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Method for treating desulfurization ash

A treatment method, desulfurization ash technology, applied in separation methods, chemical instruments and methods, dispersed particle separation, etc., can solve the problems of excessive leaching toxicity, high loss on ignition, difficult process control, etc., and achieve the elimination of large fluctuations in components and effective Obvious, simple process effect

Active Publication Date: 2011-04-06
BAOSHAN IRON & STEEL CO LTD
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Problems solved by technology

[0003] Due to the high Ca / S of dry / semi-dry flue gas desulfurization process, low utilization rate of desulfurization agent, slow reaction speed, and difficult process control, the chemical composition of desulfurization ash fluctuates greatly and the content of unstable components is high. Therefore, the utilization mode of desulfurization ash and The scope of application is strictly limited: (1) The properties of desulfurization ash are very unstable during the utilization process, such as CaSO 3 Oxidizes slowly in humid environment, decomposes in acidic environment and high temperature, Ca(OH) 2 and CaCO 3 Pyrolysis produces CaO, and f-CaO will cause volume expansion of cement and concrete during the hydration process; (2) Excessive sulfur content limits the use of desulfurized ash as cement and concrete admixtures, because in ordinary According to the national standard of cement, SO in cement 3 (3) The leaching toxicity of desulfurization ash exceeds the standard, which is a hazardous waste, and the safety and later stability of agricultural or building materials need to be further evaluated; (4) SiO 2 +Al 2 o 3 +Fe 2 o 3 If the content is too low, it will affect the chemical activity of desulfurization ash, and the MgO and ignition loss will be higher; (5) Desulfurization ash is easy to raise dust, and secondary pollution is prone to occur during transportation, storage and utilization
[0004] At present, the research on the characteristics and application of calcium sulfite desulfurization ash is not in-depth at home and abroad, and no technical approach for large-scale industrial utilization has been found. Environment, occupying land, causing secondary pollution, and directly affecting the application and promotion of dry / semi-dry desulfurization process

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  • Method for treating desulfurization ash

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Embodiment 1

[0036] A kind of processing method of desulfurization ash, technological process is as follows figure 2shown. On the top of the desulfurizing agent slurry preparation box of the desulfurizing agent preparation system 1, there is a desulfurizing ash powder silo 11 and a limestone powder silo, and desulfurizing ash and limestone powder are used as raw materials for the desulfurizing agent, and the desulfurizing ash is obtained from a circulating fluidized bed dry process Flue gas desulfurization process, where CaSO 4 ·H 2 O mass fraction is 6.7%, CaSO 3 1 / 2H 2 O mass fraction is 59.6%, f-CaO mass fraction is 14.3%, Ca(OH) 2 The mass fraction is 9.5%, SiO 2 The mass fraction is 6.2%, Al 2 o 3 Mass fraction is 1.1%, MgO mass fraction is 0.5%, Fe 2 o 3 The mass fraction is 0.4%, where CaSO 3 1 / 2H 2 O, CaCO 3 , f-CaO and Ca(OH) 2 The total mass fraction of the four substances is 90.1%. The desulfurized ash and limestone powder are mixed according to the mass fraction r...

Embodiment 2

[0038] A kind of processing method of desulfurization ash, technological process is as follows figure 2 shown. On the top of the desulfurizing agent slurry preparation box of the desulfurizing agent preparation system 1, there is a desulfurizing ash powder silo 11 and a limestone powder silo. Desulfurizing ash and limestone powder are used as raw materials for the desulfurizing agent. The desulfurizing ash is taken from the furnace and sprayed with calcium oxide. Activation of semi-dry desulfurization process, where CaSO 4 ·H 2 O mass fraction is 21.5%, CaSO 3 1 / 2H 2 O mass fraction is 45.5%, f-CaO mass fraction is 10.4%, Ca(OH) 2 The mass fraction is 8.5%, SiO 2 The mass fraction is 3.1%, Al 2 o 3 Mass fraction is 0.8%, MgO mass fraction is 0.2%, Fe 2 o 3 The mass fraction is 0.1%, where CaSO 3 1 / 2H 2 O, CaCO 3 , f-CaO and Ca(OH) 2 The total mass fraction of the four substances is 64.4%. The desulfurized ash and limestone powder are mixed according to the mass f...

Embodiment 3

[0040] A kind of processing method of desulfurization ash, technological process is as follows figure 2 shown. On the top of the desulfurizing agent slurry preparation box of the desulfurizing agent preparation system 1, there is a desulfurizing ash powder silo 11 and a limestone powder silo. Desulfurizing ash and limestone powder are used as raw materials for the desulfurizing agent. The desulfurizing ash is obtained from limestone flue gas purification semi-dry desulfurization process, where CaSO 4 ·H 2 O mass fraction is 22.2%, CaSO 3 1 / 2H 2 O mass fraction is 45.8%, f-CaO is 8.5%, Ca(OH) 2 The mass fraction is 9.5%, SiO 2 The mass fraction is 3.1%, Al 2 o 3 Mass fraction is 0.8%, MgO mass fraction is 0.2%, Fe 2 o 3 The mass fraction is 0.1%, where CaSO 3 1 / 2H 2 O, CaCO 3 , f-CaO and Ca(OH) 2 The total mass fraction of the four substances is 63.8%. The desulfurized ash and limestone powder are mixed according to the mass fraction ratio of 1:4, mixed into the d...

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Abstract

The invention discloses a method for treating desulfurization ash. The method comprises the following steps of: mixing the desulfurization ash generated by a dry / semidry desulphurization process and limestone powder, which serve as raw materials of a desulfurizer in a wet flue gas desulfurization process, according to a proportion; uniformly stirring the desulfurizer and pumping the desulfurizer into a slurry pond of an absorption tower; adding a catalyst into the slurry pond; introducing oxidation air into the slurry pond; introducing flue gas into the slurry pond through a flue; reacting the desulfurizer with SO2 in the flue gas under the action of the oxidation air and the catalyst; controlling the pH value of the slurry in the absorption tower, the slurry temperature, the content of solid matters contained in the slurry and the retention time of the desulfurizer in the slurry pond; after the reaction is completed, performing vortex concentration and vacuum filtration to obtain a gypsum by-product; and adding wastewater produced in the process into a process water collection box for recycling. The method is simple, is easy to realize, has remarkable effect, provides a safe and proper treatment way for the dry / semidry desulfurization ash and has good economic and social benefits.

Description

technical field [0001] The invention belongs to the field of flue gas desulfurization, and in particular relates to a method for treating dry / semi-dry desulfurization ash by using a limestone-gypsum wet flue gas desulfurization process. Background technique [0002] Flue gas desulfurization in SO 2 Plays an important role in pollution prevention and control. According to the different desulfurization processes, the calcium desulfurization process is divided into wet method, dry method and semi-dry method, and the dry method / semi-dry method has the advantages of desulfurization products in dry powder form and low water consumption in the process. , no wet smoke emission, less corrosion, and strong adaptability to small and medium coal-fired units, etc., occupying a place in the desulfurization market. [0003] Due to the high Ca / S of dry / semi-dry flue gas desulfurization process, low utilization rate of desulfurization agent, slow reaction speed, and difficult process contro...

Claims

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Application Information

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IPC IPC(8): B01D53/50B01D53/78B01D53/80B01D53/81B01D53/96
Inventor 石磊沈晓林陈荣欢王如意刘道清周晶
Owner BAOSHAN IRON & STEEL CO LTD
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