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1.
An experimental investigation was carried out on the boiling heat transfer characteristics of water and R-11 on the outside of a horizontal heated tube in narrow spaces. Two kinds of heat transfer surfaces (roll-worked and smooth surfaces) were tested. The test section consisted of a narrow annular space formed by enclosing the heated tube in an isolated concentric outer tube with two horizontal slats on the top and bottom. The nucleate boiling heat transfer characteristics were investigated experimentally at atmospheric pressure. The experimental results indicated that a single roll-worked tube in bulk liquid showed better boiling heat transfer than a single smooth tube. In the narrow spaces, the boiling heat transfer coefficients for the smooth tube were considerably enhanced when the gap size was so selected as to take an optimum value. There was no clear optimum gap size for heat transfer enhancement for the roll-worked tube in the narrow spaces. Enhancement of boiling heat transfer in the narrow spaces for the roll-worked tube was not clearly observed in this experiment. Finally, the critical heat flux (CHF) for boiling heat transfer in narrow spaces can be predicted by using a proposed CHF correlation. 相似文献
2.
《Heat Recovery Systems and CHP》1994,14(5):507-515
In the frame of the JOULE 1 R&D programme of the Commission of the European Communities a project has been carried out on enhanced evaporation heat transfer surfaces. A specific investigation has been realised on refrigerant oil mixtures boiling in a planar confined space.An experimental investigation of the boiling phenomenon in the confined space between a 30 mm wide × 120 mm high, heated plate and an opposing, adiabatic plate was carried out. The heated surface was made of a copper-aluminium-nickel alloy (Ra = 1 micrometer) and a saturated R-113/SUNISO 3GS oil mixture at atmospheric pressure was used as the boiling fluid.The maximum heat flux tested was approximately 90% of CHF. The parameters investigated were the gap size (1–5 mm) and the oil concentration (1–7% by weight). It was again observed that confinement does not improve the nucleate boiling performance of pure R-113 in any significant way, whereas the CHF decreases with decreasing gap size. In addition, while the presence of oil was observed to have only a relatively minor effect on low flux nucleate boiling, it caused a serious degradation of the high flux boiling performance. This deterioration increased with increasing oil concentration and was more severe for smaller gap sizes. However, for a given gap size, the CHF increased with increasing oil concentration accompanied by increasingly larger surface superheats. 相似文献
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The influence of nucleation on the flow boiling heat transfer coefficient of R-134a/R-290/R-600a refrigerant mixture is experimentally
studied in a smooth horizontal tube of 12.7 mm diameter. The heat transfer coefficients are experimentally measured for stratified
flow patterns under a varied heat flux condition; a condition found in the evaporator of refrigerators and deep freezers.
The experiments are conducted in a counter-current heat exchanger test section. By regulating the flow rate and inlet temperature
of acetone, which is the heating fluid flowing in the outer tube, a varied heat flux is provided to the refrigerant flowing
in the inner tube. The refrigerant mass flow rate is fixed between 3 and 5 g s−1 and its inlet temperature between −8.59 and 5.33°C, which corresponds to a pressure of 3.2 to 5 bar. The significance of
nucleate boiling prevailing in the above-mentioned evaporators is highlighted. The experimental heat transfer coefficients
are also compared with well known heat transfer correlations. 相似文献
5.
Analytical expressions for nucleate pool boiling heat transfer of nanofluid in the critical heat flux (CHF) region are derived taking into account the effect of nanoparticles moving in liquid based on the fractal geometry theory. The proposed fractal model for the CHF of nanofluid is explicitly related to the average diameter of the nanoparticles, the volumetric nanoparticle concentration, the thermal conductivity of nanoparticles, the fractal dimension of nanoparticles, the fractal dimension of active cavities on the heated surfaces, the temperature, and the properties of the fluid. It is found that the CHF of nanofluid decreases with the increase of the average diameter of nanoparticles. Each parameter of the proposed formulas on CHF has a clear physical meaning. The model predictions are compared with the existing experimental data, and a good agreement between the model predictions and experimental data is found. The validity of the present model is thus verified. The proposed fractal model can reveal the mechanism of heat transfer in nanofluid. 相似文献
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Experimental investigation into the pool boiling heat transfer of aqueous based γ-alumina nanofluids
This paper is concerned about pool boiling heat transfer using nanofluids, a subject of several investigations over the past few years. The work is motivated by the controversial results reported in the literature and the potential impact of nanofluids on heat transfer intensification. Systematic experiments are carried out to formulate stable aqueous based nanofluids containing γ-alumina nanoparticles (primary particle size 10–50 nm), and to investigate their heat transfer behaviour under nucleate pool boiling conditions. The results show that alumina nanofluids can significantly enhance boiling heat transfer. The enhancement increases with increasing particle concentration and reaches ∼
∼40% at a particle loading of 1.25% by weight. Discussion of the results suggests that the reported controversies in the thermal performance of nanofluids under the nucleate pool boiling conditions be associated with the properties and behaviour of the nanofluids and boiling surface, as well as their interactions. 相似文献
8.
Experimental investigation into the pool boiling heat transfer of aqueous based γ-alumina nanofluids
This paper is concerned about pool boiling heat transfer using nanofluids, a subject of several investigations over the past few years. The work is motivated by the controversial results reported in the literature and the potential impact of nanofluids on heat transfer intensification. Systematic experiments are carried out to formulate stable aqueous based nanofluids containing γ-alumina nanoparticles (primary particle size 10–50 nm), and to investigate their heat transfer behaviour under nucleate pool boiling conditions. The results show that alumina nanofluids can significantly enhance boiling heat transfer. The enhancement increases with increasing particle concentration and reaches ∼
∼40% at a particle loading of 1.25% by weight. Discussion of the results suggests that the reported controversies in the thermal performance of nanofluids under the nucleate pool boiling conditions be associated with the properties and behaviour of the nanofluids and boiling surface, as well as their interactions.This revised version was published online in August 2005 with a corrected issue number. 相似文献
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The nucleate pool boiling heat transfer data on a smooth flat surface were measured for three binary mixtures of HC600a/HFC134a, HC600a/HC290, and HC600a/HFC23. Much effort was made to investigate the influence of the boiling range on the pool-boiling heat transfer performance. From the experimental results, the HC600a/HFC23 mixture with a wide boiling range showed lower heat transfer coefficients (HTCs) than the mixture with a narrow boiling range such as HC600a/HFC134a and HC600a/HC290 systems. The measured data were also compared with the results predicted by five well-known correlations. It can be found that the average deviation is less than 25% for mixtures with narrow boiling ranges, but a larger deviation for mixtures with wide boiling ranges. 相似文献
10.
实验研究了高油浓度的制冷剂/油混合物在泡沫金属加热表面池沸腾换热特性。使用三种泡沫铜作为加热表面,其参数分别为10ppi/90%孔隙率、10 ppi/95%孔隙率和30 ppi/98%孔隙率,厚度均为10 mm。制冷剂为R113,润滑油为VG68,油浓度为0%~40%。实验结果表明,泡沫金属总是强化池沸腾换热,换热系数最多提高450%;润滑油恶化制冷剂在泡沫金属加热表面池沸腾换热,换热系数最多降低90%。开发了高油浓度的制冷剂/油混合物在泡沫金属加热表面池沸腾换热关联式,预测值与95%的实验值误差在±30%以内。 相似文献
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Experimental results concerning pool film boiling on a wire under the action of an externally imposed electric field are reported. The working fluid was saturated R113 at atmospheric pressure, the heaters were platinum wires of 0.2, 0.3, and 0.6 mm diameter. An electrostatic field of cylindrical geometry was created around the wire by means of a 60-mm-diameter cylindrical cage in order to assess electrohydrodynamic (EHD) effects on boiling. Voltages up to 15 kV d.c. were applied. The results showed that two different film boiling regimes, separated by an additional boiling crisis, can exist in the presence of an electric field. The first regime, at low wire superheat, is strongly influenced by the electric field, showing a remarkable heat transfer enhancement with increasing voltage. The second one, at higher superheat, is weakly dependent on the field strength and almost coincident with the zero field one. The two film boiling regimes are separated by a transition characterized by a hysteresis cycle, similar to the one between nucleate boiling and first film boiling regime. 相似文献
13.
Sarit K. Das G. Prakash Narayan Anoop K. Baby 《Journal of nanoparticle research》2008,10(7):1099-1108
Pool boiling heat transfer using nanofluids (which are suspensions of nano-sized particles in a base fluid) has been a subject
of many investigations and incoherent results have been reported in literature regarding the same. In the past, experiments
were conducted in nucleate pool boiling with varying parameters such as particle size, concentration, surface roughness etc.
and all sort of results ranging from heat transfer enhancement, deterioration and no effect were reported. This work tries
to segregate a survey on pool boiling of nanofluids with respect to particle concentration. This is due to the fact that a
major drift in heat transfer behavior is observed at higher and lower particle concentration. But upon deep perusal it has
been found that deterioration in heat transfer coefficient are mainly observed at higher particle concentrations (4–16% by
weight) and enhancements mainly at lower particle concentrations (0.32–1.25% by weight). Moreover, the relative size of the
particle with respect to the surface roughness of the heating surface seems to play an important role in understanding the
boiling behaviour. Also, recent works have reported that change in ‘surface wetting’ of the heating surface due to nanofluids
and the formation of a porous layer modifiying nucleation site density can be of importance in predicting nucleate pool boiling
characteristics of nanofluids. In the present paper, attempts are made to make systematic analysis of results in literature
and try to bring out a common understanding of the results in literature. 相似文献
14.
This study presents new data on nucleate boiling heat transfer obtained in compact horizontal tube bundles with small tube gaps. The experiment investigates the heat transfer enhancement effects by the restricted spaces comprising the compact tube bundles and the enhanced heat transfer tubes for nucleate boiling heat transfer of R-11 at atmospheric pressure. A roll-worked tube was used as a new type of enhanced heat transfer tube. The experimental results show that the small tube gaps can greatly enhance boiling heat transfer in a smooth tube bundle, while enhancement effects of small gaps were not quite significant for the enhanced tube bundle. There is a compound effect from the enhanced surface and the restricted space only for the enhanced tube bundle with the tube gap of 0.5 mm. The effects of the tube positions within both compact tube bundles on the boiling heat transfer were minor. 相似文献
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Pool boiling characteristics on horizontal tubes with diameter lying between wires and industrial tubes have been investigated experimentally. Boiling experiments are carried out at near atmospheric pressures with water and R-123 as boiling liquids. The experimental results show quite a different boiling behavior compared to larger tubes or plates. The commonly used correlations are found to be ineffective over this range of diameters. A developing sliding bubble mechanism can be attributed to such behavior which shows a strong diameter effect. The heat transfer is found to increase with diameter which is contrary to that on industrial size tubes. Useful boiling data are presented in this range of diameters in which experimental data are scarce. The need for more investigations is stressed in view of emerging applications in this area. 相似文献
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The characteristics of boiling and critical heat flux (CHF) behavior of nano-fluids with alumina and silver nano-particles
suspended in de-ionized water (pure water) were studied with circular plate heaters in the present study. Enhancements of
CHF in nano-fluids in the wide range of particle sizes and concentrations were compared with those in pure water. Also, the
effects of the particle deposition on CHF enhancement were investigated. All experiments were performed at the atmospheric
pressure condition. The results show that the measured boiling curves in nano-fluids were shifted to the right and CHF were
significantly enhanced for different nano-particle sizes and concentrations. The CHF of nano-fluids was increased as the size
of the nano-particles decreased. On the other hand, nano-particle concentration value showing the maximum CHF had a critical
value. In each pool boiling experiment of nano-fluids, nano-particles were deposited on the heater surface. Assuming that
this phenomenon caused the CHF enhancement, pool boiling experiments of pure water were carried out with these nano-particle
deposited heaters. The results of these tests were similar to those of the test of the nano-fluids for the CHF enhancement.
The main cause of CHF enhancement was found to be the change of the heater surface structure. In order to analyze boiling
phenomena of pure water and Al2O3 nano-fluids, boiling process was visualized by using a high speed camera. 相似文献
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This paper deals with experimental results on flowboiling heat transfer of liquid moving in an annular channel with unilateral
central heating under the conditions of a significant effect of capillary forces on the flow modes and heat transfer. Experiments
were carried out on boiling freon R318C in an annular channel with a gap of 0.95 mm and transparent outer wall. The inner
wall was heated by the electric current. The local heat transfer coefficients and flow modes are presented. The critical film
thickness corresponding to suppression of nucleate boiling was determined. 相似文献