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Method for recycling desulfurization byproduct of power plant

A desulfurization by-product, power plant technology, applied in the direction of thiosulfate/dithionite/polythionate, etc., can solve the problem of unsatisfactory data reproducibility, unstable properties of calcium sulfite, and reduced desulfurization efficiency and other problems, to achieve the effect of fewer types of chemicals, fewer types of equipment, and improved desulfurization efficiency

Inactive Publication Date: 2020-04-17
郑州中科新兴产业技术研究院 +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Calcium sulfite is unstable, not only may itself pollute the water body, but may re-release SO after decomposition 2 into the flue gas, thereby reducing the desulfurization efficiency
At present, most power plants treat calcium sulfite by oxidizing it, but the oxidation of calcium sulfite, whether it is homogeneous or heterogeneous, depends on the specific experimental parameters, such as liquid phase composition (concentration of sulfite, dissolved oxygen, pH value), temperature, trace catalyst (inhibitor), etc., can all have a very significant impact on the reaction rate, so the data reproducibility of this type of experiment is not very ideal

Method used

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  • Method for recycling desulfurization byproduct of power plant

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0021] Add 100g of calcium sulfite, 100g of soda ash, and 1L of deionized water into the reaction kettle, heat up to 60°C while stirring, react for 1 hour and then filter to obtain 940mL of filtrate. Put the filtrate and 300g of sublimed sulfur into the reactor and heat to 90°C, stir and react for 2 hours, then filter to obtain 860mL of filtrate, put the filtrate into the crystallization kettle and evaporate it under reduced pressure for 1 hour, the pressure of the crystallization kettle is -0.01MPa, and the temperature is 30°C. After drying, the obtained filter residue was soda, with a weight of 122.4 g.

Embodiment 2

[0023] Add 120 g of calcium sulfite, 106 g of soda ash, and 1.5 L of deionized water into the reaction kettle, heat and stir at 100° C. for 1 hour, and then filter to obtain 1.36 L of filtrate. Put the filtrate and 400 g of sublimed sulfur into the reactor, heat and stir at 105°C for 2 hours, then filter to obtain 1.2 L of filtrate. The filtrate was added to the crystallization kettle and evaporated under reduced pressure for 1 hour. The pressure of the crystallization kettle was -0.005MPa, and the temperature was 40°C. After drying, the obtained filter residue was soda, weighing 152.7g.

Embodiment 3

[0025] Add 100 g of calcium sulfite, 150 g of soda ash, and 2 L of deionized water into the reaction kettle, heat and stir at 110° C. for 1 hour, and then filter to obtain 1.14 L of filtrate. The filtrate and 500 g of sublimed sulfur were put into a reaction kettle, heated and stirred at 110° C. for 2 hours, and then filtered to obtain 970 mL of filtrate. The filtrate was added to the crystallization kettle and evaporated under reduced pressure for 1 hour. The pressure of the crystallization kettle was -0.01MPa and the temperature was 50°C.

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Abstract

The invention provides a method for recycling a desulfurization byproduct of a power plant. The method comprises the following steps: adding water into a reaction kettle to emulsify calcium sulfite, adding sodium carbonate after the emulsifying, performing heating and stirring, and performing filtering; adding sulfur powder into the obtained filtrate, heating and stirring, filtering again, and recycling filter residues in the heating and stirring process; and enabling the obtained filtrate to enter a crystallization kettle, performing reduced-pressure evaporation crystallization, filtering, returning the obtained filtrate to the crystallization kettle, and drying filter residues to obtain sodium thiosulfate. The method can recover the desulfurization byproduct calcium sulfite of the powerplant, thereby enhancing the desulfurization efficiency; the process is simple, the types of required chemicals are few, only sodium carbonate and the sulfur powder are required, and the types of required equipment are few; the product sodium thiosulfate is large in application range; and the purity requirement of calcium sulfite is low, and the final product sodium thiosulfate generated by low-purity calcium sulfite can be directly added with potassium ferrocyanide and the like as an environment-friendly gold extracting agent.

Description

technical field [0001] The invention relates to the field of desulfurization by-products in power plants, in particular to a method for recovering and reusing the desulfurization by-products in power plants. Background technique [0002] Thermal Power Plant SO 2 The main emission reduction measures are to change fuels, reduce fuel sulfur content, shut down small units and install flue gas desulfurization and other measures. When the potential of measures such as changing fuels and reducing the sulfur content of coal combustion in our country is very small, if we want to further reduce SO 2 Displacement, the key is to set the flue gas desulfurization device port. So far, my country has not fully mastered the core technology of flue gas desulfurization design and equipment supply capacity. There are continuous problems in actual desulfurization operation, and the problem of fouling and blockage is the first to bear the brunt. In the process of flue gas desulfurization, the ...

Claims

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Application Information

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IPC IPC(8): C01B17/64
CPCC01B17/64
Inventor 李申郭强李永利李道荣田登超付明波赵俊利朱顺伟李会林张灵
Owner 郑州中科新兴产业技术研究院
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