Flue gas injection conveying technology for achieving absorbent pretreatment in flue gas purification method
A flue gas purification and absorbent technology, applied in chemical instruments and methods, separation methods, dispersed particle separation, etc., can solve the problems of inconspicuous industrial application, long process flow, poor technical economy, etc., to improve desulfurization and denitrification efficiency, The effect of improving processing efficiency and high crushing efficiency
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Embodiment 1
[0035] In the traditional flue gas purification method, the rough purification process of the raw flue gas by the absorbent usually includes: metering the absorbent, and then sending it into the pulverizer system for pulverization, and then sending the pulverized absorbent particles through a dry powder injector. The main flue 1 mixes and reacts with the raw flue gas. During this process, the purification efficiency of the absorbent to the raw flue gas is usually about 50%, and the desulfurization efficiency is low. Therefore, in order to improve the working efficiency of the absorbent, this The invention proposes a flue gas jet conveying process to realize absorbent pretreatment in the flue gas purification method. This process overcomes the pulverization treatment of the absorbent in the traditional flue gas purification method, and adopts the setting of the impact mill, pulverizer and classifier. The process flow is as follows: During the process of transporting the raw flue...
Embodiment 2
[0037] The difference between this embodiment and Embodiment 1 is that in this embodiment, an auxiliary flue 2 is provided on the main flue 1 for auxiliary flue gas to pass through. After being fed into the impact mill, pulverizer and classifier along the entrance of the auxiliary flue 2, the obtained gas-powder mixture is then sent to the main flue 1 from the outlet of the auxiliary flue 2, wherein the volume ratio of the flue gas to the auxiliary flue gas is 9 :1.
[0038] In the actual application process of this embodiment, the original flue gas is sent into the main flue 1 through the flue gas booster fan, and a part of the original flue gas enters the auxiliary flue 2 through the entrance of the auxiliary flue 2, which is called auxiliary flue gas. A part of the original flue gas remains in the main flue 1, which is called flue gas. The auxiliary flue gas drives the absorbent and enters the impact mill crushing classifier together. The absorbent is pretreated in the impa...
Embodiment 3
[0040] The difference between this embodiment and Embodiment 2 is that in this embodiment, the impact mill pulverizing classifier is mainly composed of a pulverizer, a classifier and a high-pressure induced draft fan, and the absorbent and auxiliary flue gas are sent into the mill with the high-pressure induced draft fan. The absorbent is pulverized and then sent to the classifier with the auxiliary flue gas for screening. In the actual operation process, the gas-powder mixture can be selected by adjusting the speed of the classifier. Usually, the particle size of the absorbent in the gas-powder mixture It is controlled at 10-40um, that is: the absorbent with a particle size of ≤40um is mixed with the auxiliary flue gas to obtain a gas-powder mixture, and the absorbent with a particle size of >40um is returned to the mill for further pulverization.
[0041] Since the amount of absorbent introduced is related to the pollutant content in the original flue gas, it is necessary to ...
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