2019
DOI: 10.1088/1755-1315/272/2/022193
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Coiled Heat Exchanger with Small Radius Bent Tubes for Controlled Heat Treatment of High Viscosity Waxy Oil

Abstract: The necessity of using the controlled heat treatment technology of oil instead of «hot pumping» is substantiated. A number of advantages of the “cold” transportation of oil are presented, as well as the main tasks that need to be solved for the successful usage of the above technology at the trunk oil pipelines. The main drawbacks of the heat exchanging equipment used at the heating and pumping stations of trunk pipelines for non-Newtonian solidifying waxy oils. Particular attention is paid to deposition and a… Show more

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Cited by 3 publications
(2 citation statements)
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“…The fact that effective implementation of the heat treatment technology is impossible because of the relatively low technology level and reliability indicators of exchanger equipment has also become the reason for the ineffectiveness of widely introduced methods of chemical treatment because of inadequate temperatures of oil preheating when adding pour point depressants [6,7,8].…”
Section: Relevance Of the Issue And Its Current Statementioning
confidence: 99%
“…The fact that effective implementation of the heat treatment technology is impossible because of the relatively low technology level and reliability indicators of exchanger equipment has also become the reason for the ineffectiveness of widely introduced methods of chemical treatment because of inadequate temperatures of oil preheating when adding pour point depressants [6,7,8].…”
Section: Relevance Of the Issue And Its Current Statementioning
confidence: 99%
“…One option to make the heat exchanger's design more compact is the use of close-packed with small bend radius coils (SBRC). Such designs [1] have been applied in various industries. However, heat transfer in the complex geometry of a heat exchanger's annular space (Figure 1) cannot be described by simple one-dimensional cases and dependencies; for example, formulas for the heat transfer coefficient of a transverse flow around a tube bundle must consider the three-dimensional spatial structure of the heat exchange surface.…”
Section: Introductionmentioning
confidence: 99%