CN214468633U

CN214468633U - Filtering device of garbage disposal system

Info

Publication number: CN214468633U
Application number: CN202120304996.0U
Authority: CN
Inventors: 付玲玲
Original assignee: Individual
Current assignee: Individual
Priority date: 2021-02-03
Filing date: 2021-02-03
Publication date: 2021-10-22
Anticipated expiration: 2031-02-03

Abstract

The utility model discloses a filtering device of a garbage disposal system, which comprises a feeding device, a pyrolysis furnace, a heat exchanger, a dry deacidification tower, a bag-type dust remover, a high-pressure plasma dust remover, a draught fan, a chimney, a cooling device, a slag extractor and a burner, wherein an exhaust port of the pyrolysis furnace is connected with the input end of the heat exchanger through a pipeline, the output end of the heat exchanger is connected with a three-way pipeline, the first output end of the three-way pipeline is connected with the first input end of the dry deacidification tower, the second output end of the three-way pipeline is connected with the input end of the bag-type dust remover through a pipeline, the output end of the bag-type dust remover is connected with the second input end of the dry deacidification tower, the output end of the dry deacidification tower is connected with the high-pressure plasma dust remover, the output end of the high-pressure plasma dust remover is connected with the chimney through the draught fan, and the three-way pipeline is provided with a valve, the utility model can switch the valve in the three-way pipeline, the flue gas from the heat exchanger can be directly dedusted by the high-pressure plasma deduster from the deacidification tower, so that the bag deduster is not damaged by water vapor.

Description

Filtering device of garbage disposal system

Technical Field

The utility model relates to a refuse treatment technical field, concretely relates to refuse treatment system's filter equipment.

Background

Domestic refuse treatment all burns rubbish today, and refuse incineration all adopts the refuse treatment system to burn and gas cleaning handles, and the gas cleaning who has now in refuse treatment system all adopts the sack cleaner, and well-known, the sack cleaner is a dry-type dust filter, can not filter steam more, and too big or the steam is more when the rubbish humidity of handling, just causes the sack cleaner to damage easily, has increased use cost.

SUMMERY OF THE UTILITY MODEL

In order to overcome the above-mentioned weak point that exists among the prior art, the utility model aims to provide a refuse treatment system's filter equipment.

The utility model discloses a following technical scheme realizes: the filtering device of the garbage treatment system comprises a feeding device, a pyrolysis furnace, a heat exchanger, a dry deacidification tower, a bag-type dust remover, a high-pressure plasma dust remover, a draught fan, a chimney, a cooling device, a slag extractor and a burner, wherein the slag extractor is arranged at the lower end of the pyrolysis furnace, the slag extractor is provided with a slag extractor port, one side of the pyrolysis furnace is also provided with an exhaust port, the exhaust port is connected with the input end of the heat exchanger through a pipeline, the output end of the heat exchanger is connected with a three-way pipeline, the three-way pipeline is provided with a first input end, a first output end and a second output end, the first output end of the three-way pipeline is connected with the first input end of the dry deacidification tower, the second output end of the three-way pipeline is connected with the input end of the bag-type dust remover, the output end of the dry deacidification tower is connected with the high-pressure plasma dust remover, the output end of the high-pressure plasma dust remover is connected with the chimney through the induced draft fan, and the three-way pipeline is provided with a valve for communicating or closing the first output end and the second output end of the three-way pipeline.

Compared with the prior art, the utility model, following advantage and beneficial effect have: the utility model discloses increased high-pressure plasma dust remover in the system, when the more rubbish of wet or steam is handled to needs, can switch over the valve in the tee bend pipeline, the flue gas that makes heat exchanger come out does not pass through the sack cleaner, directly removes dust through high-pressure plasma dust remover from deacidifying the tower to can not make steam damage the sack cleaner.

Drawings

Other features, objects and advantages of the invention will become more apparent upon reading of the detailed description of non-limiting embodiments with reference to the following drawings:

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

FIG. 2 is a schematic top view of the structure of FIG. 1;

wherein: the device comprises a feeding device, a pyrolysis furnace, a heat exchanger, a dry deacidification tower, a bag-type dust remover, a draught fan, a chimney, a cooling device, a slag extractor, a combustor, an exhaust port, a tee pipeline, a combustor, a gas exhaust port, a tee pipeline, a high-pressure plasma dust remover and a valve, wherein the feeding device comprises 1 part, the pyrolysis furnace comprises 2 parts, the heat exchanger comprises 3 parts, the dry deacidification tower comprises 4 parts, the bag-type dust remover comprises 5 parts, the draught fan comprises 6 parts, the chimney comprises 7 parts, the cooling device comprises 8 parts, the slag extractor comprises 9 parts, the combustor comprises 11 parts, the exhaust port comprises 12 parts, the tee pipeline comprises 13 parts, a first input end, a first output end, a second output end, a high-pressure plasma dust remover and a valve 17 part.

Detailed Description

Reference will now be made in detail to embodiments of the present invention, examples of which are illustrated in the accompanying drawings, wherein like reference numerals refer to the same or similar elements or elements having the same or similar function throughout. The embodiments described below with reference to the drawings are exemplary only for the purpose of explaining the present invention, and should not be construed as limiting the present invention.

In the description of the present invention, it is to be understood that the terms "center", "longitudinal", "lateral", "up", "down", "front", "back", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", and the like, indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, and are used merely for convenience of description and for simplicity of description, and do not indicate or imply that the device or element being referred to must have a particular orientation, be constructed and operated in a particular orientation, and therefore, should not be construed as limiting the present invention. In the description of the present invention, "a plurality" means two or more unless otherwise specified.

In the description of the present invention, it is to be noted that, unless otherwise explicitly specified or limited, the terms "mounted," "connected," and "connected" are to be construed broadly, and may be, for example, fixedly connected, detachably connected, or integrally connected; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meaning of the above terms in the present invention can be understood in specific cases to those skilled in the art.

The filtering device of the garbage disposal system of the embodiment, as shown in fig. 1 to fig. 2, comprises a feeding device 1, a pyrolysis furnace 2, a heat exchanger 3, a dry deacidification tower 4, a bag-type dust remover 5, a high-pressure plasma dust remover 16, an induced draft fan 6, a chimney 7, a cooling device 8, a slag extractor 9 and a burner 10, wherein the slag extractor 10 is installed at the lower end of the pyrolysis furnace 2, the slag extractor 10 is provided with a slag discharge port, one side of the pyrolysis furnace 2 is also provided with an exhaust port 11, the exhaust port 11 is connected with the input end of the heat exchanger 3 through a pipeline, the output end of the heat exchanger 3 is connected with a three-way pipeline 12, the three-way pipeline 12 is provided with a first input end 13, a first output end 14 and a second output end 15, the first output end 14 of the three-way pipeline is connected with the first input end of the dry deacidification tower 4, the second output end 15 of the three-way pipeline is connected with the input end of the bag-type dust remover 6 through a pipeline, the output end of a bag-type dust collector 6 is connected with the second input end of a dry-type deacidification tower 4, the output end of the dry-type deacidification tower 4 is connected with a high-pressure plasma dust collector 16, the output end of the high-pressure plasma dust collector 16 is connected with a chimney 7 through an induced draft fan 6, a valve 17 for communicating or closing a first output end 14 and a second output end 15 of a three-way pipeline is arranged on the three-way pipeline 12, when wet or more water vapor garbage needs to be treated, the valve 17 in the three-way pipeline can be switched, smoke coming out of a heat exchanger 3 does not pass through the bag-type dust collector, and dust is directly removed from the deacidification tower 4 through the high-pressure plasma dust collector, so that the bag-type dust collector cannot be damaged by water vapor.

While embodiments of the present invention have been shown and described, it will be understood by those of ordinary skill in the art that: various changes, modifications, substitutions and alterations can be made to the embodiments without departing from the principles and spirit of the invention, the scope of which is defined by the claims and their equivalents.

Claims

1. The filter equipment of the refuse disposal system is characterized in that: the device comprises a feeding device, a pyrolysis furnace, a heat exchanger, a dry deacidification tower, a bag-type dust remover, a high-pressure plasma dust remover, an induced draft fan, a chimney, a cooling device, a slag extractor and a burner, wherein the slag extractor is arranged at the lower end of the pyrolysis furnace, the slag extractor is provided with a slag extractor opening, one side of the pyrolysis furnace is also provided with an exhaust opening, the exhaust opening is connected with the input end of the heat exchanger through a pipeline, the output end of the heat exchanger is connected with a three-way pipeline, the three-way pipeline is provided with a first input end, a first output end and a second output end, the first output end of the three-way pipeline is connected with the first input end of the dry deacidification tower, the second output end of the three-way pipeline is connected with the input end of the bag-type dust remover through a pipeline, the output end of the bag-type dust remover is connected with the second input end of the dry deacidification tower, the output end of the dry deacidification tower is connected with the high-pressure plasma dust remover, the output end of the high-pressure plasma dust remover is connected with the chimney through the induced draft fan, and a valve for communicating or closing the first output end and the second output end of the three-way pipeline is arranged on the three-way pipeline.