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Fly ash melting vitrification pretreatment system and method

A melting vitrification and pretreatment technology, applied in sustainable waste treatment, solid waste management, climate sustainability, etc., can solve the problems of many irregular sections, poor thermal strength, easy to be extracted, etc., and achieve environmental benefits and Significant economic benefits, improve molding rate and strength, solve the effect of wasting energy

Pending Publication Date: 2022-05-27
SOUND ENVIRONMENTAL RESOURCES
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, the backspray of the leachate concentrate aggravates the corrosion of the furnace, causing related systems to fail to operate normally, and also increases the treatment cost of the flue gas purification system
[0004] Chinese patent application CN110345484A discloses a system for the co-processing of garbage fly ash and leachate. This scheme utilizes the residual heat of fly ash melting to evaporate the leachate concentrate, but this scheme does not carry out molding and compatibility pretreatment on fly ash. After the fly ash enters the melting furnace, it is easy to be drawn out under the action of negative pressure suction, increasing the pressure of the subsequent purification system, and the molten vitrification rate is difficult to meet the requirements
[0005] Chinese patent application CN106217925B discloses a method for pretreatment of waste incineration fly ash before melting. The leachate is directly mixed with the two materials of fly ash and extruded. Electric arc furnace raw materials, but the cold strength, hot strength and vitrification rate of molten products after forming are difficult to meet the requirements of current production standards
[0006] In the existing scheme of pretreatment of waste incineration fly ash before melting, only fly ash and leachate are directly co-processed, and the influence of material strength after molding on subsequent utilization is not fully considered
For example, due to the very weak viscosity of the leachate itself, the columnar electric arc furnace raw material after direct molding has many irregular sections, low strength, and is easy to pulverize, especially the thermal strength is very poor, and the effect is not ideal. At the same time, only extruding Forming the final raw material has the problems of low efficiency and high energy consumption; and the melting of fly ash needs to be carried out according to the requirements of vitrification. Compatibility of raw material components, only simple mixing and molding, can not meet the molten vitrification rate (national standard GB / T41015-2021 "Technical Requirements for Vitrification Treatment Products of Solid Waste" requires vitrification rate ≥ 85%)

Method used

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Embodiment 1

[0086] The present embodiment provides a method for pretreatment of fly ash melting and vitrification, using the pretreatment system of the present invention, comprising the following steps:

[0087] Step 1, use the mixing unit 5 to mix and stir the domestic waste incineration fly ash, leachate concentrate, compounding agent, and binder into a mixture; wherein, the addition of the domestic waste incineration fly ash is 65wt%, The addition amount of the domestic garbage leachate concentrate is 20wt%, the addition amount of the compounding agent is 11wt%, and the addition amount of the binder is 4wt%;

[0088] Step 2, using the molding unit 6 to extrude the mixture obtained in step 1 into an ellipsoidal raw material under an extrusion pressure of 23 MPa;

[0089] In step 3, the ellipsoid-shaped raw material obtained in step 2 is dried at 120° C. by the drying unit 7, and the raw material for high temperature molten vitrification with a moisture content of 8 wt% is obtained after...

Embodiment 2

[0092] The present embodiment provides a fly ash fusion vitrification pretreatment method, using the pretreatment system of the present invention, comprising the following steps:

[0093] Step 1, use the mixing unit 5 to mix and stir the medical waste incineration fly ash, leachate concentrate, compounding agent, binder, etc. in a certain place in Anhui into a mixture; wherein, the addition of the medical waste incineration fly ash is 70wt% , the addition amount of the domestic garbage leachate concentrate is 20wt%, the addition amount of the compounding agent is 7wt%, and the addition amount of the binder is 3wt%;

[0094] Step 2, using the molding unit 6 to extrude the mixture obtained in step 1 into an ellipsoidal raw material under an extrusion pressure of 23 MPa; preferably, the molding unit 6 adopts a high-pressure molding machine;

[0095] In step 3, the ellipsoid-shaped raw material obtained in step 2 is dried by the drying unit 7 to become the raw material for high te...

Embodiment 3

[0098] The present embodiment provides a fly ash fusion vitrification pretreatment method, using the pretreatment system of the present invention, comprising the following steps:

[0099] Step 1, use the mixing unit 5 to mix and stir the hazardous waste incineration fly ash, leachate concentrate, compounding agent, binder, etc. in a certain place in Inner Mongolia into a mixture; wherein, the addition amount of the hazardous waste incineration fly ash is 75wt% , the addition amount of the domestic garbage leachate concentrate is 16wt%, the addition amount of the compounding agent is 5wt%, and the addition amount of the binder is 4wt%;

[0100] Step 2, using the molding unit 6 to extrude the mixture obtained in step 1 into an ellipsoidal raw material under an extrusion pressure of 20 MPa;

[0101] In step 3, drying unit 7 is used to dry the ellipsoid raw material obtained in step 2 at 125° C., and after drying, a raw material for high temperature molten vitrification with a moi...

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Abstract

The invention discloses a fly ash melting vitrification pretreatment system and method, and the system is characterized in that a material mixing unit is provided with a fly ash inlet, a leachate concentrated solution inlet, a binder inlet, a compounding agent inlet and a mixed material outlet, and the material mixing unit is internally provided with a stirrer; the leachate concentrated solution storage unit is provided with a leachate concentrated solution outlet which is connected with the leachate concentrated solution inlet of the material mixing unit; a fly ash outlet of the fly ash storage unit is connected with a fly ash inlet of the mixing unit; a compound agent outlet of the compound agent storage unit is connected with a compound agent inlet of the mixing unit; a binder outlet of the binder storage unit is connected with a binder inlet of the mixing unit; the forming unit is provided with a mixed material inlet and a formed material outlet, and the mixed material inlet is connected with the mixed material outlet of the mixing unit; the drying unit is provided with a formed material inlet and a dried formed material outlet, and the formed material inlet is connected with the formed material outlet of the forming unit. According to the system and the method, fly ash molded products meeting requirements can be prepared.

Description

technical field [0001] The invention relates to the field of garbage disposal, in particular to a system and method for pretreatment of fly ash melting and vitrification. Background technique [0002] Waste incineration, medical waste incineration and hazardous waste incineration have shown a good momentum of development in my country. Due to the thorough innocence of incineration and a high degree of reduction, it is considered to be an important direction for urban waste treatment in my country. Waste incineration will produce a large amount of fly ash, which is the powdery particulate matter collected after the waste incineration flue gas is purified by the bag filter. It is an inevitable product of waste incineration, accounting for about 3% to 5% of the total waste incineration. The components are oxides and calcium salts containing Si, Ca, Al, Fe, etc., and also contain a large amount of heavy metals adsorbed by activated carbon and highly toxic organic compounds such ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C03C1/02C03C6/02C03C6/04
CPCC03C1/002C03C1/02Y02W30/91
Inventor 许修强车慧吴朝锋
Owner SOUND ENVIRONMENTAL RESOURCES
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