Active coke adsorption tower and method for adsorbing and purifying flue gas by active coke
A technology of activated coke and adsorption tower, which is applied in the field of activated coke adsorption tower and activated coke adsorption and purification of flue gas, and can solve the problems of secondary pollution of ammonia and low adsorption capacity of activated coke.
Patent Information
- Authority / Receiving Office
- CN · China
- Current Assignee / Owner
- Publication Date
- 2020-03-24
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Abstract
Description
technical field
[0001] The present disclosure relates to the technical field of activated coke dry flue gas desulfurization, in particular to an activated coke adsorption tower and a method for activated coke adsorption and purification of flue gas. Background technique
[0002] The activated coke dry flue gas purification process began to be applied industrially in the 1980s. With the increasing environmental protection requirements, the activated coke dry flue gas purification process has outstanding advantages such as high desulfurization efficiency, simultaneous removal of multiple pollutants, no water consumption for reaction, no waste water and waste residue discharge, and no corrosion problems for system equipment. More and more attention has been paid to it, and the application of this process is becoming more and more extensive.
[0003] Activated coke has the functions of desulfurization, denitrification, dust removal and simultaneous removal of various pollutants...
Examples
Embodiment
[0066] This example is used to illustrate the method for purifying flue gas by activated coke adsorption of the present disclosure.
[0067] Such as figure 2 As shown, the adsorption tower adopts a three-stage cross-flow adsorption structure, and the flue gas 1 to be purified in the comparative example is used. From the upstream device, it first enters the inlet gas buffer A4 of the adsorption tower A, and then passes through the first-stage cross-flow adsorption bed A1 , cross-flow contact with activated coke to remove most of the SO in the flue gas 2 . The flue gas from the first-stage cross-flow adsorption bed A1 enters the first inter-stage gas buffer zone A5, where it is evenly mixed with the denitrification ammonia injection 5, and then enters the second-stage cross-flow adsorption bed A2, where it is mixed with the active coke cross-flow contact to remove the remaining SO 2 and NO X . The flue gas from the second-stage cross-flow adsorption bed layer A2 enters the...