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Concentric tube heat exchanger

About: Concentric tube heat exchanger is a research topic. Over the lifetime, 5053 publications have been published within this topic receiving 81130 citations.


Papers
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Patent
02 Jan 1991
TL;DR: In this paper, an in situ thermal system for enhanced oil recovery and the like from a subterranean formation is described, where a down hole, fuel fired radiant tube burner of long length is provided to achieve the desired heat patterns within the formation.
Abstract: An in situ thermal system is disclosed for enhanced oil recovery and the like from a subterranean formation. The system pressurizes the formation with water whereupon the entire formation is heated to relatively high temperatures in the absence of gas formation to significantly decrease the viscosity of substantially all the crude in the formation and permit recovery thereof. A down hole, fuel fired radiant tube burner of long length is provided to achieve the desired heat patterns within the formation. The burner includes three concentric, closed end tubes with the innermost tube containing a burner and spaced closely adjacent the intermediate tube. A hole pattern in the innermost and intermediate tube establishes a laminar flow of the burner's products of combustion therebetween which modifies the radiation heat flux pattern so that uniform heat is emitted from the outermost tube along its length.

304 citations

Journal ArticleDOI
TL;DR: In this paper, the delta winglet-type vortex generators are placed with a heretofore-unused orientation for the purpose of augmenting heat transfer in fin-tube heat exchanger.

254 citations

Journal ArticleDOI
TL;DR: In this paper, the relative advantage of using a helical coil versus a straight tube heat exchanger for heating liquids was investigated. But the particular difference in this study compared to other similar studies was the boundary conditions for the helical coils, whereas most studies focus on constant wall temperature or constant heat flux.

251 citations

Journal ArticleDOI
TL;DR: In this article, an experimental study on the air-side heat transfer and pressure drop characteristics for multi-louvered fin and flat tube heat exchangers has been performed, where the inlet temperatures of the air and water for heat exchanger were 21 and 45°C, respectively.
Abstract: An experimental study on the air-side heat transfer and pressure drop characteristics for multi-louvered fin and flat tube heat exchangers has been performed. For 45 heat exchangers with different louver angles (15–29°), fin pitches (1.0, 1.2, 1.4 mm) and flow depths (16, 20, 24 mm), a series of tests were conducted for the air-side Reynolds numbers of 100–600, at a constant tube-side water flow rate of 0.32 m3/h. The inlet temperatures of the air and water for heat exchangers were 21 and 45°C, respectively. The air-side thermal performance data were analyzed using effectiveness-NTU method for cross-flow heat exchanger with both fluid unmixed conditions. The heat transfer coefficient and pressure drop data for heat exchangers with different geometrical configurations were reported in terms of Colburn j-factor and Fanning friction factor f, as functions of Reynolds number based on louver pitch. The general correlations for j and f factors are developed and compared to other correlations. The f correlation indicates that the flow depth is one of the important parameters for the pressure drop.

244 citations

Journal ArticleDOI
TL;DR: In this paper, a literature search is presented on plate heat exchangers and new correlations for evaporation heat transfer coefficient and friction factor are introduced, which are applicable to various system pressure conditions and plate chevron angles.
Abstract: Plate heat exchangers are used regularly in the heating, ventilating, air conditioning, and refrigeration industry. There is an urgent need for detailed and systematic research regarding heat transfer and the fluid flow characteristics of these types of exchangers. As an initiative in this respect, a literature search is presented on plate heat exchangers. New correlations for evaporation heat transfer coefficient and friction factor are introduced, which are applicable to various system pressure conditions and plate chevron angles. The correlations are based on actual field data collected during several years of installation and operation of chillers, and they are intended to serve as design tools and perhaps as a starting point for future research.

243 citations


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Performance
Metrics
No. of papers in the topic in previous years
YearPapers
202357
2022123
202120
202013
201916
201849