Spiral Heat Exchanger Utilizing Dimpled Primary Surface

Author(s):  
B. Glezer ◽  
I. Borisov ◽  
A. Khalatov ◽  
S. Kobsar

Paper presents a small demonstrator of the heat exchanger technology based on spiral counter-flow arrangement of dimpled primary surfaces. The heat exchanger has been developed as result of collaborative effort between Ukrainian and US scientists, authors of the paper. The heat transfer surfaces were fabricated out of stainless steel foil with arrays of spherical dimples augmenting heat transfer on the hot (gas) sides and corresponding spherical protrusions enhancing heat transfer on the cold (air) sides of the heat exchanger passages. About thirty primary surface geometries have been studied prior to selection of the presented configuration. Protruding diagonal ribs were introduced between lines of dimples on each side of the low-pressure passages, which were sandwiched between high-pressure passages, to prevent collapsing of the heat transfer surfaces under the pressure difference of 3.5 Bar. The counter-flow heat exchanger was assembled out of 24 (12 pairs) spiral rectangular cross-section channels, which were formed between dimpled surfaces. Development work was focused on optimizing thermal effectiveness and pressure losses within the heat exchanger core with little attention devoted to the entry and exit sections of the heat exchanger. The paper provides details of the experimental rig that was build for testing of the heat exchanger simulating operational parameters, which were representative for microturbine application. The overall recuperator effectiveness of 80–82% at total pressure loss of 10% was measured, including entry and exit losses. Excessive pressure losses in the entry-exit sections and headers were found to be main contributors to these losses. It was revealed that losses in the headers were related to inadequate structural support of the foil surfaces in the lower pressure passages, causing these passages to be partially closed. Design improvement measures addressing this issue are being evaluated with a goal of achieving 90% effectiveness with total pressure losses of less than 5% of the air inlet pressure.

Author(s):  
K. Koyama ◽  
Y. Asako

Heat exchange characteristics of a gas-gas counterflow microchannel heat exchanger have been investigated experimentally. The microchannel has a rectangular cross section with 200 μm high and 300 μm wide. Working fluid is air. Reynolds number in the hot passage ranges from 127 to 381, and that in the cold passage ranges from 25 to 381. Temperatures and pressures at inlets and outlets of the heat exchanger have been measured to obtain heat transfer rates and pressure losses. The heat exchange and the pressure loss characteristics of the tested microchannel heat exchanger are discussed. Since the partition wall of the heat exchanger is thick comparing with the microchannel dimensions, a simple heat exchange model, the wall temperature of which is constant, is proposed to predict the heat transfer rate. The predicted heat transfer rates are compared with those of the experimental results and both results agree well.


1988 ◽  
Vol 110 (1) ◽  
pp. 60-67 ◽  
Author(s):  
H. Halle ◽  
J. M. Chenoweth ◽  
M. W. Wambsganss

Throughout the life of a heat exchanger, a significant part of the operating cost arises from pumping the heat transfer fluids through and past the tubes. The pumping power requirement is continuous and depends directly upon the magnitude of the pressure losses. Thus, in order to select an optimum heat exchanger design, it is is as important to be able to predict pressure drop accurately as it is to predict heat transfer. This paper presents experimental measurements of the shellside pressure drop for 24 different segmentally baffled bundle configurations in a 0.6-m (24-in.) diameter by 3.7-m (12-ft) long shell with single inlet and outlet nozzles. Both plain and finned tubes, nominally 19-mm (0.75-in.) outside diameter, were arranged on equilateral triangular, square, rotated triangular, and rotated square tube layouts with a tube pitch-to-diameter ratio of 1.25. Isothermal water tests for a range of Reynolds numbers from 7000 to 100,000 were run to measure overall as well as incremental pressure drops across sections of the exchanger. The experimental results are given and correlated with a pressure drop versus flowrate relationship.


2021 ◽  
Vol 6 (1) ◽  
pp. 69-75
Author(s):  
Taiwo O. Oni ◽  
Ayotunde A. Ojo ◽  
Daniel C. Uguru-Okorie ◽  
David O. Akindele

A shell-and-tube heat exchanger which was subjected to different flow configurations, viz. counter flow, and parallel flow, was investigated. Each of the flow configurations was operated under two different conditions of the shell, that is, an uninsulated shell and a shell insulated with fiber glass. The hot water inlet temperature of the tube was reduced gradually from 60 oC to 40 oC, and performance evaluation of the heat exchanger was carried out. It was found that for the uninsulated shell, the heat transfer effectiveness for hot water inlet temperature of 60, 55, 50, 45, and 40 oC are 0.243, 0.244, 0.240, 0.240, and 0.247, respectively, for the parallel flow arrangement. For the counter flow arrangement, the heat transfer effectiveness for the uninsulated shell are 2.40, 2.74, 5.00, 4.17, and 2.70%, respectively, higher than those for the parallel flow. The heat exchanger’s heat transfer effectiveness with fiber-glass-insulated shell for the parallel flow condition with tube hot water inlet temperatures of 60, 55, 50, 45, and 40 oC are 0.223, 0.226, 0.220, 0.225, and 0.227, respectively, whereas the counter flow condition has its heat transfer effectiveness increased by 1.28, 1.47, 1.82, 1.11, and 1.18%, respectively, over those of the parallel flow.


2004 ◽  
Vol 2004.14 (0) ◽  
pp. 331-334
Author(s):  
Kazuhiko SATO ◽  
Hiroshi KUROTANI ◽  
Himsar Ambarita ◽  
Jun SUZUKI ◽  
Norihiko KAMADA ◽  
...  

1990 ◽  
Vol 112 (1) ◽  
pp. 64-70 ◽  
Author(s):  
S. A. Idem ◽  
A. M. Jacobi ◽  
V. W. Goldschmidt

The effects upon the performance of an air-to-water copper finned-tube crossflow heat exchanger due to condensation on the outer surface are considered. A four-tube, two-pass heat exchanger was tested over a Reynolds number range (based on hydraulic diameter) from 400 to 1500. The coil was operated both in overall parallel and overall counterflow configurations. Convective heat and mass transfer coefficients are presented as plots of Colburn j-factor versus Reynolds number. Pressure losses are, similarly, presented as plots of the friction factor versus Reynolds number. Enhancement of sensible heat transfer due to the presence of a condensate film is also considered.


2011 ◽  
Vol 255-260 ◽  
pp. 1378-1382
Author(s):  
Bai Sheng Liao

This article apply the CFX computational fluid software of ANSYS software company to casing tube heat exchanger of inside diameter of 10mm, 16mm, wall thickness of 1mm, pipe sections of the counter-flow 1000mm long, including concentric and eccentric placement of three kinds of state and other conditions in different conducted, draw a conclusion that the speed of the fluid and temperature distribution in the tube, and compared the case of three kinds of heat transfer coefficient.


Author(s):  
Andreas Penkner ◽  
Peter Jeschke

This paper considers the effect of excessive total pressure losses for heat transfer problems in fluid flows with a high circumferential swirl component. At RWTH Aachen University, a novel gas generator concept is under research. This design avoids some disadvantages of small gas turbines and uses a rotating combustion chamber. During the pre-design of the rotating combustion chamber using CFD tools, unexpected high total pressure losses were detected. To analyze this unknown phenomenon, a gas-dynamic model of the rotating combustion chamber has been developed to explain the unexpected high Rayleigh pressure losses. The derivation of the gas-dynamic model, the physical phenomenon related to the high total pressure losses in high-swirl combustion, the influencing factors, as well as thermodynamic interpretation of the Rayleigh pressure losses, are presented in this paper. In addition, the CFD results are validated by the gas-dynamic model derived. The results presented here are of possible interest for a wide range of applications, since these fundamental findings can be transferred to all heat transfer problems in fluid flows with a high circumferential swirl component.


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