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Double-area double-circulation flue gas carbon dioxide absorption tower and process

A technology of carbon dioxide and absorption towers, which is applied in gas treatment, air quality improvement, chemical instruments and methods, etc., can solve the problems of increasing equipment footprint, reducing equipment investment costs, reducing the height of absorption towers, etc., to achieve height reduction, Achieve automatic control and safe operation, and reduce energy consumption in the regeneration process

Pending Publication Date: 2021-11-16
ZHEJIANG ZHENENG TECHN RES INST
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] In order to meet the flue gas carbon dioxide capture efficiency while minimizing the height of the absorption tower, the design of the absorption tower often adopts the scheme of multi-tower series connection or multiple small systems instead of large systems. These schemes not only reduce the equipment investment cost to a limited extent, but also increase Equipment footprint
At present, there is no report on the design of a carbon dioxide absorption tower that can meet the high-efficiency absorption and can effectively reduce the tower height. Therefore, it is of great significance to propose a dual-zone double-circulation flue gas carbon dioxide absorption tower and its technology.

Method used

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  • Double-area double-circulation flue gas carbon dioxide absorption tower and process

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Embodiment 1

[0038] Embodiment 1 of the present application provides a dual-zone double-cycle flue gas carbon dioxide absorption tower, including a raw flue gas inlet flow regulating valve 1, a raw flue gas distributor 2, a lower absorption packing layer 3, an upper absorption packing layer 4, and a lower spraying layer Device 5, upper layer spray device 6, absorption tower demister 7, upper layer absorption liquid collector 8, upper layer filler anti-wall flow circle 9, tower kettle one 10, tower kettle two 11, lower layer liquid supply pump 12, upper layer liquid supply pump 13. The flow regulating valve of the upper layer liquid supply pump 14, the second valve of the upper layer absorption liquid return tower kettle 15, the upper layer absorption liquid flowmeter 16, the upper layer absorption liquid return tower kettle one valve 17, the lower layer liquid supply pump flow regulating valve 18, the lower layer absorption liquid Flow meter 19, clean flue gas discharge valve 20, absorption...

Embodiment 2

[0050] Embodiment 2 of the present application provides a process for a double-zone double-circulation flue gas carbon dioxide absorption tower. The flue gas is introduced into the absorption tower through the original flue gas inlet flow regulating valve 1 and the original flue gas distributor 2, and then passes through the lower absorption packing layer 3, The upper absorption packing layer 4 and the absorption tower demister 7 are discharged from the absorption tower; after the absorption liquid is prepared in the absorption liquid preparation tank 25, it is pumped into the tower kettle two 11 through the absorption liquid replenishment pump 24, and the absorption liquid in the tower kettle two 11 is The upper-layer liquid supply pump 13 transports it to the upper-layer absorption tower, and sprays it evenly on the upper absorption packing layer 4 through the upper-layer spray device 6. After the reaction is completed, it flows back from the upper-layer absorption liquid coll...

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Abstract

The invention relates to a double-area double-circulation flue gas carbon dioxide absorption tower which comprises an absorption tower main body, a lower absorption filler layer, an upper absorption filler layer, a lower-layer spraying device, an upper-layer spraying device, an absorption tower demister, a tower kettle I, a tower kettle II and an absorption liquid preparation box, the absorption tower main body comprises an upper-layer absorption tower and a lower-layer absorption tower; a lower absorption filler layer is arranged in the lower absorption tower, and a lower spraying device is arranged above the lower absorption filler layer; and an upper absorption filler layer is arranged in the upper-layer absorption tower, and an upper-layer spraying device is arranged above the upper absorption filler layer. The method has the beneficial effects that the height of the absorption tower can be reduced on the premise of ensuring the capture rate of lower-layer carbon dioxide by increasing the liquid-gas ratio of the lower-layer absorption tower, and the height of the absorption tower can be effectively reduced on the premise of ensuring the capture rate of upper-layer carbon dioxide by increasing the concentration of an absorbent in the upper-layer absorption tower and increasing the absorption reaction intensity; and finally, the height of the absorption tower is effectively reduced while higher capture rate of carbon dioxide in the whole tower is realized.

Description

technical field [0001] The invention relates to the fields of carbon dioxide capture, absorption tower design and environmental protection, in particular to a double-zone double-circulation flue gas carbon dioxide absorption tower and a process. Background technique [0002] In 2019, the carbon emissions of coal-fired power plants in my country's power industry accounted for about 65% of the country's total carbon emissions, making it the industry with the largest carbon emissions. Taking into account the development of my country's thermal power industry, carbon capture will be the basis for stock thermal power before 2035. The unit mainly carries out post-combustion capture technology transformation. Among the existing carbon capture technologies, the chemical absorption method is the most promising capture technology. This technology mostly uses a single-zone single-pass packed absorption tower as the absorption reactor, and uses organic amines, inorganic strong bases, etc...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/62B01D53/75B01D53/78B01D53/96
CPCB01D53/62B01D53/75B01D53/78B01D53/96B01D2251/304B01D2251/604B01D2257/504B01D2258/0283Y02A50/20Y02C20/40
Inventor 祁志福申震厉宸希刘飞高强生翁建明王亮杨睿刘羽
Owner ZHEJIANG ZHENENG TECHN RES INST
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