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Circulating fluidized bed boiler flue gas desulfurizing system and treatment method thereof

A circulating fluidized bed and boiler flue gas technology, applied in the field of flue gas purification, to eliminate the influence of temperature changes and atmosphere on the sulfur fixation reaction and its products, improve the sulfur fixation rate, and improve the utilization rate

Active Publication Date: 2019-04-19
YANKUANG GRP CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] CN 103272475 A discloses a desulfurization system for a circulating fluidized bed boiler, in which the upper part of the cyclone separator is connected to the upper part of the furnace of the boiler, and the lower part of the cyclone separator is connected to the lower part of the furnace through a return pipe , there is a desulfurizer inlet on the return pipe, and the inlet is located at the negative pressure position of the return pipe, but the calcium spraying desulfurization technology in the furnace also has some defects in practical application, such as the actual operating bed temperature deviates from the design value, higher than the desulfurization The optimum temperature range is 850°C to 900°C; the dense-phase region at the bottom of the circulating fluidized bed is in a state of constant alternation of oxidation / reduction atmosphere, but most of the time it is in a reducing atmosphere, while in a reducing atmosphere CaSO 4 Easy to decompose, etc.

Method used

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  • Circulating fluidized bed boiler flue gas desulfurizing system and treatment method thereof

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Embodiment 1

[0039] This embodiment provides a circulating fluidized bed boiler flue gas desulfurization system, the structural diagram of the system is as follows figure 1 As shown, it includes a circulating fluidized bed boiler 1 and a desulfurization fluidized bed 2, the flue gas outlet of the circulating fluidized bed boiler 1 is connected to the gas inlet provided at the bottom of the desulfurization fluidized bed 2, and the desulfurization fluidized bed 2 The bottom is provided with a desulfurizer inlet.

[0040] The system also includes a separator 3 and a feeder 4, the material outlet at the top of the desulfurization fluidized bed 2 is connected to the material inlet of the separator 3, the separator 3 includes a flue gas outlet and a material outlet, and the separator The material outlet of the device 3 is connected with the material inlet of the feeder 4, and the material outlet of the feeder 4 is connected with the desulfurizing agent inlet at the bottom of the desulfurization ...

Embodiment 2

[0042] This embodiment provides a method for flue gas desulfurization of a circulating fluidized bed boiler, which is carried out using the system in Embodiment 1, and includes the following steps:

[0043](1) Flue gas with a temperature of 900°C generated by coal combustion enters the desulfurization fluidized bed 2 and reacts with the desulfurizing agent limestone, the particle size of which is 0.4mm;

[0044] (2) The product after the reaction in step (1) is subjected to gas-solid centrifugation, and 99 wt% of the obtained solid limestone is returned to step (1) to continue the reaction.

[0045] In this embodiment, the high-temperature flue gas provides heat for the decomposition of limestone, and the flue gas desulfurization is transferred to the circulating fluidized bed boiler 1. The desulfurization efficiency reaches 97%, and the utilization rate of desulfurizer reaches 70%.

Embodiment 3

[0047] This embodiment provides a method for flue gas desulfurization of a circulating fluidized bed boiler. The method is carried out using the system in Embodiment 1, with reference to the method in Embodiment 2, the only difference is that the temperature of the flue gas in step (1) is At 880° C., the particle size of limestone is 0.1 mm, and the return ratio of limestone in step (2) is 99.4 wt %.

[0048] In this embodiment, the high-temperature flue gas provides heat for the decomposition of limestone, and the flue gas desulfurization is transferred to the circulating fluidized bed boiler 1. The desulfurization efficiency reaches 96%, and the utilization rate of desulfurizer reaches 70%.

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Abstract

The invention provides a circulating fluidized bed boiler flue gas desulfurizing system and a treatment method thereof. The system comprises a circulating fluidized bed boiler and a desulfurizing fluidized bed. A flue gas outlet of the circulating fluidized bed boiler is connected with a gas inlet formed in the bottom of the desulfurizing fluidized bed, and the bottom of the desulfurizing fluidized bed is provided with a desulfurizer inlet. The system is provided with the desulfurizing fluidized bed behind the circulating fluidized bed boiler, a sulfur fixation reaction is transferred to the region with the stable and proper temperature, the influences of temperature changes and atmosphere in the hearth on sulfur fixation reactions and products thereof are eliminated, and by arranging a separator and a return feeder, the desulfurizer is recycled; the accumulation effect in the circulating process is used for enhancing the sulfur fixation reaction, the desulfurizing cost is lowered, andthe desulfurizer utilization rate and desulfurizing efficiency are improved.

Description

technical field [0001] The invention belongs to the technical field of flue gas purification, and relates to a circulating fluidized bed boiler flue gas desulfurization system and a treatment method thereof. Background technique [0002] SO 2 As one of the most important pollutants in the flue gas emitted by circulating fluidized bed (CFB) boilers in coal-fired power plants, its emissions are strictly limited. Desulfurization, thereby reducing environmental pollution. [0003] CFB boilers are usually desulfurized by adding limestone and other desulfurizers to the boiler for flue gas desulfurization. It is a recognized clean combustion technology and has been widely used for its high desulfurization efficiency, low cost, simple operation, and no water pollution. application. The bed temperature of the CFB boiler is uniform and low, generally between 850°C and 900°C. This temperature is just the optimum temperature for the sulfur fixation reaction. At the same time, the gas...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/50B01D53/83B01D45/16
CPCB01D45/16B01D53/502B01D53/83B01D2251/404B01D2251/602B01D2258/0283
Inventor 刘忠攀王海苗许义王传志宋令坡卢晓明
Owner YANKUANG GRP CO LTD
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