阅读说明：本技术 一种飞灰脱氯方法 (Fly ash dechlorination method ) 是由 陈宏衍 郑世恩 于 2021-09-08 设计创作，主要内容包括：本发明提供了一种飞灰脱氯方法,包括以下步骤：S10：将飞灰溶解在脱氯介质中,然后加入疏水剂,得到第一过程混合物；S20：在第一过程混合物中加入第一脱氯剂混合均匀,得到第二过程混合物；S30：对第二过程混合物进行压滤处理,得到脱氯飞灰和废水。与常规飞灰水洗脱氯相比,发明提供的飞灰脱氯方法用水量只需原来的15-25％,且无其他次生废弃物。(The invention provides a fly ash dechlorination method, which comprises the following steps: s10: dissolving fly ash in dechlorination medium, and adding hydrophobic agent to obtain first process mixture; s20: adding a first dechlorinating agent into the first process mixture, and uniformly mixing to obtain a second process mixture; s30: and carrying out filter pressing treatment on the mixture in the second process to obtain dechlorinated fly ash and wastewater. Compared with the conventional fly ash washing dechlorination, the fly ash dechlorination method provided by the invention only needs 15-25% of the original water consumption, and has no other secondary waste.)

1. A fly ash dechlorination method is characterized by comprising the following steps:

s10: dissolving fly ash in dechlorination medium, and adding hydrophobic agent to obtain first process mixture;

s20: adding a first dechlorinating agent into the first process mixture, and uniformly mixing to obtain a second process mixture;

s30: and carrying out filter pressing treatment on the mixture in the second process to obtain dechlorinated fly ash and wastewater.

2. A fly ash dechlorination process according to claim 1, wherein the mass ratio of the fly ash to the dechlorination medium is (0.8-1.5): 1.

3. The method of claim 1,

the hydrophobic agent is a silicon compound, and/or,

the addition amount of the hydrophobic agent is 0.3-1.7% of the mass of the fly ash.

4. A fly ash dechlorination process according to claim 3, wherein the silicon based compounds comprise: at least one of water glass, quartz sand and silica.

5. A fly ash dechlorination process according to claim 1, wherein the S20 comprises the steps of:

s21: adjusting the pH of the first process mixture to 7-7.5;

s22: and controlling the temperature of the first process mixture to be 40-45 ℃, adding the first dechlorinating agent, and uniformly mixing to obtain a second process mixture.

6. A fly ash dechlorination process according to claim 5, wherein S21 is in particular:

adding an acidic additive to the first process mixture,

the adding amount of the acidic additive is 2-5% of the mass of the first process mixture.

7. A fly ash dechlorination process according to claim 6 wherein the acidic additive is one or more of sulphuric acid, nitric acid, hydrochloric acid.

8. A fly ash dechlorination process according to claim 1, wherein the first dechlorinating agent is alumina and hydrogen peroxide.

9. A fly ash dechlorination process according to claim 1, further comprising:

s40: adding a second dechlorinating agent into the wastewater, and uniformly mixing to obtain dechlorinated reclaimed water;

and taking the dechlorinated reclaimed water as the dechlorinating medium for dechlorinating the fly ash in the next round.

10. A fly ash dechlorination process according to claim 9,

the second dechlorination agent is a composite dechlorination agent containing calcium elements and aluminum elements; and/or the presence of a gas in the gas,

the addition amount of the secondary dechlorinating agent is 2-5% of the mass of the wastewater.

Technical Field

The invention relates to the technical field of environmental engineering, in particular to a fly ash dechlorination method.

Background

The garbage incineration power generation satisfactorily solves the harmlessness and resource utilization of household garbage, but also generates fly ash hazardous waste which is not small in quantity and contains dioxin, heavy metals and water-soluble chlorine salt. Dioxin and heavy metals are treated by a plurality of methods at present, but the excessive chlorine salt contained in the fly ash becomes a pain point for the disposal and utilization of the fly ash. The fly ash with excessive chlorine salt can pollute soil and environment and damage equipment for subsequent disposal and recycling of the fly ash. If the dechlorination of the fly ash is not solved, a plurality of fly ashes can not enter a landfill and a cement kiln for cooperative treatment due to the ultralimit of chlorine salt. The influence of the chloride ions on the structure and the performance of the material reduces the strength and the durability of the material, so that the material cannot be recycled as other materials.

At present, several mainstream modes for treating fly ash do not adopt desalination as a treatment premise, so that incomplete treatment, low treatment efficiency, secondary pollution, reduction of quality of resource products and influence of the resource level of fly ash treatment are caused.

The first method is as follows: medicament chelation and solidification landfill-a large amount of fly ash is buried in a landfill at present, not only occupies a large amount of land, but also heavy metal, dioxin and soluble salt in the fly ash are likely to be transferred to enter landfill leachate after long-time landfill. Especially soluble salts, which cannot be sequestered and solidified by the chelating agent, resulting in the easy leaching of the salts from the fly ash into landfill leachate.

The second method comprises the following steps: melting/sintering building materials-if not desalted beforehand, the flue gas generated during melting/sintering will contain a large amount of alkaline earth metal hydrochloride, and along with a large amount of secondary fly ash, secondary pollution will result. The treatment difficulty is very high, and the chlorine content in the building materials can exceed the standard and can not reach the relevant national standard.

The third method comprises the following steps: cement kiln calcination treatment for preparing cement, namely the cement kiln calcination treatment can treat heavy metal and dioxin in fly ash but cannot treat salt in the fly ash. If the desalting is not carried out in advance, the content of chlorine in the cement kiln is too high, so that the cement kiln is skinned and blocked, the production of normal cement is influenced, and the produced cement is not in accordance with the national standard and cannot be normally used.

At present, the fly ash dechlorination is generally to wash the fly ash by a large amount of water so as to transfer chloride ions and soluble salts in the fly ash into the water, and then the dechlorinated fly ash is obtained by solid-liquid separation, which is commonly called as the fly ash washing dechlorination. This process requires a large amount of water and also produces a large amount of highly chlorine and toxic waste water which needs to be disposed of. In order to reach the discharge standard of the waste water, the waste water needs to be treated, the chloride ions in the waste water need to be removed, and high-chlorine and high-toxicity sludge is generated. This method is not only very costly but also not environmentally friendly.

Disclosure of Invention

In order to solve the problems, the invention provides a method for dechlorinating fly ash, which comprises the following steps: firstly, hydrophilic fly ash aggregates are changed into hydrophobic aggregates by a hydrophobic agent, so that water-soluble chloride ions in fly ash are quickly and fully transferred into water, then a dechlorinating agent is used for complexing chloride ions in a solution, dechlorinated fly ash is obtained after solid-liquid separation, waste water generated by fly ash dechlorination is treated to be changed into dechlorinated water with inorganic precipitates, and the dechlorinating water are recycled for next round of fly ash dechlorination, so that water resources are completely recycled, and fly ash dechlorination without other secondary wastes is avoided.

The technical scheme provided by the invention is as follows: a fly ash dechlorination method, comprising the following steps:

s10: dissolving fly ash in dechlorination medium, and adding hydrophobic agent to obtain first process mixture;

s20: adding a first dechlorinating agent into the first process mixture, and uniformly mixing to obtain a second process mixture;

s30: and carrying out filter pressing treatment on the mixture in the second process to obtain dechlorinated fly ash and wastewater.

In the technical scheme, the fly ash is firstly dissolved in a dechlorination medium, so that the subsequent chemical reaction is facilitated; the dechlorination medium is generally water, which is not specifically limited herein, and may be tap water or primary treated reclaimed water. The hydrophobic agent is added to change hydrophilic fly ash aggregates into hydrophobic aggregates, then the first dechlorinating agent is added, the physical and chemical method is adopted, so that chloride ions in the fly ash are quickly and fully separated out along with water, and the chloride ions in the solution are precipitated, and the dechlorination treatment of the fly ash is realized. Furthermore, dechlorinated fly ash is obtained by a filter pressing method, and the treatment mode can be combined with the actual situation, for example, the dechlorinated fly ash can be directly put into a cement kiln for cooperative treatment, can be solidified to be used as a foundation and roadbed backfill material, and can also be solidified to be used as a non-sintered building material.

In one embodiment, the mass ratio of fly ash to dechlorination medium is (0.8-1.5): 1.

In the above technical scheme, the addition amount of the dechlorination medium is determined according to the original chloride ions in the fly ash, and in principle, the larger the content of the original chloride ions is, the higher the proportion is. The technical scheme provided by the invention is different from a water washing dechlorination method, the principle is that the dechlorination reaction is carried out in a physical and chemical combined mode, the aim of saving water is fulfilled, and the parameters are set.

In one embodiment, the hydrophobizing agent is a silicon based compound and/or the hydrophobizing agent is added in an amount of 0.3-1.7% by mass of the fly ash.

In the above technical solution, the hydrophobic agent acts to change the fly ash into hydrophobic aggregates, so that the fly ash is precipitated from the water, and on the other hand, the soluble chloride ions in the fly ash can be dissolved in the water, so that the soluble chloride ions in the fly ash are removed by adding the hydrophobic agent.

In one embodiment, the silicon-based compound includes: at least one of water glass, quartz sand and silica.

In one specific example, step S20 includes:

s21: adjusting the pH of the first process mixture to 7-7.5;

s22: controlling the temperature of the mixture in the first process to be 40-45 ℃, adding a first dechlorinating agent, and uniformly mixing to obtain a mixture in the second process.

In the technical scheme, the pH value of the mixture in the first process is adjusted to provide good reaction conditions for subsequent dechlorination; on the other hand, the temperature needs to be controlled at 40-45 ℃, and a first dechlorinating agent is added for complexing chloride ions in the solution.

In one embodiment, step S21 is specifically: adding an acidic additive to the first process mixture in an amount of 2-5% by weight of the first process mixture.

In the above technical solution, the solution formed after the fly ash is dissolved in the dechlorination medium is alkaline, so that an acidic additive is required to be added to adjust the pH value of the solution.

In a specific example, the acidic additive is one or more of sulfuric acid, nitric acid, hydrochloric acid.

In the above technical scheme, the acidic additive is selected from sulfuric acid, nitric acid or hydrochloric acid which is stable and can not react with the first process mixture.

In one particular example, the first dechlorinating agent is alumina and hydrogen peroxide.

In the technical scheme, the first dechlorinating agent selects a mixture of alumina and hydrogen peroxide, and dechlorination treatment of the solution is carried out from two aspects of physics and chemistry, on one hand, the alumina is used as a carrier to adsorb chloride ions, and on the other hand, the hydrogen peroxide can carry out irreversible chemical reaction with the chloride ions to form stable ionic bonds or covalent bonds.

In one embodiment, the fly ash dechlorination method further comprises:

s40: adding a second dechlorinating agent into the wastewater, and uniformly mixing to obtain dechlorinated reclaimed water; dechlorinating reclaimed water as a dechlorinating medium for the next round of fly ash dechlorinating.

In the technical scheme, the waste water also contains untreated chloride ions, secondary dechlorination treatment is needed in order to enable the discharge standard to reach the standard, and dechlorination reclaimed water is obtained by adding a second dechlorinating agent. Dechlorination reclaimed water can also be used for the fly ash dechlorination of the next round, so that the cyclic utilization of water resources is realized, and the water consumption of the whole dechlorination system is reduced.

In one embodiment, the second dechlorination agent is a composite dechlorination agent containing calcium element and aluminum element; and/or the addition amount of the secondary dechlorinating agent is 2-5% of the mass of the wastewater.

In the technical scheme, the calcium-aluminum composite dechlorinating agent polymerizes chloride ions into inorganic precipitates which are difficult to dissolve in water to form dechlorinated water containing white precipitates.

After the technical scheme of the invention is adopted, the following technical effects can be achieved:

1. a large amount of water resources are saved, the water-cement ratio is only (0.8-1.5):1, the water consumption is very small, and dechlorination of fly ash is carried out by circularly using dechlorination reclaimed water on the basis, so that the water consumption is further saved.

2. No secondary waste, no matter fly ash or water, is subjected to dechlorination treatment, and the content of the soluble chlorine after treatment meets the relevant standard of the national environmental protection regulations.

3. The hydrophobic agent is adopted to change the hydrophilic fly ash granules into hydrophobic granules, so that chloride ions can be separated out quickly along with free water, and the water consumption is reduced.

Drawings

In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the drawings needed to be used in the description of the embodiments are briefly introduced below, and it is obvious that the drawings in the following description are only some embodiments of the present invention, and it is obvious for those skilled in the art to obtain other drawings based on these drawings without creative efforts.

FIG. 1 is a flow diagram of fly ash dechlorination.

Detailed Description

The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.

The technical scheme provided by the invention aims to thoroughly solve the problem of fly ash dechlorination, and chlorine in the fly ash is not simply transferred into water by a water washing method; the invention provides a technical scheme, which treats chlorine in a solid phase and a liquid phase, and does not produce high-chlorine sludge or high-chlorine wastewater. The specific technical scheme is as follows:

referring to fig. 1, a fly ash dechlorination method includes the following steps:

s10: dissolving fly ash in dechlorination medium, and adding hydrophobic agent to obtain first process mixture;

s20: adding a first dechlorinating agent into the first process mixture, and uniformly mixing to obtain a second process mixture;

s30: and carrying out filter pressing treatment on the mixture in the second process to obtain dechlorinated fly ash and wastewater.

Further, the mass ratio of the fly ash to the dechlorination medium is (0.8-1.5): 1.

Further, the hydrophobic agent is a silicon compound, and/or the addition amount of the hydrophobic agent is 0.3-1.7% of the mass of the fly ash.

Further, the silicon-based compound includes: at least one of water glass, quartz sand and silica.

Further, S20 includes the steps of:

s21: adjusting the pH of the first process mixture to 7-7.5;

s22: controlling the temperature of the mixture in the first process to be 40-45 ℃, adding a first dechlorinating agent, and uniformly mixing to obtain a mixture in the second process.

Further, S21 specifically includes: adding an acidic additive to the first process mixture in an amount of 2-5% by weight of the first process mixture.

Further, the acidic additive is one or more of sulfuric acid, nitric acid and hydrochloric acid.

Further, the first dechlorinating agent is aluminum oxide and hydrogen peroxide.

Further, the fly ash dechlorination method also comprises the following steps:

s40: adding a second dechlorinating agent into the wastewater, and uniformly mixing to obtain dechlorinated reclaimed water; dechlorinating reclaimed water as the dechlorinating medium for the next round of fly ash dechlorinating.

Further, the second dechlorination agent is a composite dechlorination agent containing calcium elements and aluminum elements; and/or the addition amount of the secondary dechlorinating agent is 2-5% of the mass of the wastewater.

The fly ash dechlorination method provided by the invention comprises the steps of dissolving fly ash in a dechlorination medium, adding a hydrophobic agent and a first dechlorination agent to remove chlorine in the fly ash, and then carrying out solid-liquid separation to obtain dechlorinated fly ash and wastewater; finally, dechlorinating the wastewater to obtain dechlorinated reclaimed water which can be used as a dechlorinating medium for the next round of fly ash dechlorinating.

Before the fly ash is dissolved, the chlorine content in the fly ash needs to be detected, because the proportion of the dechlorination medium and the fly ash needs to be adjusted according to original chloride ions in the fly ash, and the aim of saving water is also achieved, the water-ash ratio in the technical scheme provided by the invention is (0.8-1.5):1, and generally, the higher the original chloride ion content is, the higher the water-ash ratio is. In order to facilitate the dissolution of the fly ash and to promote the subsequent reaction, the fly ash can be ground to reduce the particle size; in the specific implementation process, the materials are processed to 120 meshes.

A physicochemical method is adopted, and a hydrophobic agent is used for changing hydrophilic fly ash aggregates into hydrophobic aggregates, so that chloride ions in the fly ash are quickly and fully separated out along with water, and the water consumption is reduced; and then adding a first dechlorinating agent for complexing chloride ions in the solution, and performing filter pressing and solid-liquid separation to obtain dechlorinated fly ash and wastewater. The hydrophobic agent is selected from silicon compounds, more specifically, at least one of water glass, quartz sand and silicon oxide. The first dechlorinating agent is a mixture of alumina and hydrogen peroxide, and the dechlorination treatment of the solution is carried out from the physical and chemical aspects, wherein on one hand, alumina is used as a carrier to adsorb chloride ions, and on the other hand, hydrogen peroxide can carry out irreversible chemical reaction with the chloride ions to form stable ionic bonds or covalent bonds. In order to promote the reaction and provide better reaction conditions, the pH value of the solution is adjusted before the first dechlorinating agent is added, the solution of the fly ash after being dissolved in water is alkaline, so that an acidic additive is required to be added, the pH value is adjusted to be 7-7.5, and the temperature is controlled to be 40-45 ℃. The subsequent disposal of the dechlorinated fly ash obtained by pressure filtration depends on the case, for example: can be directly put into a cement kiln for cooperative treatment, can be solidified to be used as a foundation and roadbed backfill material, and can also be solidified to be used as a sintering-free building material.

And (3) dechlorinating the wastewater obtained by filter pressing for the second time to reach the discharge standard, and adding a second dechlorinating agent into the wastewater to obtain dechlorinated reclaimed water. Dechlorination reclaimed water can also be used for the fly ash dechlorination of the next round, so that the cyclic utilization of water resources is realized, and the water consumption of the whole dechlorination system is reduced. The second dechlorinating agent is a composite dechlorinating agent containing calcium element and aluminum element; chloride ions can be polymerized into inorganic precipitates which are difficult to dissolve in water to form dechlorinated water containing white precipitates; finally reaching the aim of dechlorination.

[ example 1 ]

Dechlorination of fluidized bed incineration fly ash (fly ash with chlorine content of 6-7%).

S10: 100g of the chelated fly ash is detected, and the original chloride ion content is 6.86%.

S20: processing the chelated fly ash into powder with the fineness of 120 meshes, putting the powder into a container, adding 80g of purified water according to the weight ratio of water to ash of 0.8:1.0, adding 0.3g of water glass, and stirring the mixture for 5 minutes by using an electric stirrer at the rotating speed of 450/min to obtain a mixture in the first process.

S30: adding 2g of sulfuric acid into the mixture in the first process, and stirring for 5 minutes by using an electric stirrer at the rotating speed of 450/min; then, 1g of alumina and 0.5g of hydrogen peroxide were added thereto at 42 ℃ and stirred for 5 minutes at a rotation speed of 450/min by an electric stirrer to obtain a second process mixture.

S40: and carrying out filter pressing treatment on the mixture obtained in the second process to obtain 110g of dechlorinated fly ash and 70g of wastewater.

S50: adding 1g of calcium oxide and 1g of aluminum oxide into the wastewater, stirring for 10 minutes by using an electric stirrer at the rotating speed of 450/min to obtain dechlorinated reclaimed water, and entering the next dechlorination circulation.

The salinity of the dechlorinated reclaimed water is 1.18 percent by detecting, and the requirement of the production process for water resource recycling is met.

The dechlorinated fly ash is detected, the salinity is shown to be 1.25%, and the salinity removal rate reaches 81.8%. The salinity ratio of 1.25% is the soluble chloride salt content, and is about 4.37g/kg in terms of chloride ion content. Meets the requirements of the 6.3-c bar of HJ-1134-Busy 2020): the content of soluble chlorine in the treated product of fly ash should be controlled, and the soluble chlorine can be removed by high-temperature process, water washing process, etc., and the content of soluble chlorine in the treated product should not exceed 2%, preferably not higher than 1%.

[ example 2 ]

Dechlorination of the incineration fly ash of the grate furnace (fly ash with chlorine content of 8-12%).

S10: 100g of the chelated fly ash is detected, and the original chloride ion content is 9.6 percent.

S20: processing the chelated fly ash into powder with the fineness of 120 meshes, putting the powder into a container, adding 100g of purified water according to the weight ratio of water to ash of 1.0:1.0, adding 1g of silicon oxide, and stirring the mixture for 5 minutes at the rotating speed of 450/min by using an electric stirrer to obtain a mixture in the first process.

S30: adding 3g of hydrochloric acid into the mixture in the first process, and stirring for 5 minutes by using an electric stirrer at the rotating speed of 450/min; then, 3g of alumina and 1g of hydrogen peroxide were added thereto at 42 ℃ and stirred for 5 minutes at 450/min with an electric stirrer to obtain a second process mixture.

S40: and performing filter pressing treatment on the mixture obtained in the second process to obtain 120g of dechlorinated fly ash and 80g of wastewater.

S50: 1.2g of calcium oxide and 1.2g of aluminum oxide were added to the wastewater, and the mixture was stirred for 10 minutes at a rotation speed of 450/min by an electric stirrer to obtain dechlorinated reclaimed water, which was then subjected to the next dechlorination cycle.

The salinity of the dechlorinated reclaimed water is 1.2 percent by detecting, and the requirement of the production process for water resource recycling is met.

The dechlorinated fly ash is detected, the salinity is shown to be 1.35%, and the salinity removal rate reaches 80%. The salinity ratio of 1.35% is the soluble chloride salt content, which is about 4.71g/kg in terms of chloride ion content. Meets the requirements of the 6.3-c bar of HJ-1134-Busy 2020): the content of soluble chlorine in the treated product of fly ash should be controlled, and the soluble chlorine can be removed by high-temperature process, water washing process, etc., and the content of soluble chlorine in the treated product should not exceed 2%, preferably not higher than 1%.

[ example 3 ]

Dechlorination of the incineration fly ash of the grate furnace (fly ash with 13-17% of chlorine content).

S10: 100g of the chelated fly ash is detected, and the original chloride ion content is 16.6 percent.

S20: processing the chelated fly ash into powder with the fineness of 120 meshes, putting the powder into a container, adding 150g of purified water according to the weight ratio of water to ash of 1.5:1.0, adding 1.7g of a mixture of quartz sand and silicon oxide, and stirring the mixture for 5 minutes at the rotation speed of 450/min by using an electric stirrer to obtain a first process mixture.

S30: adding 5g of nitric acid into the mixture in the first process, and stirring for 5 minutes by using an electric stirrer at the rotating speed of 450/min; then 5g of alumina and 2g of hydrogen peroxide were added at 42 ℃ and stirred for 5 minutes with an electric stirrer at a rotation speed of 450/min to obtain a second process mixture.

S40: and performing filter pressing treatment on the mixture obtained in the second process to obtain 120g of dechlorinated fly ash and 130g of wastewater.

S50: 5g of calcium oxide and 5g of aluminum oxide are added into the wastewater, and the wastewater is stirred for 10 minutes by an electric stirrer at the rotating speed of 450/min to obtain dechlorinated reclaimed water, and then enters the next dechlorination circulation.

The salinity of the dechlorinated reclaimed water is 1.35 percent by detecting, and the requirement of the production process for water resource recycling is met.

The dechlorinated fly ash is detected, the salinity is shown to be 1.85%, and the salinity removal rate reaches 88.9%. The salinity ratio of 1.85% is the soluble chloride salt content, which is about 6.46g/kg in terms of chloride ion content. Meets the requirements of the 6.3-c bar of HJ-1134-Busy 2020): the content of soluble chlorine in the treated product of fly ash should be controlled, and the soluble chlorine can be removed by high-temperature process, water washing process, etc., and the content of soluble chlorine in the treated product should not exceed 2%, preferably not higher than 1%.

[ example 4 ]

Dechlorination of the incineration fly ash of the grate furnace (fly ash with chlorine content of 18-20%).

S10: 100g of the chelated fly ash is detected, and the original chloride ion content is 18.3 percent.

S20: processing the chelated fly ash into powder with the fineness of 120 meshes, putting the powder into a container, adding 150g of purified water according to the weight ratio of water to ash of 1.5:1.0, adding 1.7g of a mixture of quartz sand and silicon oxide, and stirring the mixture for 5 minutes at the rotation speed of 450/min by using an electric stirrer to obtain a first process mixture.

S30: adding 5g of nitric acid into the mixture in the first process, and stirring for 5 minutes by using an electric stirrer at the rotating speed of 450/min; then 5g of alumina and 2g of hydrogen peroxide were added at 42 ℃ and stirred for 5 minutes with an electric stirrer at a rotation speed of 450/min to obtain a second process mixture.

S40: and performing filter pressing treatment on the mixture obtained in the second process to obtain 120g of dechlorinated fly ash and 130g of wastewater.

S50: 5g of calcium oxide and 5g of aluminum oxide are added into the wastewater, and the wastewater is stirred for 10 minutes by an electric stirrer at the rotating speed of 450/min to obtain dechlorinated reclaimed water, and then enters the next dechlorination circulation.

The salinity of the dechlorinated reclaimed water is 1.21 percent by detecting, and the requirement of the production process for water resource recycling is met.

The dechlorinated fly ash is detected, the salinity is shown to be 1.68 percent, and the salinity removal rate reaches 90.8 percent. The salinity ratio of 1.68% is the soluble chloride salt content, which is about 5.87g/kg in terms of chloride ion content. Meets the requirements of the 6.3-c bar of HJ-1134-Busy 2020): the content of soluble chlorine in the treated product of fly ash should be controlled, and the soluble chlorine can be removed by high-temperature process, water washing process, etc., and the content of soluble chlorine in the treated product should not exceed 2%, preferably not higher than 1%.

Finally, it should be noted that: the above examples are only intended to illustrate the technical solution of the present invention, but not to limit it; although the present invention has been described in detail with reference to the foregoing embodiments, it will be understood by those of ordinary skill in the art that: the technical solutions described in the foregoing embodiments may still be modified, or some technical features may be equivalently replaced; and such modifications or substitutions do not depart from the spirit and scope of the corresponding technical solutions of the embodiments of the present invention.