Temperature Field Prediction of Rectangular Shell and Tube Heat ExchangerSource: Journal of Pressure Vessel Technology:;2013:;volume( 135 ):;issue: 006::page 61208DOI: 10.1115/1.4024437Publisher: The American Society of Mechanical Engineers (ASME)
Abstract: Shellandtube heat exchangers are the most common type of heat exchangers in oil refineries and other large chemical processes. In this manuscript, we demonstrate that the shellside flow in a cylindrical shell was not as homogeneous as that in a rectangular shell. According to the periodic flow field and the arrangement of tubes in the rectangular shell, the solidfluid coupling heat transfer model consisting of a single tube section and the outer and inner fluids was developed to represent the whole heat exchanger. Using this model, the relationship among four temperatures, namely the inlet and outlet temperatures of tubeside fluid and the upstream and downstream temperatures of shellside fluid, was established. By dividing each tube into several tube sections at the sites of baffles, a method for predicting the temperature field of the rectangular shellandtube heat exchanger was proposed. Based on the node temperature correlation, all the node temperatures were obtained by iterative computation using the established relationship between the four temperatures and the operating conditions. It was found that the temperature distribution of the fluid in tube was approximately linear along axial direction, but the temperature of tube showed nonlinear regularity. The axial deformation compatibility condition for the tube bundle and shell was considered when resolving the stresses in tubes. For the model established in this paper, the mean temperature of the tube at lower position was found to be larger than that at higher position; hence the thermal expansion of the tube at the lower end is larger. In the case the tubeside fluid was heated, all tubes were pulled because of the larger axial thermal expansion of shell, and the stress in the tube with higher temperature is smaller because of the smaller strain.
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| contributor author | Zhou, J. F. | |
| contributor author | Li, Y. | |
| contributor author | Gu, B. Q. | |
| contributor author | Shao, C. L. | |
| date accessioned | 2017-05-09T01:02:29Z | |
| date available | 2017-05-09T01:02:29Z | |
| date issued | 2013 | |
| identifier issn | 0094-9930 | |
| identifier other | pvt_135_06_061208.pdf | |
| identifier uri | http://yetl.yabesh.ir/yetl/handle/yetl/153106 | |
| description abstract | Shellandtube heat exchangers are the most common type of heat exchangers in oil refineries and other large chemical processes. In this manuscript, we demonstrate that the shellside flow in a cylindrical shell was not as homogeneous as that in a rectangular shell. According to the periodic flow field and the arrangement of tubes in the rectangular shell, the solidfluid coupling heat transfer model consisting of a single tube section and the outer and inner fluids was developed to represent the whole heat exchanger. Using this model, the relationship among four temperatures, namely the inlet and outlet temperatures of tubeside fluid and the upstream and downstream temperatures of shellside fluid, was established. By dividing each tube into several tube sections at the sites of baffles, a method for predicting the temperature field of the rectangular shellandtube heat exchanger was proposed. Based on the node temperature correlation, all the node temperatures were obtained by iterative computation using the established relationship between the four temperatures and the operating conditions. It was found that the temperature distribution of the fluid in tube was approximately linear along axial direction, but the temperature of tube showed nonlinear regularity. The axial deformation compatibility condition for the tube bundle and shell was considered when resolving the stresses in tubes. For the model established in this paper, the mean temperature of the tube at lower position was found to be larger than that at higher position; hence the thermal expansion of the tube at the lower end is larger. In the case the tubeside fluid was heated, all tubes were pulled because of the larger axial thermal expansion of shell, and the stress in the tube with higher temperature is smaller because of the smaller strain. | |
| publisher | The American Society of Mechanical Engineers (ASME) | |
| title | Temperature Field Prediction of Rectangular Shell and Tube Heat Exchanger | |
| type | Journal Paper | |
| journal volume | 135 | |
| journal issue | 6 | |
| journal title | Journal of Pressure Vessel Technology | |
| identifier doi | 10.1115/1.4024437 | |
| journal fristpage | 61208 | |
| journal lastpage | 61208 | |
| identifier eissn | 1528-8978 | |
| tree | Journal of Pressure Vessel Technology:;2013:;volume( 135 ):;issue: 006 | |
| contenttype | Fulltext |