳热流密度值为-40 000 W/m2,使EF达到最大值2.001 26,此时SCO2冷却换热综合性能最优。 相似文献
11.
采用RNG k-ε 湍流模型对超临界CO2流体在内径为4 mm, 长度2000 mm, 节距为10 mm, 曲率为0.1的水平螺旋管内的冷却换热进行了数值模拟.研究了质量流量、热流量以及压力对换热系数的影响, 并和超临界CO2在水平直管内的冷却换热进行了对比.研究结果表明, 超临界CO2在水平螺旋管内流动产生的二次流强于水平直管内的二次流, 前者的换热系数大于后者; 换热系数随质量流量的增加而增大; 在似气体区, 换热系数随着热流量的增加而增大, 而在似液体区, 热流量对换热系数几乎没有影响; 换热系数峰值点随着压力的升高而下降, 并向高温区偏移. 相似文献
12.
本文通过实验研究了CO2质量分数为11.39%~70.95%,壁面过冷度为5~25 K,总压力为5~15 kPa的CO2/H2O混合气体自然对流条件下在水平管外的凝结换热规律,结果表明CO2/H2O的凝结换热系数随CO2含量和壁面过冷度的增大而降低,但随总压力的增大而增大。根据实验结果建立了新关联式,将关联式应用到凝汽器的设计计算与分析,且对凝汽器进行了分离特性和经济性分析。 相似文献
13.
Coulombe S. Meunier J.L. 《IEEE transactions on plasma science. IEEE Nuclear and Plasma Sciences Society》1997,25(5):913-918
The importance of having high local cathode spot pressures for the self-sustaining operation of a thermal arc plasma on a cold cathode is theoretically investigated. Applying a cathode sheath model to a Cu cathode, it is shown that cathode spot plasma pressures ranging 7.4-9.2 atm and 34.2-50 atm for electron temperatures of ~1 eV are needed to account for current densities of 109 and 1010 A·m-2, respectively. The study of the different contributions from the ions, the emission electrons, and the back-diffusing plasma electrons to the total current and heat transfer to the cathode spot has allowed us to show the following. 1) Due to the high metallic plasma densities, a strong heating of the cathode occurs and an important surface electric field is established at the cathode surface causing strong thermo-field emission of electrons. 2) Due to the presence of a high density of ions in the cathode vicinity, an important fraction of the total current is carried by the ions and the electron emission is enhanced. 3) The total current is only slightly reduced by the presence of back-diffusing plasma electrons in the cathode sheath. For a current density jtot=109 A·m-2 , the current to the cathode surface is mainly transported by the ions (76-91% of jtot while for a current density jtot = 1010 A·m-2, the thermo-field electrons become the main current carriers (61-72% of jtot). It is shown that the cathode spot plasma parameters are those of a high pressure metallic gas where deviations from the ideal gas law and important lowering of the ionization potentials are observed 相似文献
14.
Hausmann H.L. Mentel J. 《IEEE transactions on plasma science. IEEE Nuclear and Plasma Sciences Society》1990,18(4):708-716
A pure fluorine 10-A DC arc has been operated in an Al2O3 tube of 18 mm diameter at atmospheric pressure. This arc was used to perform radially resolved spectroscopic end-on measurements in the visible and UV-spectral regions. An excitation temperature of 7800 K on the arc axis was determined from the intensity of atomic fluorine lines, and an ion density of 1.7×10 21 m-3 was determined from the half-width of the contamination line H β. A Boltzmann plot of the affinity continuum in the UV-spectral region yields two groups of electrons. A group of hot electrons is characterized by a temperature that agrees with the excitation temperature, and a group of cold electrons has a temperature in accordance to the gas temperature of 4000 K. The absolute intensity of the affinity continuum gives and electron density of 1.3×1020 m-3 on the arc axis, which is lower than the density of both positive and negative ions in the discharge. From the difference between the electron and gas temperature, an elastic collision cross section between the electrons and F-atoms of 2×10-20 m2 is determined 相似文献
15.
Ф ����Ҧ��ë���� �ڣ����Բ� 《核聚变与等离子体物理》2015,35(4):356-360
In order to improve the anti-thermal load and heat dissipation performance of the divertor of EAST, its first wall material is changed to tungsten from graphite. In the structure, outer target adopts the ITER-like monoblock, bracing and cooling structure adopts incorporate cassette. After establishing the cooling structure of EAST tungsten divertor, the flows-solid coupling heat conduction model of water-pipes is used to analyze the heat dissipation situation of outside target in the form of turbulent flow. While the cooling system comes to failure, a series of heat flux value 3MW·m-2, 5MW·m-2, 8MW·m-2, 10MW·m-2 are applied in the hazardous area to analyze transient conditions and real temperature distribution. The results shows that if the water flows at 4m·s-1, the cooling pipes can withstand the heat flux with peak power in 10MW·m-2. It can well meet the needs in heat dissipation of EAST experiment. 相似文献