ISSUES OF HEAT EXCHANGE APPARATUS OPTIMIZATION

The possibility of use of the heat-exchangers in whole or in part manufactured with use of polymers and plastics is considered. Despite obvious, at first sight, inexpediency of use of polymeric materials in the heat-exchange equipment (low coefficient of heat conductivity, and also low, in comparison with metals, the strength properties of the majority of the most widespread polymers), «polymeric» heat-exchangers find application in various areas of the industry more and more surely. Classification of heat-exchange apparatuses which constructive elements are executed with use of polymeric materials is proposed. The following signs are the basis for classification: polymer type, a type of polymer meric material, type of the heat-exchange apparatus (a form of heat-exchange elements), reliance on polymeric materials in apparatuses, motion freedom of polymeric heat-exchange elements, level of assembly of a design, and also diameter of tubular elements. Critical analysis the most characteristic designs developed by domestic and foreign designers and inventors is carried out. Ref. 21, Fig. 13.

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Heat exchange apparatus of low thermal conductivity plastics

Chemical and Petroleum Engineering ◽

10.1007/bf01833034 ◽

1969 ◽

Vol 5 (8) ◽

pp. 650-651

Author(s):

S. M. Lukomskii ◽

D. F. Kagan ◽

M. Ya. Nemlikher

Keyword(s):

Thermal Conductivity ◽

Heat Exchange ◽

Low Thermal Conductivity ◽

Exchange Apparatus

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Analysis Of Three Layer Concentric Tube Heat Exchange Using Mathematic Modeling

Journal Basic Science and Technology ◽

10.35335/jbst.v10i3.1757 ◽

2021 ◽

Vol 10 (3) ◽

pp. 86-92

Author(s):

Rinaldy Valendry

Keyword(s):

Mathematical Modeling ◽

Heat Exchange ◽

Coming Out ◽

Theoretical Calculations ◽

Fluid Temperature ◽

Modeling Methods ◽

Mathematic Modeling ◽

Cold Fluid ◽

Theory Calculation ◽

Exchange Apparatus

A three-channel concentric pipes heat exchanger is a development or improvement of a two-channel concentric heat exchange apparatus. This study was conducted to determine the output temperature of each channel, and compare the results of theoretical calculations using mathematical modeling of experimental results conducted in the field. So that obtained difference of value between result of experiment to result of theory calculation. In this study have 3 variations of temperature data that is 50 °C, 55°C, and 60 °C with two streams namely CounterFlow and PararellFLow and discharge 2.5 l/minute, while cold fluid with 25 °C discharge 1.5 l/minute. From the above analysis it can be concluded that the temperature of the hot fluid coming out of the APK in the experiment tends to be higher than the temperature of the hot fluid coming out of the APK on theoretical calculations of mathematical modeling methods. Meanwhile, the cold cold fluid temperature coming out of the APK in experimental tends to be lower than the temperature of the cold fluid coming out of the APK on theoretical calculations of mathematical modeling methods.

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A model heat-exchange apparatus for the investigation of fouling of stainless steel surfaces by milk I. Deposit formation at 100 °C

Journal of Dairy Research ◽

10.1017/s002202990002642x ◽

1989 ◽

Vol 56 (2) ◽

pp. 201-209 ◽

Cited By ~ 29

Author(s):

Carole L. Foster ◽

Michel Britten ◽

Margaret L. Green

Keyword(s):

Stainless Steel ◽

Heat Exchange ◽

Time Course ◽

Small Scale ◽

Lag Phase ◽

Stainless Steel Surface ◽

Deposit Formation ◽

Factors Affecting ◽

Steel Surfaces ◽

Exchange Apparatus

SummaryA model heat-exchange apparatus was used to investigate the factors affecting deposit formation from milk on a stainless steel surface at 100 °C. The structure and composition of the deposits were determined by scanning electron microscopy, energy-dispersive X-ray spectroscopy, and chemical analysis after solution in alkali. The effects of changing the pH, preheating and skimming of the milk were similar to those observed in a small-scale continuous ultra high temperature plant. The time course of deposit formation showed that a lag phase did not occur, but the deposit which formed after more than 45 min was more porous than that formed after shorter times. Most (50–90%) of the fresh deposit was readily removed by sonication, leaving a sublayer richer in minerais than the original. The results provide evidence for the two-layer model for deposit formation proposed by Tissier & Lalande (1986).

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Icing control model and algorithm for wasteheat exchangers of ventilation systems

MATEC Web of Conferences ◽

10.1051/matecconf/201819401004 ◽

2018 ◽

Vol 194 ◽

pp. 01004

Author(s):

Аndrew Arbatskiy ◽

Аndrew Garyaev ◽

Vasiliy Glasov

Keyword(s):

Mathematical Model ◽

Heat Exchange ◽

Heat Exchangers ◽

Heat Recovery ◽

Waste Heat Recovery ◽

Waste Heat ◽

Control Model ◽

Humid Air ◽

Exchange Apparatus ◽

Ice Control

Currently, ice control on various heat exchangers to be used for waste heat recovery of discharge air is a rather topical subject because ice building is a factor to reduce efficiency of heat recovery. In such systems, icing always takes place on the side of humid discharge air, with a background of heat exchange between inlet air at temperatures of -30°C and below, and discharge air. To effectively prevent this, it is required to find solutions to problems as follows: study a mechanism of ice building on heat exchange surfaces when interacting with humid air; determine engineering methods to prevent icing, for each type of heat-exchange apparatus, and check efficiency of their operation; develop a mathematical model of ice growth on heat exchange surfaces to enable to vary key parameters (both geometrical and algorithmical ones), determined beforehand, and engineering means aimed at icing prevention.

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