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Optimum design method of pipeline length of organic Rankine cycle heat exchanger considering flow pattern

A Rankine cycle and pipeline length technology, applied in the direction of instruments, calculations, special data processing applications, etc., can solve the problem of narrow application range, which is not conducive to the research, promotion and application of organic Rankine cycle, and does not consider two-phase evaporation and condensation flow Type and other problems, to improve the effect of calculation accuracy

Inactive Publication Date: 2013-08-21
CENT SOUTH UNIV
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Problems solved by technology

[0004] In the existing evaporator and condenser pipe length design methods, a certain empirical formula is basically selected for calculation, without considering the flow pattern in the two-phase evaporation and condensation process, resulting in low calculation accuracy of the heat exchanger pipe length
At the same time, the scope of application of the empirical formula is narrow, which is not conducive to the research, promotion and application of the organic Rankine cycle

Method used

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  • Optimum design method of pipeline length of organic Rankine cycle heat exchanger considering flow pattern
  • Optimum design method of pipeline length of organic Rankine cycle heat exchanger considering flow pattern
  • Optimum design method of pipeline length of organic Rankine cycle heat exchanger considering flow pattern

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Embodiment Construction

[0016] , Determination of pipe length for single-phase flow heat exchange between evaporator and condenser

[0017] The present invention selects the Gnielinski formula with the highest calculation accuracy so far to calculate the convective heat transfer coefficient in the evaporator and the condenser under the single-phase flow state of the working medium. The steps to determine the length of the pipeline in the single-phase flow state of the evaporator and condenser are as follows:

[0018] Step 1: Divide the dynamic viscosity of the working fluid at the average temperature of the segment according to the working fluid and the heat source fluid mu i , Heat capacity at constant pressure c p,i and thermal conductivity k i Calculate the Prandtl numbers of the working fluid at these two temperatures Pr i (For gas, it is only necessary to calculate the Prandtl number at the average temperature of the working medium in the division section), where the Prandtl number cal...

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Abstract

The invention discloses an optimum design method of the pipeline length of an organic Rankine cycle heat exchanger considering a flow pattern. When organic working media are in a single-phase flow state, an average Nu of one section is calculated to get heat exchange amount of the section, the heat exchange amount is compared with actual heat exchange amount, and a pipe length value of the section is determined. When the organic working media are in a two-phase flow state, a convective heat-transfer coefficient calculation method of a corresponding flow pattern is selected to obtain a convective heat-transfer coefficient of the section, heat exchange amount of the section is calculated according to the convective heat-transfer coefficient value and an assumed pipe length in the end, the heat exchange amount is compared with the actual heat exchange amount, the pipe length of each dividing section is determined, and the pipeline length of the heat exchanger can be obtained. Computational accuracy of the heat exchange amount is obviously improved through consideration of flow pattern changes of media in the process of two-phase evaporation and condensation, and the optimum design method can be applied to determination of pipeline lengths of organic Rankine cycle heat exchangers using various commonly-used fluids.

Description

technical field [0001] The invention relates to a method for optimizing the pipe length design of an organic Rankine cycle heat exchanger considering the flow pattern. technical background [0002] In 2011, my country's GDP was about 7.30 trillion US dollars, and the total primary energy consumption was 2.613 billion tons of oil equivalent. my country's GDP accounts for 10.47% of the world's total GDP, but the energy consumed for this accounted for 21.29% of the world's total energy consumption. Statistics show that my country's energy consumption per 10,000 yuan of GDP is 2.03 times that of the world average, 2.38 times that of the United States, 4.18 times that of Germany, and 4.40 times that of Japan. my country's industrial energy consumption accounts for more than 70% of the whole society's energy consumption, and high industrial energy consumption is the main reason for my country's high energy consumption per unit of GDP. However, 60% - 65% of industrial energy cons...

Claims

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Application Information

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IPC IPC(8): G06F17/50
Inventor 孙志强朱启的周孑民
Owner CENT SOUTH UNIV
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