Fuel-free energy circulation type garbage disposal equipment

文档序号:1858515 发布日期:2021-11-19 浏览:34次 中文

阅读说明:本技术 一种无燃料能源循环型垃圾处理设备 (Fuel-free energy circulation type garbage disposal equipment ) 是由 吴书文 泽井正和 施明辉 黄蒙安 张博 于 2021-09-24 设计创作,主要内容包括:本发明提出了一种无燃料能源循环型垃圾处理设备,包括反应炉,所述的反应炉的上方设有投放舱,投放舱的下端设有与反应炉的内部连通的落料口,所述的反应炉的下方设有与其内部连通的出灰机构,还包括二次燃烧装置、排气装置、送风装置、磁化装置,反应炉通过管道与二次燃烧装置连通,送风装置通过管道分别与反应炉和二次燃烧装置连通,二次燃烧装置通过管道与排气装置连通,连通送风装置和反应炉的管道从磁化装置形成的磁场中穿过。(The invention provides a fuel-free energy circulation type garbage treatment device, which comprises a reaction furnace, wherein a feeding cabin is arranged above the reaction furnace, a blanking port communicated with the interior of the reaction furnace is arranged at the lower end of the feeding cabin, an ash discharging mechanism communicated with the interior of the reaction furnace is arranged below the reaction furnace, the fuel-free energy circulation type garbage treatment device also comprises a secondary combustion device, an exhaust device, an air supply device and a magnetization device, the reaction furnace is communicated with the secondary combustion device through a pipeline, the air supply device is respectively communicated with the reaction furnace and the secondary combustion device through pipelines, the secondary combustion device is communicated with the exhaust device through a pipeline, and the pipeline communicated with the air supply device and the reaction furnace penetrates through a magnetic field formed by the magnetization device.)

1. A fuel-free energy circulation type garbage disposal device is characterized in that: including the reacting furnace, the top of reacting furnace be equipped with and put in the cabin, the lower extreme of putting in the cabin be equipped with the blanking mouth of the inside intercommunication of reacting furnace, the below of reacting furnace be equipped with rather than the ash hoist of inside intercommunication, still include secondary combustion device, exhaust apparatus, air supply arrangement, magnetization unit, the reacting furnace passes through pipeline and secondary combustion device intercommunication, air supply arrangement passes through the pipeline respectively with reacting furnace and secondary combustion device intercommunication, secondary combustion device passes through pipeline and exhaust apparatus intercommunication, the pipeline of intercommunication air supply arrangement and reacting furnace passes from the magnetic field that magnetization unit formed.

2. The fuel-free energy recycling type garbage disposal apparatus according to claim 1, wherein: the secondary combustion device comprises a combustion pipe, wherein one end of the combustion pipe is a flue gas inlet, the other end of the combustion pipe is a flue gas outlet, the flue gas inlet is communicated with the reaction furnace, the flue gas outlet is communicated with the exhaust device, the secondary combustion device also comprises an air inlet pipe, one end of the air inlet pipe is communicated with the air supply device, and the other end of the air inlet pipe is communicated with the combustion pipe.

3. The fuel-free energy recycling type garbage disposal apparatus according to claim 2, wherein: the other end of air-supply line set up for sealing, be equipped with on the lateral wall of air-supply line rather than the branch tuber pipe of inside intercommunication, divide the tuber pipe to be connected with the lateral wall of burning tube and communicate with the inside of burning tube, branch tuber pipe be equipped with a plurality ofly, a plurality ofly divide the tuber pipe to be connected with the different positions of the extending direction of burning tube respectively.

4. The fuel-free energy recycling type garbage disposal apparatus according to claim 3, wherein: the number of the air inlet pipes is two.

5. The fuel-free energy recycling type garbage disposal apparatus according to claim 2, wherein: the combustion tube is arranged in a bent and coiled manner.

6. The fuel-free energy recycling type garbage disposal apparatus according to claim 2, wherein: the center of reacting furnace be equipped with rotatable rotation axis, rotatory lower extreme sets up the bottom of reacting furnace, the lower extreme of rotation axis is connected with the level and sets up the puddler, the upper end of rotation axis extends the upside of input cabin, is connected with the stirring leaf on the rotation axis, the stirring leaf be located input under-deck, rotation axis and puddler in form the air flue of mutual intercommunication, the puddler on be equipped with the venthole, the air flue run through the upper end setting of rotation axis, the upper end and the air supply arrangement intercommunication setting of rotation axis.

Technical Field

The invention relates to the technical field of garbage disposal equipment, in particular to fuel-free energy circulation type garbage disposal equipment.

Background

The dry distillation treatment of the garbage is to treat the garbage by a reaction furnace, and the garbage after the dry distillation treatment generates various gases, steam and solid residues. When the garbage incinerator works, moisture brought into the garbage can be generated when external garbage is poured into the reaction furnace, steam is generated when the external garbage is poured into the reaction furnace, the generated waste gas is insufficient in combustion reaction, environmental pollution is easily caused by direct discharge, and certain resource waste problem also exists in the working process.

Disclosure of Invention

In view of the problems identified in the background art, the present invention provides a fuel-free energy recycling type garbage disposal apparatus.

The technical scheme of the invention is realized as follows:

the utility model provides a no fuel energy circulation type refuse handling installation, includes the reacting furnace, the top of reacting furnace be equipped with and put in the cabin, the lower extreme of putting in the cabin be equipped with the blanking mouth of the inside intercommunication of reacting furnace, the below of reacting furnace be equipped with rather than the ash discharging mechanism of inside intercommunication, still include secondary combustion device, exhaust apparatus, air supply arrangement, magnetization unit, the reacting furnace passes through pipeline and secondary combustion device intercommunication, air supply arrangement passes through the pipeline respectively with reacting furnace and secondary combustion device intercommunication, secondary combustion device passes through pipeline and exhaust apparatus intercommunication, the pipeline of intercommunication air supply arrangement and reacting furnace passes from the magnetic field that magnetization unit formed.

The secondary combustion device further comprises a combustion pipe, wherein one end of the combustion pipe is a smoke inlet, the other end of the combustion pipe is a smoke outlet, the smoke inlet is communicated with the reaction furnace, the smoke outlet is communicated with the exhaust device, the secondary combustion device further comprises an air inlet pipe, one end of the air inlet pipe is communicated with the air supply device, and the other end of the air inlet pipe is communicated with the combustion pipe.

The invention is further arranged in a way that the other end of the air inlet pipe is arranged in a closed way, the side wall of the air inlet pipe is provided with an air distribution pipe communicated with the inside of the air inlet pipe, the air distribution pipe is connected with the side wall of the combustion pipe and communicated with the inside of the combustion pipe, the air distribution pipe is provided with a plurality of air distribution pipes, and the air distribution pipes are respectively connected with different positions of the extension direction of the combustion pipe.

The invention is further provided that the number of the air inlet pipes is two.

The invention is further provided that the combustion tube is arranged in a curved coiled manner.

The invention is further provided that a rotatable rotating shaft is arranged in the center of the reaction furnace, the lower end of the rotating shaft is arranged at the bottom of the reaction furnace, the lower end of the rotating shaft is connected with a horizontally arranged stirring rod, the upper end of the rotating shaft extends to the upper side of the throwing cabin, the rotating shaft is connected with a stirring blade, the stirring blade is positioned in the throwing cabin, mutually communicated air passages are formed in the rotating shaft and the stirring rod, an air outlet hole is formed in the stirring rod, the air passages penetrate through the upper end of the rotating shaft, and the upper end of the rotating shaft is communicated with an air supply device.

By adopting the technical scheme, the invention has the beneficial effects that:

(1) the dry distillation gas generated by the primary combustion in the reaction furnace enters a secondary combustion device for secondary combustion, so that the combustion is more sufficient, the pollution of discharge is reduced, and the heat generated in the secondary combustion can be used for heating and the like;

(2) the oxygen entering the reaction furnace is magnetized by the magnetizing device, and the magnetized oxygen ions are regularly arranged and enter the reaction furnace, so that the decomposition reaction is favorably and quickly carried out, and the working efficiency of the reaction furnace is improved;

(3) the feeding cabin is arranged at the upper side of the reaction furnace, so that the reaction furnace can heat the feeding cabin, and moisture in the garbage in the feeding cabin is evaporated;

(4) the reaction work in the reaction furnace is carried out at the bottom of the reaction furnace, the thrown new garbage is positioned at the upper side of the garbage subjected to combustion decomposition reaction, so that the upward moving dry distillation gas needs to pass through the new garbage, and the new garbage can filter out impurities such as soot of the dry distillation gas.

Drawings

In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below, and it is obvious that the drawings in the following description are only some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to these drawings without creative efforts.

FIG. 1 is a schematic structural view of the present invention;

FIG. 2 is a first schematic structural diagram of a secondary combustion apparatus according to the present invention;

FIG. 3 is a schematic structural diagram of a secondary combustion apparatus of the present invention.

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 invention is illustrated below with reference to fig. 1-3:

the utility model provides a no fuel energy circulation type refuse handling installation, includes reacting furnace 1, reacting furnace 1's top be equipped with and put in cabin 2, the lower extreme of putting in cabin 2 is equipped with the blanking mouth with reacting furnace 1's inside intercommunication, reacting furnace 1's below be equipped with rather than the ash discharging mechanism 3 of inside intercommunication.

The device also comprises a secondary combustion device 3, an exhaust device 4, an air supply device 5 and a magnetization device 6.

The reaction furnace 1 is communicated with the secondary combustion device 3 through a pipeline, the air supply device 5 is respectively communicated with the reaction furnace 1 and the secondary combustion device 3 through pipelines, the secondary combustion device 3 is communicated with the exhaust device 4 through a pipeline, and the pipeline which is communicated with the air supply device 5 and the reaction furnace 1 penetrates through a magnetic field formed by the magnetizing device 6.

The secondary combustion device 3 comprises a combustion pipe 31, a flue gas inlet 32 is arranged at one end of the combustion pipe 31, a flue gas outlet 33 is arranged at the other end of the combustion pipe 31, the flue gas inlet 32 is communicated with the reaction furnace 1, the flue gas outlet 33 is communicated with the exhaust device 4, the secondary combustion device also comprises an air inlet pipe 34, one end of the air inlet pipe 34 is communicated with the air supply device 5, and the other end of the air inlet pipe 34 is communicated with the combustion pipe 31.

The dry distillation gas entering the secondary combustion device 3 has high temperature and spontaneously combusts after contacting with air.

The other end of the air inlet pipe 34 is sealed, an air distributing pipe 35 communicated with the inside of the air inlet pipe 34 is arranged on the side wall of the air inlet pipe 34, the air distributing pipe 35 is connected with the side wall of the combustion pipe 31 and communicated with the inside of the combustion pipe 31, a plurality of air distributing pipes 35 are arranged, and the plurality of air distributing pipes 35 are respectively connected with different positions of the combustion pipe 31 in the extending direction.

Wherein, the number of the air inlet pipes 34 is two.

Wherein, the combustion tube 31 is arranged in a curved and coiled shape.

Wherein, the center of reacting furnace 1 be equipped with rotatable rotation axis 7, rotatory lower extreme sets up the bottom of reacting furnace 1, the lower extreme of rotation axis 7 is connected with the level and sets up puddler 8, the upper end of rotation axis 7 extends the upside of input cabin 2, is connected with the stirring leaf on the rotation axis 7, the stirring leaf be located input cabin 2 in, rotation axis 7 and puddler 8 in form the air flue of mutual intercommunication, puddler 8 on be equipped with the venthole, the air flue run through the upper end setting of rotation axis 7, the upper end and the 5 intercommunication settings of air supply arrangement of rotation axis 7.

By adopting the technical scheme, the invention has the beneficial effects that:

(5) the dry distillation gas generated by the primary combustion in the reaction furnace 1 enters the secondary combustion device 3 for secondary combustion, so that the combustion is more sufficient, the emission pollution is reduced, and the heat generated in the secondary combustion can be used for heating and the like;

(6) the oxygen entering the reaction furnace 1 is magnetized by the magnetizing device 6, and the magnetized oxygen ions are regularly arranged and enter the reaction furnace 1, so that the decomposition reaction is rapidly carried out, and the working efficiency of the reaction furnace 1 is improved;

(7) the feeding cabin 2 is arranged at the upper side of the reaction furnace 1, so that the reaction furnace 1 can heat the feeding cabin 2, and water in the garbage in the feeding cabin 2 is evaporated;

the reaction work in the reaction furnace 1 is carried out at the bottom of the reaction furnace 1, the thrown new garbage is positioned at the upper side of the garbage subjected to combustion decomposition reaction, so that the upward moving dry distillation gas needs to pass through the new garbage, and the new garbage can filter out impurities such as soot of the dry distillation gas.

Description of the working process:

flow of garbage (solid matter):

and (4) smashing the wet garbage and the screened combustible garbage, and then putting the smashed wet garbage and the screened combustible garbage into a putting cabin by taking 120L as a unit. The garbage is quantitatively supplied to the reaction furnace by the rotation of the stirring blades in the charging chamber, but the dry distillation gas from the reaction furnace does not flow into the charging chamber.

On the lower surface of the feeding cabin, a part of water of the garbage is evaporated and dried due to heat transferred from the reaction furnace. After the steam is evaporated, the waste is introduced into a reaction furnace. Therefore, the water vapor generated in the drying process of the garbage can be prevented from reacting with the dry distillation gas to generate tar, and the spontaneous combustion reduction combustion can be realized by using the reaction furnace without auxiliary fuel.

The garbage entering the reaction furnace is horizontally dispersed by the stirring rod which is supplied with air once through the stirring rod in the furnace. The stirring rod and the stirring blade rotate coaxially, and can ensure the stable supply and reduction combustion of the garbage in the reaction furnace.

The garbage entering the reaction furnace is dried by the generated 600-800 ℃ dry distillation gas at the upper part and is subjected to partial combustion and thermal decomposition by primary air preheated by the temperature of 300-500 ℃ in the furnace at the lower part to generate dry distillation gas.

The burning ash powder is reduced through reduction and combustion in the reaction furnace, and harmful heavy metals such as hexavalent chromium and the like are reduced into trivalent chromium and discharged through an ash discharging mechanism.

Gas flow:

the primary air supplied to the reaction furnace is preheated to 300-500 deg.C by the combustion heat in the furnace and the residual heat of ash powder, and in the reducing environment, it makes partial combustion and thermal decomposition reaction with the dry garbage in the furnace to become the dry distillation gas with 600-800 deg.C.

When the reducing gas (H2O, CO2, N2, CO, H2, CH4, etc., and not O2) generated in the reaction furnace passes through the garbage dried layer in the furnace, the entrained ash is removed, and the concentration of coal dust in the dry distillation gas is reduced.

The retort gas is sucked out from the furnace top by an exhaust gas suction device to reduce the pressure in the furnace, and then introduced into a secondary combustion device. In the secondary combustion apparatus, the secondary air and the combustible gas in the dry distillation gas are all combusted, and the generation of odor, CO, dioxin, and the like is suppressed.

Since the secondary combustion apparatus generates harmful components such as NOx when it burns at a high temperature of 900 ℃ or higher, it is necessary to cool the outer wall of the secondary combustion apparatus with air and appropriately control the combustion temperature. The hot air generated at this time can be used for heating houses in winter.

The completely combusted waste gas is exhausted from the chimney through the air suction device by utilizing the Venturi effect, and because the waste gas from the chimney has the characteristics of low self temperature, low concentration of harmful components and the like, and the phenomenon of white frost generated when the exhaust port of the chimney exhausts is avoided, the gas which is more fully combusted in the secondary combustion chamber can be exhausted into the air in a negative pressure rapid cooling state by utilizing the Venturi effect.

The above description is only for the purpose of illustrating the preferred embodiments of the present invention and is not to be construed as limiting the invention, and any modifications, equivalents, improvements and the like that fall within the spirit and principle of the present invention are intended to be included therein.

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