CN205640929U - Waste incineration treatment system - Google Patents

Abstract

The utility model provides a garbage incineration treatment system. The flue gas and fly ash produced by garbage incineration leave the furnace and enter the tail flue, and enter the first-stage dust collector after releasing heat and cooling in the tail flue, and the coarse particles in the flue gas are collected by the first-stage The dust collector is collected and discharged to the ash storage. The flue gas and fine particles leave the primary dust collector and then enter the secondary dust collector. Activated carbon is sprayed into the inlet of the secondary dust collector to absorb dioxins, activated carbon and fly ash in the flue gas. The ash is captured by the secondary dust collector and sent back to the furnace. The dioxins returned to the furnace decompose and lose their toxicity, and the purified flue gas leaves the secondary dust collector for discharge. The utility model overcomes the deficiencies of the prior art. The first-stage dust collector collects the fly ash and discharges it, does not contain dioxins adsorbed by activated carbon, and the content of dioxins in the fly ash is low. Dioxin content, and return the collected dioxin-rich fly ash to the furnace for incineration, so as to avoid the discharge of dioxin adsorbed by activated carbon into the environment.

Description

Waste incineration treatment system

technical field

The utility model relates to the technical field of garbage incineration and pollutant control, in particular to a garbage incineration treatment system.

Background technique

Waste incineration has obvious advantages in terms of reduction, harmlessness and resource utilization, and has been widely used in the European Union and Japan. With the development of urbanization in China, the land for landfill is decreasing day by day, and more and more municipal waste is disposed of by incineration.

Garbage contains organic matter and chlorine, and the flue gas produced by waste incineration contains halogenated compound dioxin, which is a very toxic organic matter and needs to be controlled during the process of waste incineration. According to the formation mechanism and physical and chemical properties of dioxins, China’s “Standards for Pollution Control of Domestic Waste Incineration” (GB18485-2014) proposes that there are four main methods to control the emission of dioxins in the flue gas of waste incineration plants: control source, reduce the generation in the furnace, avoid resynthesis in the low temperature area outside the furnace, and purify the flue gas.

1) Control the source to prevent chlorine-containing waste from entering the incinerator. 2) To reduce the generation in the furnace, adopt the "3T+E" process, that is, the incineration temperature (Temperature) is greater than 850 ° C, the residence time (Time) is greater than 2.0 seconds, the combustion process is full of gas-solid turbulence (Turbulence), and sufficient excess Air volume (Excess air), so that the concentration of O2 in the flue gas is at 6~11%. 3) Reduce the low-temperature resynthesis outside the furnace, and reduce the low-temperature resynthesis of dioxins in the tail flue of the incinerator, especially in the temperature range of 200 ° C to 400 ° C. The main mechanism of low-temperature resynthesis of dioxins outside the furnace is that copper or iron compounds catalyze dioxin precursors (such as benzene, chlorobenzene, phenols, hydrocarbons, etc.) on the surface of fly ash to synthesize dioxins. Britain. The methods often used in engineering to reduce the resynthesis of dioxins outside the furnace include: such as reducing the residence time of flue gas between 200°C and 400°C, improving the incineration process to reduce the precursor substances that generate dioxins, and reducing flying The deposition of ash on the inner surface of the equipment to reduce the catalyst support required for dioxin formation, etc. 4) To improve the flue gas purification efficiency, spray activated carbon powder into the flue gas. The activated carbon has a strong adsorption capacity, which can absorb most of the dioxins in the flue gas to the surface of the activated carbon, and use the dust collector to remove the fly ash and activated carbon. Collect them to prevent dioxins from being discharged into the atmosphere along with the flue gas and causing environmental pollution.

Most of China's urban waste is mixed waste, it is impossible to prevent chlorine-containing waste from entering the waste, and it is difficult to control the generation of dioxins from the source. Through good combustion control, that is, "3T+E" combustion process, the generation in the incinerator can be effectively controlled. When the waste incineration flue gas must pass through the tail flue of the incinerator, the temperature drops from 850°C to below 200°C, and it must pass through the low-temperature re-synthesis temperature region outside the furnace. The precursor substances of dioxins (such as benzene, chlorobenzene, phenols, Hydrocarbons, etc.) synthesize dioxins under the catalysis of some metal compounds in fly ash; in order to reduce the concentration of dioxins in the flue gas emitted by waste incineration, activated carbon is sprayed into the flue gas to effectively absorb the dioxins in the flue gas dioxin, and the activated carbon is collected by the dust collector, which effectively reduces the dioxin content in the purified flue gas, so that the dioxin concentration in the flue gas meets the requirements of environmental protection emissions.

Through the flue gas purification treatment, although the content of dioxins in the flue gas emitted by waste incineration has been greatly reduced, and the flue gas can meet the environmental protection emission requirements, the dioxins generated by waste incineration have not actually been reduced. The concentration of dioxins in the fly ash collected by the dust collector is relatively high, and the fly ash can only be treated as hazardous waste. Not only can it not be recycled, but the fly ash must also be stabilized. Treatment technology Complicated and expensive.

Utility model content

The purpose of this utility model is to provide a garbage incineration treatment system, which overcomes the deficiencies of the prior art and is designed reasonably. The dioxin content of the fly ash is low, and the secondary dust collector greatly reduces the dioxin content of the flue gas, and returns the collected dioxin-rich fly ash to the furnace for incineration to avoid dioxins adsorbed by activated carbon Discharge into the environment, greatly reduce the concentration of dioxins in fly ash produced by waste incineration, and reduce the toxicity of fly ash.

The technical scheme that the utility model adopts is as follows:

A waste incineration treatment system, comprising an incinerator hearth, a primary dust collector and a secondary dust remover, the incinerator hearth is provided with a measuring instrument, and the lower part of the incinerator hearth is respectively connected to a hopper and a discharge hopper of garbage. The slag pipe is connected, the incinerator hearth is connected with the blower through the primary air pipe and the secondary air pipe, the upper outlet of the incinerator hearth is connected with the inlet of the tail flue, and the outlet of the tail flue It is connected with the inlet of the first-stage dust collector, the ash outlet of the first-stage dust collector is connected with the ash storehouse, and the flue gas outlet of the first-stage dust collector is connected with the inlet of the second-stage dust collector. The entrance of the secondary dust collector is provided with an activated carbon spout, and the secondary dust collector is connected with the smoke exhaust pipe, and the ash discharge port of the secondary dust collector is connected with the lower part of the incinerator hearth through the ash return pipe.

Preferably, the primary dust collector is an electrostatic precipitator.

Preferably, the second dust collector is a bag filter.

Preferably, an ash return device is arranged on the ash return pipe.

Preferably, the tail flue is provided with a tail heating surface.

Compared with the prior art, the beneficial effects of the utility model are as follows:

(1) The fly ash produced by waste incineration is the fly ash collected by the primary dust collector, and the dioxin concentration in the fly ash is low. Therefore, the utility model greatly reduces the dioxin content of the fly ash discharged from waste incineration, and has low toxicity.

(2) The total amount of dioxin discharged by the utility model is small. Although the traditional garbage incineration treatment is the same as the utility model in that the dioxins in the flue gas are sprayed into the activated carbon to absorb the dioxins in the flue gas, the treatment of the dioxins adsorbed by the activated carbon is different between the two. In traditional waste incineration, the dioxins adsorbed by activated carbon are not further processed as by-products of waste incineration, and the total amount of dioxins generated by waste incineration is large. However, in the utility model, the dioxin adsorbed by activated carbon is transported to the furnace for high-temperature incineration, and the dioxin decomposes and loses toxicity. The fly ash discharged by the utility model is the fly ash collected by the first-stage dust collector. The fly ash collected here does not contain dioxins adsorbed by activated carbon. Therefore, the amount of dioxins discharged by the utility model is greatly reduced, causing environmental pollution. adverse effects are greatly reduced.

Description of drawings

Fig. 1 is a schematic diagram of the work flow of the utility model;

1. Blower, 2. Primary air duct, 3. Slag discharge pipe, 4. Tail flue, 5. Ash return device, 6. Ash return pipe, 7. Ash storage, 8. Secondary dust collector, 9. Smoke exhaust Pipe, 10. Activated carbon nozzle, 11. Primary dust collector, 12. Tail heating surface, 13. Furnace, 14. Measuring instrument, 15. Feeding hopper, 16. Secondary air duct

detailed description

Referring to the accompanying drawings, a waste incineration treatment system includes an incinerator hearth 13, a primary dust collector 11 and a secondary dust collector 8, the incinerator hearth 13 is provided with a measuring instrument 14, and the incinerator hearth 13 The lower part communicates with the garbage feed hopper 15 and the slagging pipe 3 respectively, the incinerator hearth 13 communicates with the blower 1 through the primary air duct 2 and the secondary air duct 16, and the upper part of the incinerator hearth 13 exits It is connected with the inlet of the tail flue 4, and the outlet of the tail flue 4 is connected with the inlet of the first-stage dust collector 11, and the ash outlet of the first-stage dust collector 11 is connected with the ash storehouse 7, so The flue gas outlet of the first-stage dust collector 11 communicates with the inlet of the second-stage dust collector 8, the inlet of the second-stage dust collector 8 is provided with an activated carbon spout 10, and the second-stage dust collector 8 is connected to the exhaust pipe 9 is connected, and the ash outlet of the secondary dust collector 8 is connected with the lower part of the incinerator hearth 13 through the ash return pipe 6 . The first-stage dust collector 11 is an electrostatic precipitator; the second-stage dust collector 8 is a bag filter; the ash return pipe 6 is provided with an ash return device 5; the tail flue 4 is provided with Tail heating surface 12.

The flue gas and fly ash produced by waste incineration leave the furnace and enter the tail flue. After cooling down in the tail flue, they enter the primary dust collector. The coarse particles in the flue gas are collected by the primary dust collector and discharged to the ash storage. The gas and fine particles enter the secondary dust collector after leaving the primary dust collector, and spray activated carbon at the inlet of the secondary dust collector to absorb dioxins in the flue gas. The activated carbon and fly ash are captured by the secondary dust collector and sent back To the furnace, the dioxin returned to the furnace is decomposed by pyrolysis and loses its toxicity, and the purified flue gas leaves the secondary dust collector for discharge. The utility model adopts two-stage dust removal, the first-stage dust removal collects the fly ash and discharges it, does not contain dioxins adsorbed by activated carbon, and the dioxin content of the fly ash is low, and the second-stage dust collector greatly reduces the dioxins in the flue gas content, and return the collected dioxin-rich fly ash to the furnace for incineration, so as to avoid the emission of dioxins adsorbed by activated carbon into the environment.

Claims (5)

1. null1. a waste incineration processing system，Including incinerator burner hearth、Primary dust removing device and secondary ash collector，Described incinerator burner hearth is provided with measuring instrument，It is characterized in that: described incinerator lower furnace portion is connected with feed hopper and the scum pipe of rubbish respectively，Described incinerator burner hearth is connected with aerator with secondary air channel by primary air piping，Described incinerator upper furnace outlet is connected with the import of back-end ductwork，The outlet of described back-end ductwork is connected with the import of primary dust removing device，The ash discharging hole of described primary dust removing device is connected with Hui Ku，The described exhanst gas outlet of primary dust removing device is connected with the import of secondary ash collector，The import of described secondary ash collector is provided with activated carbon spout，Described secondary ash collector is connected with smoke exhaust pipe，The ash discharging hole of described secondary ash collector is connected by the bottom of gray back pipe with incinerator burner hearth.
2. A kind of waste incineration processing system the most according to claim 1, it is characterised in that: described primary dust removing device is electrostatic precipitator.
3. A kind of waste incineration processing system the most according to claim 1, it is characterised in that: described secondary ash collector is sack cleaner.
4. A kind of waste incineration processing system the most according to claim 1, it is characterised in that: on described gray back pipe, gray back device is set.
5. A kind of waste incineration processing system the most according to claim 1, it is characterised in that: described back-end ductwork is provided with back-end surfaces.