Flue gas waste heat deep recovery system

A recovery system and flue gas waste heat technology, applied in the direction of indirect heat exchangers, fluid heaters, heat exchanger types, etc., can solve the problems of nonlinear energy conversion, energy waste, mismatching, etc., to improve moisture content and temperature, increase the dew point temperature, and improve the effect of thermal efficiency

Active Publication Date: 2019-06-11
TSINGHUA UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] However, since the dew point temperature of the flue gas exhaust heat recovery system commonly used in gas-fired boilers is close to the return water temperature of the heating network water, the return water of the heating network cannot effectively absorb the latent heat in the flue gas, and there is still a large amount of heat in the exhaust gas. part of the energy is wasted
However, in the existing deep waste heat recovery system, the use of air preheater or economizer has the problem of insufficient latent heat recovery or the phase change mismatch between the flue gas and the air on both sides.
In addition, some scholars have suggested that the main problem of using water as the medium for heat exchange between flue gas and air is the mismatch of energy conversion caused by the nonlinearity of the saturation line of air.

Method used

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  • Flue gas waste heat deep recovery system
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  • Flue gas waste heat deep recovery system

Examples

Experimental program
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Effect test

Embodiment 1

[0022] Such as figure 1 As shown, the flue gas waste heat deep recovery system provided by this embodiment includes a casing 1, a rotor 2, a partition 3, a baffle 4, a spray device 5, a water-to-water heat exchanger 6 and an air-flue gas exchange Heater7. Among them, the housing 1 is in the shape of a vertical thin-walled hollow cylinder; the rotating core 2 is in the shape of a vertical thick-walled hollow cylinder, and the side wall of the rotating core 2 is honeycomb-shaped and the honeycomb opening is horizontal, and the interior is filled with hygroscopic materials. The shaft is set in the upper part of the casing 1, and the rotating core 2 can rotate relative to its own central axis; the partition 3 divides the inner space of the casing 1 and the rotating core 2 into air through the central axis of the casing 1 and the rotating core 2. There are two parts, the flow channel 8 and the flue gas flow channel 9; a plurality of baffles 4 are respectively arranged between the ...

Embodiment 2

[0026] Such as figure 2 As shown, the flue gas waste heat deep recovery system provided in this embodiment has basically the same structure as that of Embodiment 1, the only difference is that in this embodiment, the liquid distributor 51 of the spray device 5 is arranged above the inlet 91 of the flue gas flow channel. The flue gas and the spray water are exchanged in countercurrent to obtain a better heat exchange effect.

[0027] In the above embodiments, the air-flue gas heat exchanger 7 is arranged below the liquid distributor 51 of the spray device 5, that is, after the flue gas enters the flue gas flow channel 9, it absorbs heat with the air-flue gas heat exchanger 7 first. end heat exchange, and then enter the spray device 5 to exchange heat with spray water.

Embodiment 3

[0029] Such as image 3 As shown, the flue gas waste heat deep recovery system provided in this embodiment has basically the same structure as that of Embodiment 1, the only difference is that the rotating core 2 in this embodiment includes a central rotating shaft 21 and a surrounding runner 22, and the rotating wheel 22 adopts The honeycomb structure and the honeycomb opening are vertical, and the outer diameter of the runner 22 matches the inner diameter of the housing 1; since the air can only flow vertically in the runner 22, the partition 3 is only arranged under the rotor 2 In the housing 1, the inner space of the lower part of the housing 1 is divided into two parts: the air flow channel 8 and the smoke flow channel 9, and the baffle plate 4 only needs to be arranged on the top of the rotor core 2 on the side of the smoke flow channel 9 and Between the top of the housing 1. When the flue gas waste heat deep recovery system of this embodiment is in use, the air passes ...

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Abstract

The invention relates to a flue gas waste heat deep recovery system. The flue gas waste heat deep recovery system comprises a vertical type thin-walled hollow barrel-shaped shell, a rotating core which is disposed coaxially on the upper part of the shell and can rotate relative to the self central axis, a separation plate which is arranged in the shell and passes through the central axis of the shell and the rotating core, a plurality of baffles, a spraying device and a plate heat exchanger connected to a water inlet and a water outlet of a heat releasing unit and a spraying device; the rotating core is in a vertical type thin-walled hollow barrel shape, the longitudinal section of the side wall of the rotating core is in a honeycomb shape, and the rotating core is filled with a hygroscopic material; the separation plate divides the inner space of the shell and the rotating core into two parts of an air flow passage and a flue gas flow passage; the multiple baffles are separately disposed between the top of the shell and the top of the rotating core, between the top, on one side of the flue gas flow passage, of the rotating core and the top of the partition plate, between the bottom, on one side of the air flow passage, of the rotating core and the baffles and between the bottom, on one side of the flue gas flow passage, of the rotating core and the shell; and the spraying device is disposed in the flue gas flow passage in the lower part of the shell.

Description

technical field [0001] The invention belongs to the technical fields of heating, ventilating and air-conditioning and urban heating, and in particular relates to a deep recovery system for flue gas waste heat. Background technique [0002] As a clean and efficient primary energy, the demand for natural gas continues to grow in my country. In 2016, the national natural gas consumption has reached 205.8 billion cubic meters, a year-on-year increase of 6.6%. At the same time, due to the implementation of the "coal-to-gas" policy in the north, natural gas has become the main energy source for heating in winter in the north. At present, gas-fired boilers are the main way of heating in winter, and the exhaust gas temperature of natural gas is generally 80-120°C, which has huge potential for waste heat recovery. Moreover, the thermal efficiency of the boiler gradually increases as the exhaust gas temperature decreases. When the exhaust gas temperature drops to 30-55°C, it enters ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): F23J15/06F23L15/04
CPCF23J15/06F23J2219/80F23L7/005F23L15/04F24H8/00F24H9/0084F28D19/045F28D21/0015Y02B30/00Y02E20/34Y02P80/15
Inventor 江亿刘晓华徐熙张世钢
Owner TSINGHUA UNIV
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