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Finite Element Calculation Method of Simplified Model of Large Diameter Tube for Heat Exchange Tube

A calculation method and technology for simplifying models, applied in the direction of calculation, special data processing applications, instruments, etc., can solve the problems of huge calculation amount, high calculation cost, and large limitation, achieve model simplification, improve design efficiency, and reduce calculation cost Effect

Active Publication Date: 2017-04-05
HARBIN BOILER
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This model has great limitations, and it is not applicable to structures such as thermal stress, flexible tube sheet and inclined cone shell, and can only be analyzed by finite element method
For the finite element model of more than a thousand heat exchange tubes, the amount of calculation is extremely large. Even on a mainframe, the time for one calculation can be calculated in months, and the calculation cost is high and the cycle is too long.

Method used

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  • Finite Element Calculation Method of Simplified Model of Large Diameter Tube for Heat Exchange Tube
  • Finite Element Calculation Method of Simplified Model of Large Diameter Tube for Heat Exchange Tube
  • Finite Element Calculation Method of Simplified Model of Large Diameter Tube for Heat Exchange Tube

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Experimental program
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Effect test

Embodiment 1

[0029] A heat exchanger tube sheet, which consists of: a tube sheet main body, the heat exchange tubes on the tube sheet main body are calculated using the finite element calculation method of a simplified model of a large-diameter tube to obtain the structural size, and the boiler heat exchange tubes are first selected as 2 Based on the calculation of the level equivalent model, the number of equivalent heat exchange tubes of the boiler heat exchange tubes is 9; the cross-sectional area of ​​each heat exchange tube of the equivalent boiler heat exchange tube Am=A / 9=126375 mm 2 ; Select the inner diameter of the heat exchange tube of the equivalent boiler heat exchange tube as 200mm, and the outer diameter of the heat exchange tube of the equivalent boiler heat exchange tube is 448mm; use the symmetry of the model to establish a 1 / 4 overall model, and mesh the model After the equivalent boiler heat exchange tube is 9 heat exchange tubes, the ratio of the outer surface area is 4...

Embodiment 2

[0031] In the calculation process of the heat exchanger tube sheet strength, the heat exchange tube adopts the finite element calculation method of the simplified model of the large-diameter tube. The calculation method is divided into six steps. The first step is to establish a simplified finite element calculation model, and the heat exchange tube Through multi-series equivalent; the second step is to determine the number of heat exchange tubes in the a-level model according to the finite element calculation model; the third step is to determine the number of heat exchange tubes in the a-level layout according to the number of a-level model heat exchange tubes , the fourth step is to determine that the sum of the cross-sectional areas of the heat exchange tubes after the equivalent is equal to the sum of the cross-sectional areas of the heat exchange tubes before the equivalent; the fifth step is to arrange the heat exchange tubes at all levels alternately; The equivalent of ...

Embodiment 3

[0033] In the calculation process of the heat exchanger tube sheet strength, the heat exchange tube adopts the large-diameter tube simplified model finite element calculation method, and the number of heat exchange tubes in the a-level model includes the number of 1-n level model heat exchange tubes , the number of heat exchange tubes in the first-level model is 1, the number of heat exchange tubes in the second-level model is 9, the number of heat exchange tubes in the third-level model is 25, and the n The number of heat exchange tubes in the stage model is (2n-1) 2 .

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Abstract

The invention discloses a finite element calculating method for a large bore tube simplifying model of a heat exchanging tube. A plate-type heat exchanger is subjected to heat exchange through the temperature difference of fluid on the two sides of the heat exchanging tube so as to achieve the purpose of heating the fluid on one side. The finite element calculating method for the large bore tube simplifying model of the heat exchanging tube comprises the following six steps: step one, establishing and simplifying a finite element calculating model, and conducting multi-series equivalence on the heat exchanging tube; step two, determining the number of heat exchanging tubes of an a-level model according to the finite element calculating model; step three, determining the number of heat exchanging tubes in a-level distribution according to the number of the heat exchanging tubes of the a-level model; step four, determining the sum of the cross sections of the heat exchanging tube after the equivalence to be equal to that of the cross sections of the heat exchanging tubes before the equivalence; step five, arranging the all levels of heat exchanging tubes in a staggered manner; and step six, corresponding the different levels of equivalence to different correction factors being 0.20-1.09. The finite element calculating method is used for manufacturing a tube sheet of the heat exchanger.

Description

[0001] Technical field: [0002] The invention relates to the field of power station or chemical equipment; in particular, it relates to a finite element calculation method for a simplified model of a large-diameter tube of a heat exchange tube. [0003] Background technique: [0004] The tube-sheet heat exchanger is a device that exchanges heat through the temperature difference of the fluid on both sides of the heat exchange tube, so as to achieve the purpose of heating the fluid on one side. [0005] At present, the number of heat exchange tubes in tube-sheet heat exchangers with slightly larger diameters can reach more than a thousand, and the number of heat exchange tubes in larger diameter heat exchangers can even reach thousands. At this stage, the calculation of heat exchanger tube sheets generally adopts the rigid solid circular plate model that ignores the heat exchange tubes. This model has great limitations, and it is not applicable to structures such as thermal st...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): G06F17/50
Inventor 张彦军刘庆江唐卉张明宝叶涛周大坤傅吉坤方小里王非
Owner HARBIN BOILER
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