CN210495683U - Waste incineration tail gas integration deacidification device - Google Patents

Waste incineration tail gas integration deacidification device Download PDF

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Publication number
CN210495683U
CN210495683U CN201921391865.XU CN201921391865U CN210495683U CN 210495683 U CN210495683 U CN 210495683U CN 201921391865 U CN201921391865 U CN 201921391865U CN 210495683 U CN210495683 U CN 210495683U
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China
Prior art keywords
waste incineration
tail gas
reaction unit
reaction
incineration tail
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CN201921391865.XU
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Chinese (zh)
Inventor
严圣军
陆樑
戴伍华
祁竞锋
肖厚祥
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Haian Tianying Environmental Protection Energy Co ltd
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Haian Tianying Environmental Protection Energy Co ltd
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Abstract

The utility model discloses a waste incineration tail gas integration deacidification device, the device includes cooling device, dust collector and reaction unit, cooling device upper end opening and dust collector entrance fixed connection, dust collector export and reaction unit entry linkage, reaction unit is semi-circular structure, the reaction unit export sets up in the side, the reaction unit side still is provided with one and washes the mouth. The utility model has the advantages of the design that adopts the integration can effectively carry out the deacidification with the flue gas and handle, and area is little, practices thrift the cost, washs more easily.

Description

Waste incineration tail gas integration deacidification device
Technical Field
The utility model relates to a flue gas deacidification equipment, in particular to waste incineration tail gas integration deacidification device.
Background
Waste incineration is a waste treatment method which has been vigorously developed in China in recent years. Due to the restriction of the components of the garbage, after the garbage is treated by an incineration process, the generated flue gas contains a certain amount of acid gases, such as HCl, SO2, HF, NOx and the like. Flue gas treatment processes commonly adopted in the construction of domestic waste incineration treatment projects include semi-dry deacidification, dry deacidification and wet deacidification, wherein the semi-dry deacidification and the dry deacidification are most commonly applied in the domestic waste incineration treatment projects.
The semidry deacidification method generally adopts calcium oxide (CaO) or calcium hydroxide (Ca (OH) 2) as a raw material to prepare a calcium hydroxide solution. And spraying the calcium hydroxide solution into the reactor by using a nozzle or a rotary sprayer to form liquid drops with extremely small particle size, and reacting with the acid gas. The water is completely evaporated in the reaction process, so no waste water is generated.
However, the removal rate of the deacidification device in the process is not broken through, the research and development speed is almost not before stagnation, the device is complex, the reaction control difficulty is high, and the cleaning difficulty of the device is also high.
SUMMERY OF THE UTILITY MODEL
The utility model aims at providing a waste incineration tail gas integration deacidification device.
The above technical purpose of the present invention can be achieved by the following technical solutions:
the utility model provides a waste incineration tail gas integration deacidification device, a serial communication port, the device includes cooling device, dust collector and reaction unit, cooling device upper end opening and dust collector entrance fixed connection, the dust collector export and reaction unit entry linkage, reaction unit is semi-circular structure, the reaction unit export sets up in the side, the reaction unit side still is provided with one and washes the mouth.
Preferably, the cooling device comprises a plurality of spraying devices and spraying devices.
Preferably, the spraying device is arranged at the lower end of the cooling device, and the spraying device is arranged at the upper end of the cooling device.
Preferably, the dust removal device is of a cylindrical structure, and a plurality of ultrasonic generators are arranged on the side wall of the dust removal device.
Preferably, a plurality of rotary spraying devices are arranged at the top of the reaction device.
Preferably, a circular baffle is fixedly installed at the inlet of the reaction device, and the radius of the central opening of the circular baffle is smaller than that of the inlet of the reaction device.
Preferably, the included angle between the flushing port and the plane of the top end of the reaction device is 25-30 degrees.
To sum up, the utility model discloses following beneficial effect has:
1. the utility model discloses simple structure adopts the integrated design, reduces the area of whole system, optimal design scheme.
2. The utility model discloses add ultrasonic dust collector, both can be arranged in detaching the flue gas fine impurity granule, also can detach the most steam in the last step.
3. The utility model discloses set up ring baffle in the reaction unit entrance, can be with handling the rubbish temporary storage, later recycle washes the mouth and washes it.
Drawings
Fig. 1 is a schematic structural diagram of the present invention.
Detailed Description
The following description will be further described with reference to the accompanying drawings, which are not intended to limit the present invention.
As shown in fig. 1, an integrated deacidification device for waste incineration tail gas comprises a cooling device 1, a dust removal device 2 and a reaction device 3 from bottom to top, wherein flue gas enters from the lower end of the cooling device 1, an opening at the upper end of the cooling device 1 is fixedly connected with an inlet of the dust removal device 2, an outlet of the dust removal device 2 is connected with an inlet of the reaction device 3, the cooling device 1 comprises a plurality of spraying devices 4 and spraying devices 5, the spraying devices 4 are installed on the lower layer of the cooling device 1, the spraying devices 5 are installed on the upper layer of the cooling device 1, flue gas enters from the inlet of the lower end of the cooling device 1, is firstly primarily cooled after contacting with the spraying devices 4, is subsequently cooled through the spraying devices 5, and removes and filters visible impurities in the flue gas.
Dust collector 2 is cylindrical structure, is provided with several supersonic generator 6 at 2 lateral walls of dust collector, the flue gas contains a large amount of steam behind atomizer 5, through carrying out ultrasonic treatment to the flue gas, can reduce the steam that the flue gas brought into, influences reaction going on next step, also can reduce partial flue gas impurity simultaneously.
The reaction device 3 is of an inverted semicircular structure, the outlet 7 of the reaction device is arranged on the side edge, a circular baffle 9 is fixedly arranged at the inlet of the reaction device 3, and an included angle is formed between the circular baffle 9 and the horizontal plane, so that the radius of the central opening of the circular baffle 9 is smaller than that of the inlet of the reaction device 3.
The top of the reaction device 3 is provided with a plurality of rotary spraying devices 8, the prepared calcium hydroxide solution is sprayed into the reaction device 3, the calcium hydroxide solution forms liquid drops with extremely small particle size through the rotary spraying devices 8 so as to react with acidic substances in flue gas, waste generated by reaction is temporarily stored between the annular baffle 9 and the reaction device 3, and the generated waste can be prevented from entering the dust removal device 2 and the cooling device 1.
The side of the reaction device is also provided with a flushing port 10, the included angle between the flushing port 10 and the plane at the top end of the reaction device 3 is 25-30 degrees, after the flue gas treatment is completed, the inside of the reaction device 3 is flushed through the flushing port 10, the bottom of the reaction device 3 is provided with a drain outlet 11, and a valve is arranged at the drain outlet 11 and is opened during flushing.
The above description is only a preferred embodiment of the present invention, and is not intended to limit the present invention, and those skilled in the art can make various modifications or equivalent substitutions within the spirit and scope of the present invention, and such modifications or equivalent substitutions should also be considered as falling within the scope of the present invention.

Claims (7)

1. The utility model provides a waste incineration tail gas integration deacidification device, a serial communication port, the device includes cooling device, dust collector and reaction unit, cooling device upper end opening and dust collector entrance fixed connection, the dust collector export and reaction unit entry linkage, reaction unit is semi-circular structure, the reaction unit export sets up in the side, the reaction unit side still is provided with one and washes the mouth.
2. The integrated deacidification device for waste incineration tail gas according to claim 1, characterized in that: the cooling device comprises a plurality of spraying devices and spraying devices.
3. The integrated deacidification device for waste incineration tail gas as claimed in claim 2, characterized in that: the spraying device is arranged at the lower end of the cooling device, and the spraying device is arranged at the upper end of the cooling device.
4. The integrated deacidification device for waste incineration tail gas according to claim 1, characterized in that: the dust removal device is of a cylindrical structure, and a plurality of ultrasonic generators are arranged on the side wall of the dust removal device.
5. The integrated deacidification device for waste incineration tail gas according to claim 1, characterized in that: and a plurality of rotary spraying devices are arranged at the top of the reaction device.
6. The integrated deacidification device for waste incineration tail gas according to claim 1, characterized in that: the inlet of the reaction device is fixedly provided with a circular baffle, and the radius of the central opening of the circular baffle is smaller than that of the inlet of the reaction device.
7. The integrated deacidification device for waste incineration tail gas according to claim 1, characterized in that: the included angle between the flushing port and the plane of the top end of the reaction device is 25-30 degrees.
CN201921391865.XU 2019-08-26 2019-08-26 Waste incineration tail gas integration deacidification device Active CN210495683U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201921391865.XU CN210495683U (en) 2019-08-26 2019-08-26 Waste incineration tail gas integration deacidification device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201921391865.XU CN210495683U (en) 2019-08-26 2019-08-26 Waste incineration tail gas integration deacidification device

Publications (1)

Publication Number Publication Date
CN210495683U true CN210495683U (en) 2020-05-12

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201921391865.XU Active CN210495683U (en) 2019-08-26 2019-08-26 Waste incineration tail gas integration deacidification device

Country Status (1)

Country Link
CN (1) CN210495683U (en)

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