A system for preparing magnesium sulfate from slurry after flue gas desulfurization
A technology of magnesium sulfate and flue gas, which is applied in the direction of magnesium sulfate, dispersed particle separation, chemical instruments and methods, etc., can solve the problems of increasing system energy consumption, increasing floor area, and decreasing purity, so as to reduce system energy consumption, Improve efficiency and save space
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[0032] Attached below figure 1 The system for preparing magnesium sulfate of the present invention is introduced in detail.
[0033] The system for preparing magnesium sulfate of the present invention includes a device for adjusting the oxygen content of flue gas, preferably a supplementary oxidizing air device. The system of the present invention may also include a pulping device, a desulfurization device, a filtration device, an evaporation device, a cooling crystallization device, and a separation device. The system of the present invention may also include drying means and packaging means.
[0034] The system of the present invention includes a desulfurization device, the desulfurization device is provided with a pre-desulfurization flue, and the flue gas oxygen content adjustment device is arranged on the pre-desulfurization flue, and the flue gas oxygen content adjustment device is used to control the desulfurization. Oxygen content in flue gas, and keep the oxygen con...
Embodiment 1
[0057] Step 1: Add magnesium oxide powder to high-temperature condensed water from an evaporator at 60°C to make a magnesium hydroxide slurry, and pump it to the absorption tower.
[0058] Step 2: Control the oxygen content of the flue gas before desulfurization in Table 1 to 18% by using the flue gas oxygen content regulating device.
[0059] Step 3: The flue gas velocity at the entrance of the absorption tower is 3m / s, and the flue gas temperature at the entrance is 120°C. The pH value of the slurry tank area at the bottom of the absorption tower is controlled to fluctuate between 6 and 7 to obtain a magnesium sulfate solution.
[0060] Step 4: pass the magnesium sulfate solution through a precision filter of no less than 300 mesh filter media to achieve fine filtration of the magnesium sulfate solution.
[0061] Step 5: Set the temperature at 30°C and the density at 1.2t / m 3 The magnesium sulfate solution is sent to the three-effect evaporator for evaporation to obtain a te...
Embodiment 2
[0073] Under the same working conditions as in Example 1, step 2: utilize the flue gas oxygen content regulating device to control the flue gas oxygen content before desulfurization respectively at 23%, the desulfurization effect obtained and the magnesium sulfate output are as follows:
[0074] Table 4 Emissions and magnesium sulfate output of desulfurization projects with 23% oxygen content
[0075] serial number
project
quantity
unit
1
Flue gas volume at the outlet of the desulfurization unit (working condition)
1384210
m 3 / h
2
exhaust temperature
50
℃
3
SO 2 emission concentration
<40
mg / Nm 3
4
Magnesium sulfate output
4.5
t / h
5
>98
% mass percentage
[0076] Magnesium sulfate quality and its test method are the same as in Table 3.
[0077] It can be seen from Examples 1 to 2 that the present invention utilizes the m...
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