System and method for multistage desulfurization rich liquid cavitation desorption of sulfur dioxide
A technology for desulfurization rich liquid and sulfur dioxide, applied in chemical instruments and methods, sulfur compounds, separation methods, etc., can solve the problems of high investment, large-scale heat transmission equipment and water vapor condensation equipment, high heat consumption, etc., to reduce condensation load , The effect of reducing the steam condensation load and reducing the amount of condensation
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Embodiment 1
[0048] Taking the system of three-stage desulfurization rich liquid cavitation desorption sulfur dioxide as an example, set the cavitation desorption temperature of the basic aluminum sulfate desulfurization rich liquid in the cavitation desorption chamber 2 of the final cavitation desorption unit to be 55°C, and the cavitation desorption temperature of the two adjacent cavitation desorption units The inter-stage temperature difference of desulfurization rich liquid cavitation desorption temperature of the desulfurization desorption unit is set at 5°C, and the cavitation temperature of desulfurization rich liquid in the same stage is the same as that of the steam or steam, SO 2 The temperature difference of the mixed gas is set at 5°C; the exhaust steam from the steam turbine operating at a back pressure of 12.34kPa is used as the supply for cavitation desorption of SO 2 The heat source of the heat, the exhaust steam of the steam turbine corresponds to a steam temperature of ab...
Embodiment 2
[0064] Taking the system of three-stage desulfurization rich liquid cavitation desorption sulfur dioxide as an example, set the cavitation desorption temperature of the basic aluminum sulfate desulfurization rich liquid in the cavitation desorption chamber 2 of the final cavitation desorption unit to be 55°C, and the cavitation desorption temperature of the two adjacent cavitation desorption units The inter-stage temperature difference of desulfurization-rich liquid cavitation desorption temperature of the desulfurization desorption unit is set at 5°C, and the cavitation temperature of the desulfurization-rich liquid cavitation temperature of the cavitation desorption unit of the same stage is the same as that of the steam or steam in the steam heating chamber 3, SO 2 The temperature difference of the mixed gas is set at 5°C; the exhaust steam from the steam turbine operating at a back pressure of 31.16kPa is used as the supply for cavitation desorption of SO 2 As the heat sour...
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