Experimental investigations on the effect of the spiral helical fins & flow channel routing inside flowing water stream on the heat exchanger performance in tropical environment

Author(s):  
Afrasyab Khan ◽  
Khairuddin Sanaullah ◽  
Andrew Regai Henry Rigit ◽  
Mohammed Zwawi ◽  
Mohammed Algarni ◽  
...  
Author(s):  
R. W. Anderson ◽  
D. L. Senecal

A problem was presented to observe the packing densities of deposits of sub-micron corrosion product particles. The deposits were 5-100 mils thick and had formed on the inside surfaces of 3/8 inch diameter Zircaloy-2 heat exchanger tubes. The particles were iron oxides deposited from flowing water and consequently were only weakly bonded. Particular care was required during handling to preserve the original formations of the deposits. The specimen preparation method described below allowed direct observation of cross sections of the deposit layers by transmission electron microscopy.The specimens were short sections of the tubes (about 3 inches long) that were carefully cut from the systems. The insides of the tube sections were first coated with a thin layer of a fluid epoxy resin by dipping. This coating served to impregnate the deposit layer as well as to protect the layer if subsequent handling were required.


1998 ◽  
Vol 37 (12) ◽  
pp. 255-261 ◽  
Author(s):  
Mark Johnson

A simple, laser-based reflectometer is described for the measurement of water turbidity via 180° optical scattering. Applications exist both in clean source waters (0-1000NTU) with a minimum detectable turbidity better than 1NTU, and in dense wastewater primary-clarifier sludges. The non-contact measurement is performed from a distance at least up to 10m, substantially avoiding the usual window fouling problems of optical instruments. By measuring directly in the process, through a free water surface or on the side of a flowing water stream, the difficulties of transporting sample to the instrument are also avoided. Extensions to be described allow measurement also of water colour.


2014 ◽  
Vol 67 ◽  
pp. 02046 ◽  
Author(s):  
Pavel Charvat ◽  
Josef Stetina ◽  
Ondrej Pech ◽  
Lubomir Klimes ◽  
Milan Ostry

Energies ◽  
2019 ◽  
Vol 12 (17) ◽  
pp. 3276 ◽  
Author(s):  
Jan Wajs ◽  
Michał Bajor ◽  
Dariusz Mikielewicz

In this paper a patented design of a heat exchanger with minijets, with a cylindrical construction is presented. It is followed by the results of its systematic experimental investigations in the single-phase convection heat transfer mode. Based on these results, validation of selected correlations (coming from the literature) describing the Nusselt number was carried out. An assessment of the heat exchange intensification level in the described heat exchanger was done through the comparison with a shell-and-tube exchanger of a classical design. The thermal-hydraulic characteristics of both units were the subjects of comparison. They were constructed for the identical thermal conditions, i.e., volumetric flow rates of the working media and the media temperatures at the inlets to the heat exchanger. The experimental studies of both heat exchangers were conducted on the same test facility. An increase in the heat transfer coefficients values for the minijets heat exchanger was observed in comparison with the reference one, whereas the generated minijets caused greater hydraulic resistance. Experimentally confirmed intensification of heat transfer on the air side, makes the proposed minijets heat exchanger application more attractive, for the waste heat utilization systems from gas sources.


1983 ◽  
Vol 23 (01) ◽  
pp. 99-114 ◽  
Author(s):  
Alfredo Arriola ◽  
G. Paul Willhite ◽  
Don W. Green

Abstract An experimental apparatus was developed to study trapping and mobilization of oil drops in a capillary of square cross section [100 microns×100 microns (100µm×100µm)] having a constriction also approximately square in shape. The throat of the constructions had dimensions of about 10 microns (10µm) on a side. Experiments to investigate trapping consisted of injecting a drop of nonwetting phase liquid "oil") into a flowing water stream (wetting phase). A nonane/water system was used for most of the experiments. Pre-equilibrated alcohol/water systems were used to study effects of interfacial tension (IFT). A drop was displaced toward the constriction by the flowing water. The behavior of the drop as it approached and was trapped by the constriction or as it moved through the constriction was observed as a function of flow rate, drop length, and IFT between the water and nonwetting liquid. Mobilization by surfactants was investigated by conducting a series of displacement experiments in the capillary cell. In each experiment, an oil drop about 890 µm in length was trapped at the constriction by brine (10,100 ppm NaCl) flowing at an average pore velocity of 1.3 ft/D (0.4 m/d). A chemical slug containing surfactant and cosurfactant was injected into the capillary cell and displaced toward the trapped oil drop by the brine. Observations, measurements, photographs, and movies were made using a microscope. Provision also was made to monitor the pressure drop across the constriction. Two phenomena were observed in the trapping experiments. First, the position of a trapped, stable drop relative to the throat depended on IFT, displacing liquid velocity, and oil drop size. Second, by increasing the main stream velocity, increasing the drop size, or decreasing the IFT, the front interface of a stable drop could be caused to move further into the throat of the constriction until the drop became unstable and a "snap-off" of the drop started. In this snap-off process, small drops of oil broke away from the main drop and moved through the constriction. Eventually the oil drop achieved a size where the snap-off stopped. Data were correlated empirically to define conditions under which a drop was stable as well as those where snap-off occurred. Data from the mobilization experiments allowed two mechanisms to be identified. In Mechanism 1, minute quantities of the surfactant and/or cosurfactant were carried ahead of the main surfactant slug by brine that bypassed the slug. This reduced the IFT between the oil and brine. The oil drop moved further into the constriction and a snap-off process ensued. Mechanism 2 occurred when a sharp interface of the surfactant slug contacted the trailing edge of a nonane drop that was either trapped or in a snap-off process. A series of events that mobilized the drop occurred over a very short time period (<4.0 seconds). The events included rupture of the drop interface, rolling motions inside the drop with resulting emulsification, and passage of the emulsified drop through the pore constriction without snap-off. The emulsification reflected hydrodynamic instabilities - i.e., a Marangoni effect.


2014 ◽  
Vol 592-594 ◽  
pp. 1438-1442
Author(s):  
Suman Gupta ◽  
P. Chellapandi

The tube to tubesheet joint in a heat exchanger is one of the most critical joint and it has to meet stringent requirements as it provides the main barrier between the tube side and shell side fluids of heat exchanger. This paper discusses the various kinds of tube to tubesheet joint in heat exchanger, joint configuration adopted in PFBR IHX, structural analysis of IHX, axial load distribution in tube rows and experimental verification in order to evaluate allowable strength of tube to tubesheet joint. In IHX, tubes in outer rows are under tension and maximum stresses are below the allowable stresses in the tubes. Detailed experimental investigations result shows that the rolled and welded joint is stronger than the basic strength of the tube material. However, the allowable tensile strength of the joint under mechanical loading considered is 0.95 times the allowable value for tubes as per ASME.


1994 ◽  
Vol 29 (4) ◽  
pp. 211-217
Author(s):  
C. B. Sobhan ◽  
K. T. Mohammed Kutty ◽  
M. Hannan ◽  
P. Krishtaiah

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