Coupling boiler applied to supercritical carbon dioxide and thermoelectric power generation

A carbon dioxide and thermoelectric power generation technology, applied in generators/motors, electrical components, steam generation, etc., can solve problems such as heat loss, greenhouse effect, energy waste, etc., and achieve the effect of reducing emissions

Pending Publication Date: 2022-01-11
HARBIN BOILER
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The flue gas at the end of pulverized coal combustion has a temperature of up to 160°C and the main component of the flue gas is O 2 , CO 2 , SO 2 , NO 2 , water vapor, etc., and also contain a small amount of CO, SO 3 、H 2 、CH 4 and other hydrocarbons (CnHm), after desulfurization and denitrification treatment, the tail gas composition is about 15%O 2 +80%CO 2 +5% other gases, after the exhaust gas is discharged, it will cause a lot of heat loss and carbon emissions, resulting in energy waste and greenhouse effect

Method used

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  • Coupling boiler applied to supercritical carbon dioxide and thermoelectric power generation
  • Coupling boiler applied to supercritical carbon dioxide and thermoelectric power generation
  • Coupling boiler applied to supercritical carbon dioxide and thermoelectric power generation

Examples

Experimental program
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Effect test

Embodiment 1

[0015] A coupling boiler applied to supercritical carbon dioxide and thermoelectric power generation, which consists of a supercritical carbon dioxide furnace 13, a steam turbine 4, a pulverized-coal furnace horizontal flue outlet 1 and a heat exchange temperature rise tube 6, the level of the supercritical carbon dioxide furnace The flue is respectively communicated with the steam turbine and the CO gas pipeline 10, the steam turbine is communicated with the heat exchange temperature rise tube, the high-temperature tail gas at the outlet of the horizontal flue of the pulverized coal boiler and the gas of the horizontal flue are The high-temperature tail gas in the flue reduction section is respectively bridged with the low-temperature tail gas passing through the steam turbine through the thermoelectric power generation sheet group 5, and the heat exchange and temperature rise tube is connected to the CO2 gas cooling of the supercritical carbon dioxide furnace through a pressur...

Embodiment 2

[0017] According to the coupling boiler applied to supercritical carbon dioxide and thermoelectric power generation described in Embodiment 1, the outlet of the horizontal flue of the pulverized coal boiler communicates with the CO channel 12 .

Embodiment 3

[0019] According to the coupling boiler applied to supercritical carbon dioxide and thermoelectric power generation described in embodiment 1 or 2, the outlet of the horizontal flue of the pulverized coal boiler is connected with the absorption pool 7 through pipelines.

[0020] The thermoelectric power generation method is to use the thermoelectric power generation sheet group to bridge the high-temperature exhaust gas of the pulverized coal boiler and the low-temperature exhaust gas of the supercritical carbon dioxide circulating furnace, and the thermoelectric power generation sheet used is bismuth antimonide Bi 2 Te 3 , the high-temperature flue gas temperature T of the pulverized coal furnace is 160°C, and the supercritical carbon dioxide working medium parameter after temperature control and pressure control (heat conduction and pressure reduction) is T 0 =31.1°C, P=7.38MPa. According to Seebeck's law, for Bi 2 Te 3 As far as the thermoelectric power generation chip i...

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PUM

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Abstract

The invention provides a coupling boiler applied to supercritical carbon dioxide and thermoelectric power generation. After desulfurization and denitrification treatment and tail gas emission, a large amount of heat loss and carbon emission are caused, and energy waste and greenhouse effect are caused. The boiler comprises a supercritical carbon dioxide boiler (13), a steam turbine (4), a pulverized coal boiler horizontal flue outlet (1) and a heat exchange temperature rising pipe (6), wherein a horizontal flue of the supercritical carbon dioxide boiler is in communication with the steam turbine and a CO gas pipeline (10), the steam turbine is in communication with the heat exchange temperature rising pipe, high-temperature tail gas of the pulverized coal boiler horizontal flue outlet and high-temperature tail gas of a flue reduction section of the horizontal flue are in bridge connection to low-temperature tail gas passing through the steam turbine by means of a temperature difference power generation sheet set (5), and the heat exchange temperature rising pipe is connected to a CO2 air cooling wall (2) of the supercritical carbon dioxide boiler by means of a pressure regulating valve (8). The coupling boiler is applied to supercritical carbon dioxide and thermoelectric power generation.

Description

technical field [0001] The invention relates to a coupled boiler applied to supercritical carbon dioxide and thermoelectric power generation. Background technique [0002] Conventional pulverized coal boilers burn pulverized coal to obtain supercritical water. The critical pressure and temperature of supercritical water must reach 22.1MPa and above 374°C. At the same time, taking a 660MW boiler as an example, the exhaust heat loss is due to the fact that the exhaust gas temperature is higher than the air temperature (base temperature) entering the boiler, and this part of the heat is not used. The exhaust heat loss is the boiler efficiency The largest item in the loss accounts for about 4% to 12% of the total heat loss. The flue gas at the end of pulverized coal combustion has a temperature of up to 160°C and the main component of the flue gas is O 2 , CO 2 , SO 2 , NO 2 , water vapor, etc., and also contain a small amount of CO, SO 3 、H 2 、CH 4 and other hydrocarbon...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): F22B3/08F22B33/18F01K7/32F01K11/02F01K25/10H02N11/00
CPCF22B3/08F22B33/18F01K7/32F01K11/02F01K25/103H02N11/002
Inventor 王硕郝维勋程义魏力民史然峰王兆民李万超秦萍丽
Owner HARBIN BOILER
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