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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

Pending Publication Date: 2020-06-12
温高
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0006] In view of the above problems, the purpose of the present invention is to provide a system and method for multi-stage desulfurization rich liquid cavitation desorption of sulfur dioxide, to solve the problem of desorption of SO2 by alkaline aluminum sulfate desorption desulfurization method. 2 Problems of high heat consumption, large-scale heat transfer equipment and water vapor condensing equipment, and high investment

Method used

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  • System and method for multistage desulfurization rich liquid cavitation desorption of sulfur dioxide

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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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Abstract

The invention discloses a system and a method for multistage desulfurization rich liquid cavitation desorption of sulfur dioxide. The system for multistage desulfurization rich liquid cavitation desorption of sulfur dioxide comprises multistage cavitation desorption units, each stage of cavitation desorption unit is divided into an upper chamber and a lower chamber by a heating surface, the upperchamber is a cavitation desorption chamber, and the lower chamber is a steam heating chamber; and an exhaust port of the cavitation desorption chamber of each preceding-stage cavitation desorption unit is connected to a steam inlet of the steam heating chamber of the next-stage cavitation desorption unit, and a condensed water outlet of the steam heating chamber of each next-stage cavitation desorption unit is connected to a desorption solution inlet of the cavitation desorption chamber of the preceding-stage cavitation desorption unit. The method for multistage desulfurization rich solution cavitation desorption of sulfur dioxide involves multistage cavitation desorption units, steam generated during cavitation of cavitation desorption chamber of each preceding-stage cavitation desorptionunit is used as heating steam of the steam heating chamber of the next-stage cavitation desorption unit to perform cavitation desorption on SO2 in the stage of cavitation desorption chamber, and desorption steam heat energy of the previous stage becomes a next-stage cavitation desorption heat absorption source.

Description

technical field [0001] The invention belongs to the fields of energy and power engineering and environmental engineering, and in particular relates to a system and method for multi-stage desulfurization rich liquid cavitation desorption of sulfur dioxide. Background technique [0002] At present, the combustion of sulfur co-generated with coal produces SO 2 Air pollution is one of the factors that form acid rain and smog weather. At the same time, my country is a country that is poor in available sulfur resources. Therefore, efficient removal and recovery of SO from coal-fired flue gas 2 The advanced method has been the subject of people's research and exploration. [0003] The basic aluminum sulfate desorption desulfurization method, theoretically speaking, is a kind of removal and desorption of SO 2 High efficiency, desulfurization rich liquid desorption SO 2 The regenerated basic aluminum sulfate is recycled, and the desorption product is high-purity SO 2 It can be s...

Claims

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Application Information

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IPC IPC(8): B01D53/14C01B17/56
CPCB01D53/1418B01D53/1425B01D53/1481B01D2252/10B01D2258/0283C01B17/56
Inventor 温高温日辉
Owner 温高
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