Preparation method of wet desulphurization absorbent for flue gas from coal fired boiler
A technology for coal-fired boilers and wet desulfurization, which is applied in separation methods, chemical instruments and methods, and separation of dispersed particles. It can solve the problems of high operating costs, large power consumption, and large investment, so as to reduce operating costs and extend service life. Longevity, cheap effect
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Embodiment 1
[0021] Through the test, the SO in the flue gas of large coal-fired power plant boilers 2 The concentration is 1000mg / m 3 , the flue gas flow rate is 38×10 4 m 3 / h. Select fly ash after burning low-sulfur coal, select limestone powder, and sieve fly ash and limestone powder respectively, so that the particle size of fly ash and limestone powder is less than 80 microns, and the composition of limestone powder is loss on ignition 40.79 %, silicon 4.62%, aluminum 1.21%, iron 0.52%, calcium 50.16%. According to SO in flue gas of coal-fired boiler 2 The concentration of the limestone powder is weighed according to the calcium-sulfur molar ratio of 0.7 to remove 1000mg of SO 2 , requires 0.9g of limestone powder. According to the mass ratio of fly ash to limestone powder is 1, 0.9g of fly ash after combustion of low-sulfur coal is selected. At the same time, according to the liquid-gas mass / volume ratio of 101g / m 3 The proportion of the selected 10lg of 20 ℃ ~ 30 ℃ of water...
Embodiment 2
[0023] Through the test, the SO in the flue gas of large coal-fired power plant boilers 2 The concentration is 2000mg / m 3 , the flue gas flow rate is 80×10 4 m 3 / h. Select fly ash after burning low-sulfur coal, select limestone powder, and sieve fly ash and limestone powder respectively, so that the particle size of fly ash and limestone powder is less than 80 microns, and the composition of limestone powder is loss on ignition 40.79 %, silicon 4.62%, aluminum 1.21%, iron 0.52%, calcium 50.16%. According to SO in flue gas of coal-fired boiler 2 The concentration of the limestone powder is weighed according to the calcium-sulfur molar ratio of 0.9 to remove 2000mg of SO 2 , requires 2.2g of limestone powder. According to the mass ratio of fly ash to limestone powder of 0.8, 1.8g of fly ash after burning low-sulfur coal is selected. At the same time, according to the liquid-gas mass / volume ratio of 13lg / m 3 The proportion of the selected 13lg of 20 ℃ ~ 30 ℃ of water. A...
Embodiment 3
[0025] Through the test, the SO in the flue gas of large coal-fired power plant boilers 2 The concentration is 3000mg / m 3 , the flue gas flow rate is 130×10 4 m 3 / h. Select fly ash after burning low-sulfur coal, select limestone powder, and sieve fly ash and limestone powder respectively, so that the particle size of fly ash and limestone powder is less than 80 microns, and the composition of limestone powder is loss on ignition 40.79 %, silicon 4.62%, aluminum 1.21%, iron 0.52%, calcium 50.16%. According to SO in flue gas of coal-fired boiler 2 Concentration, according to the ratio of calcium sulfur molar ratio of 1.1 to take limestone powder, remove 3000mg of SO 2 , need 4.1g of limestone powder. According to the ratio of fly ash to limestone powder mass ratio of 0.6, select 2.5g of fly ash after combustion of low-sulfur coal. At the same time, according to the liquid-gas mass / volume ratio of 16lg / m 3The proportion of the selected 16lg of 20 ℃ ~ 30 ℃ of water. Acco...
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