A treatment process for industrial flue gas
A technology of industrial flue gas and treatment process, which is applied in the direction of combustion product treatment, waste gas exhaust device, combustion method, etc., can solve the problem of unrecovered flue gas purification process resistance drop, etc., to increase flue gas purification efficiency and flexibly switch , Reduce the effect of drag drop
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Embodiment 1
[0025] combined with figure 1 For the flue gas pipeline of the present invention, the process of treating catalytic cracking regenerated flue gas and the operation method when some equipment in the flue gas pipeline needs to be overhauled:
[0026] The process of the two sets of flue gas pipelines processing the regenerated flue gas: the regenerated flue gas from the catalytic cracking unit enters the two sets of flue gas pipelines, and the operation mode of the regenerated flue gas in the two sets of flue gas pipelines is: first enter The flue gas pipeline I passes through the water-sealed tank, and then enters the waste heat recovery boiler to recover the heat energy and chemical energy in the regeneration flue gas; if the regeneration flue gas does not need to be purified, the regeneration flue gas enters the chimney through the flue gas pipeline II to be emptied; When the flue gas needs to be purified, close the isolation valve I on the flue gas pipeline II, open the isola...
Embodiment 2
[0033] The total amount of regenerated flue gas of a 1.05 million tons / year catalytic cracking unit is 160000Nm 3 / h, set up two waste heat recovery boilers to recover flue gas energy, and the flue gas needs to be further purified before being discharged into the atmosphere. figure 1 The design of the process flow from the waste heat recovery boiler outlet to the inlet of the flue gas purification equipment adopts the flow design of the drawing, and the resistance drop of the corresponding piping system is less than 1KPa. If water-sealed tanks are designed to separate the outlet of the waste heat recovery boiler and the inlet of the flue gas purification equipment, the resistance drop of the piping system will increase by about 2-4KPa.
Embodiment 3
[0035] The total amount of regenerated flue gas of a catalytic cracking unit is 138000Nm 3 / h, set up two waste heat recovery boilers to recover flue gas energy, and the flue gas needs to be further purified before being discharged into the atmosphere; there is another 3000Nm 3 / h Hydrogen sulfide incineration tail gas needs to be further purified before being discharged into the atmosphere, according to the attached figure 1 The principle design of the process flow, from the outlet of the waste heat recovery boiler (incinerator) to the inlet of the flue gas purification equipment adopts the flow design of the drawing, and the corresponding resistance drop of the pipeline system is less than 1KPa. If water-sealed tanks are designed to separate the outlet of the waste heat recovery boiler (incinerator) and the inlet of the flue gas purification equipment, the resistance drop of the pipeline system will increase by about 2 to 5KPa.
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