Integrated energy-saving scr denitrification device
A denitrification and thermal fluid technology, applied in chemical instruments and methods, separation methods, dispersed particle separation, etc., can solve problems such as high reaction temperature, high temperature flue gas evacuation, energy waste, etc., to reduce dust content and reduce operating costs , the effect of reducing operating costs
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Embodiment 1
[0028] An integrated energy-saving SCR denitration device, including an SCR denitration reaction chamber 1 and a heat exchange chamber 2; the cold fluid inlet of the heat exchange chamber 2 is connected to the flue gas before the reaction, and the cold fluid outlet is connected to the smoke inlet port connection; the thermal fluid inlet of the heat exchange chamber 2 is connected to the smoke outlet of the SCR denitration reaction chamber 1, and the thermal fluid outlet is a smoke exhaust port. That is, the pre-reaction flue gas entering the SCR denitrification reaction chamber 1 is used as a cold fluid, and the post-reaction flue gas flowing out of the SCR denitrification reaction chamber 1 is used as a hot fluid, which respectively flows through the heat exchange chamber 2 to utilize the post-reaction flue gas. The residual heat of the flue gas increases the reaction temperature of the pre-reaction flue gas, and the pre-reaction flue gas passing through the heat exchange cham...
Embodiment 2
[0031] The temperature of the pre-reaction flue gas after passing through the heat exchange chamber sometimes does not reach the reaction temperature required by the SCR denitration reaction chamber 1. Therefore, before the pre-reaction flue gas enters the SCR denitration reaction chamber 1, the flue gas temperature needs to be adjusted. .
[0032] Therefore, in the preferred technical solution of Embodiment 2 of the present invention, it also includes a flue gas temperature adjustment chamber 3 and a flue gas temperature control system (not shown in the figure), and a heater (not shown in the figure) is installed in the flue gas temperature adjustment chamber 3 ); the smoke inlet of the flue gas temperature adjustment chamber 3 is connected to the cold fluid outlet of the heat exchange chamber 2, and the smoke outlet is connected to the smoke inlet of the SCR denitration reaction chamber 1.
[0033]The flue gas temperature control system includes a controller and a temperatur...
Embodiment 3
[0036] In the existing SCR denitrification technology, it is necessary to use an appropriate reducing agent (eg, ammonia, urea, etc.) as a reducing agent for catalytic reactions under certain conditions to convert nitrogen oxides into harmless nitrogen and water vapor. Therefore, before the pre-reaction flue gas enters the SCR denitrification reaction chamber 1, it is necessary to add an appropriate amount of reducing agent to the pre-reaction flue gas to promote the catalytic reaction and effectively decompose the harmful substances in the flue gas.
[0037] The preferred technical solution of this embodiment 3 is to further include a gas mixing chamber 4 and a reducing agent supply unit 5; before flowing into the SCR denitration reaction chamber 1, the pre-reaction gas is connected to the gas mixing chamber 4, The flue gas before the reaction after mixing the reducing agent flows into the SCR denitration reaction chamber 1; the gas injection port 51 of the reducing agent supp...
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