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Phase change heat storage device based on condensation heat transfer and key parameter determining method thereof

A phase change heat storage and heat transfer coefficient technology, which is applied in complex mathematical operations, cooling/ventilation/heating transformation, and modification using liquid cooling, etc. Smooth operation and enhanced effect of condensation heat transfer process

Active Publication Date: 2020-06-12
NANJING UNIV OF SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

Among the current phase change heat storage devices, such as the phase change heat storage device of patent No. 201720508512.8, only the input conditions of the liquid phase refrigerant are considered, and it cannot match the heat storage requirements when the gas-liquid mixed refrigerant is input.

Method used

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  • Phase change heat storage device based on condensation heat transfer and key parameter determining method thereof
  • Phase change heat storage device based on condensation heat transfer and key parameter determining method thereof
  • Phase change heat storage device based on condensation heat transfer and key parameter determining method thereof

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Embodiment

[0119] This embodiment is carried out on the premise of the technical solution of the present invention, and detailed implementation and specific operation process are given, but the protection scope of the present invention is not limited to the following embodiments.

[0120] The design condition is that the peak heat load is 300kW, lasts 6s, and the interval is 100s. The input temperature of the steam inlet 5 is 10°C, and the input temperature of the inner heat exchange tube 1 is -25°C.

[0121] According to the above calculation steps, the parameters of the phase change heat storage device are calculated.

[0122] Step 1. Estimate and round to obtain the condensation point T of the phase change heat storage device 3 -10℃, phase transition point T 4 -15°C;

[0123] Step 2. Select the outer diameter d of the inner heat exchange tube 1 2 is 3mm, the calculated wall thickness t 1 0.25mm;

[0124] Step 3. Calculate the volume V that needs to be filled with the phase chang...

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Abstract

The invention provides a phase change heat storage device based on convective heat exchange and a key parameter determining method thereof. The device comprises a condensation sleeve and a phase change heat storage device shell. A steam inlet, a condensation sleeve connector, an overflow valve and a condensate pump are arranged on the phase change heat storage device shell. The steam inlet is located in the vertex angle of the phase change heat storage device shell. The condensate pump is positioned at a bottom corner opposite to the steam inlet; at least one set of first steam channel plate and second steam channel plate are arranged in the phase change heat storage device shell in parallel. The steam channel plate and the condensate liquid level divide an inner cavity of the phase changeheat storage device shell into a plurality of wavy steam condensation channels; a plurality of condensation sleeves are inserted into the phase-change heat storage device shell through the condensation sleeve connectors in a penetrating manner; the condensation sleeve is axially parallel to the first steam channel plate; the condensation sleeve in each steam condensation channel is arranged in awavy shape in the height direction. The final design of the phase change heat storage device can be obtained through a parameter determination method, and the requirement for the heat dissipation capacity is reduced.

Description

technical field [0001] The invention belongs to the field of phase change heat storage, in particular to a condensation heat transfer based phase change heat storage device and a method for determining key parameters thereof. Background technique [0002] For the heat dissipation of high-power electronic equipment, due to the high heat flux density on its surface, it can reach 100W / cm 2 ~1000W / cm 2 , Microchannel flow is often used as a heat transfer enhancement method to improve surface heat transfer capacity, such as the microchannel evaporator with patent number 201910591725.5. Due to the high flow resistance in the microchannel, in order to reduce the design requirements of the circulating water pump, it is necessary to increase the heat dissipation per unit volume of refrigerant, and boiling the input liquid refrigerant is a common method to increase the heat dissipation per unit volume of refrigerant. [0003] The heat dissipation process of electronic equipment fluc...

Claims

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Application Information

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IPC IPC(8): H05K7/20G06F17/18
CPCG06F17/18H05K7/20H05K7/20309H05K7/20318H05K7/20336
Inventor 李强林肯胡定华
Owner NANJING UNIV OF SCI & TECH