Cement kiln system high-temperature raw material online desulfurization technology
A cement kiln, high temperature technology, applied in membrane technology, gas treatment, dispersed particle separation, etc., can solve the problems of unfavorable energy saving, environmental protection, large amount of raw meal at high temperature, etc.
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Embodiment 1
[0019] Step 1: Determine the best feeding location and feeding location, and extract high-temperature raw meal powder from a reasonable feeding location;
[0020] Step 2: After scientifically and reasonably integrating and processing through the diversion pipeline, integrated module and control module designed by the device, the gas rich in active CaO is introduced into a reasonable feeding position in an appropriate amount;
[0021] Step 3: The extracted high-temperature raw material gas is fully mixed and contacted with the sulfur-containing flue gas collected by the first-stage cyclone, and the CaO and SOx in the flue gas 2 A chemical reaction occurs to generate highly stable calcium sulfate;
[0022] Step 4: The dust containing calcium sulfate is collected by the original device, and sent back to the raw material homogenization warehouse through the original conveying equipment, and the clean exhaust gas is discharged from the chimney at the end of the kiln.
[0023] Amon...
Embodiment 2
[0026] Example 2: The average residence time of high-temperature raw meal and flue gas in the humidification pipeline can reach 8.0-10.0s, and the average reaction temperature can reach 300°C, and the amount of water sprayed in the humidification pipeline is 2-4t / h, theoretically The moisture content of the flue gas can be increased by about 1.6%, which will be more conducive to the desulfurization reaction.
[0027] The molar ratio of calcium to sulfur, according to the previous project operation experience, the initial SO 2 When the concentration is reduced from 150-200mg / Nm3 to 50mg / Nm3, the molar ratio of calcium to sulfur is generally 15-20; 2 When the initial concentration is reduced from 300-500mg / Nm3 to 50mg / Nm3, the molar ratio of calcium to sulfur is generally 30-40. When the SO2 emission concentration is less than 300mg / Nm3, use the pipeline from the calciner to the C2 ascending flue. When the SO2 emission concentration When it is greater than 300mg / Nm3, the pipeli...
Embodiment 3
[0029] Embodiment 3: The system pipeline is scientifically and rationally designed according to the actual situation on site, to ensure the smooth flow of the pipeline while minimizing the pressure loss, to ensure the smooth flow of the pipeline, and the stable operation of the system. The whole system is programmed by the PLC centralized control cabinet next to the machine Control, the control cabinet is equipped with a communication interface with DCS, which can realize remote control, and all system parameters and controls can be uniformly operated by DCS system staff.
[0030] SO 2 When the emission value does not exceed the standard, it is not necessary to open the valve of the desulfurization system for desulfurization. After the raw material mill is shut down, according to the SO 2 The discharge value of the desulfurization system can be adjusted according to the valve opening of the desulfurization system for desulfurization. 2 The concentration change is adjusted at ...
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