Purification method for industrial emission gas
An exhaust gas and industrial technology, which is applied in the field of purification of industrial exhaust gas, can solve problems such as the inability to effectively absorb carbon dioxide, achieve good social and environmental benefits, reduce alkali content, and achieve good economic benefits
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Embodiment 1
[0032] figure 1 It is a schematic flow chart of Embodiment 1 of the present invention.
[0033] This example provides a method for purifying industrial exhaust gas. The calcium-silicate slag used is the calcium-silicate slag produced after alumina is extracted from high-alumina fly ash, wherein the mass content of sodium oxide is 2.0%, and the moisture content is 35%. ; The industrial exhaust gas to be purified is the lime rotary kiln gas of Datang Renewable Resources Co., Ltd., and the mass concentration of carbon dioxide gas is 38%. The purification of the industrial exhaust gas is completed in a three-stage series absorption tower (first-stage absorption tower, second-stage absorption tower and third-stage absorption tower), such as figure 1 As shown, it specifically includes the following steps:
[0034] (1) Mix silicon-calcium slag with water to form silicon-calcium slag slurry, heat the silicon-calcium slag slurry to 80°C, in the silicon-calcium slag slurry, the liquid...
Embodiment 2
[0039] The difference from Example 1 is that the mass content of sodium oxide in the silicon-calcium slag used in this example is 1.6%, and the water content is 43%; the industrial exhaust gas to be purified is produced by Inner Mongolia Datang Tuoketuo Power Generation Co., Ltd. Desulfurization flue gas, in which the concentration of carbon dioxide gas is 10%.
[0040] (1) Mix silicon-calcium slag with water to form silicon-calcium slag slurry, heat the silicon-calcium slag slurry to 90°C, and the liquid-solid volume ratio of silicon-calcium slag to water is 8;
[0041] (2) The calcium-silicon slag slurry is sprayed from top to bottom into the first-stage absorption tower at a flow rate of 0.02L / min, and industrial exhaust gas enters the first-stage absorption tower from bottom to top at a flow rate of 1.5L / min. The coal ash calcium calcium slag slurry is in contact with the industrial exhaust gas in the first-stage absorption tower, so that the contact time between the fly a...
Embodiment 3
[0044] The difference from Example 1 is that the mass content of sodium oxide in the silicon-calcium slag used in this example is 1.4%, and the moisture content is 38%.
[0045] (1) Mix silicon-calcium slag with water to form silicon-calcium slag slurry, heat the silicon-calcium slag slurry to 75°C, and the liquid-solid volume ratio of silicon-calcium slag to water is 12;
[0046] (2) The calcium-silicon slag slurry is sprayed from top to bottom into the first-stage absorption tower at a flow rate of 0.2L / min, and industrial exhaust gas enters the first-stage absorption tower from bottom to top at a flow rate of 0.5L / min, so that the powder The coal ash calcium calcium slag slurry is in contact with the industrial exhaust gas in the first-stage absorption tower, so that the fly ash calcium calcium slag slurry is in contact with the industrial exhaust gas for 20 minutes;
[0047] The steps in the other absorption towers are the same as in Example 1. After being absorbed by the ...
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