Method for separating particulate matter, sulfur vapor and sulfur dioxide in smoke and application of method
A sulfur dioxide and sulfur vapor technology, applied in separation methods, dispersed particle filtration, chemical instruments and methods, etc., can solve problems such as poor economy, complex process, ineffective separation, etc., and achieve reduced energy consumption, simple process, and low filtration pressure. Effect
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Embodiment 1
[0045] Such as figure 2 Shown, the method for particulate matter, sulfur vapor and sulfur dioxide in the separation flue gas of the present invention comprises the following steps:
[0046] 1) Using the heat recovery device 4 to reduce the temperature of the flue gas to 350° C., wherein the flue gas is a gas composed of particulate matter, sulfur vapor and sulfur dioxide produced by the reaction of sulfur vapor and phosphogypsum;
[0047] 2) Use the membrane filter 1 to filter the cooled flue gas, the filtering temperature is 300°C, and the filtering wind speed is 0.5m / min; the particulate matter in the flue gas is intercepted by the filter medium of the membrane filter 1, The flue gas passes through the filter medium of the membrane filter 1 to obtain the first flue gas; the material of the filter medium is an intermetallic compound, the pore size is 10 μm, and the gas flux is 300 m 3 / m 2 kPa h;
[0048] 3) The first flue gas passes through a condenser 2 with a condensat...
Embodiment 2
[0051] Such as figure 2 Shown, the method for particulate matter, sulfur vapor and sulfur dioxide in the separation flue gas of the present invention comprises the following steps:
[0052] 1) Using the heat recovery device 4 to reduce the temperature of the flue gas to 400° C., wherein the flue gas is a gas composed of particulate matter, sulfur vapor and sulfur dioxide produced by the reaction of excess sulfur vapor and phosphogypsum;
[0053] 2) Use the membrane filter 1 to filter the cooled flue gas, the filtration temperature is 350°C, and the filtration wind speed is 0.9m / min; the particulate matter in the flue gas is intercepted by the filter medium of the membrane filter 1, The flue gas passes through the filter medium of the membrane filter 1 to obtain the first flue gas; the material of the filter medium is an intermetallic compound, the pore size is 15 μm, and the gas flux is 480 m 3 / m 2 kPa h;
[0054] 3) The first flue gas is passed through a condenser 2 with...
Embodiment 3
[0057] Such as figure 2 Shown, the method for particulate matter, sulfur vapor and sulfur dioxide in the separation flue gas of the present invention comprises the following steps:
[0058] 1) Using the heat recovery device 4 to reduce the temperature of the flue gas to 450° C., wherein the flue gas is a gas composed of particulate matter, sulfur vapor and sulfur dioxide produced by the reaction of excess sulfur vapor and phosphogypsum;
[0059] 2) Use the membrane filter 1 to filter the cooled flue gas, the filtration temperature is 400°C, and the filtration wind speed is 1.3m / min; the particulate matter in the flue gas is intercepted by the filter medium of the membrane filter 1, The flue gas passes through the filter medium of the membrane filter 1 to obtain the first flue gas; the material of the filter medium is an intermetallic compound, the pore size is 20 μm, and the gas flux is 570 m 3 / m 2 kPa h;
[0060] 3) Make the first flue gas pass through a condenser 2 with...
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