CN221192076U - Carbonization equipment for biomass garbage treatment - Google Patents
Carbonization equipment for biomass garbage treatment Download PDFInfo
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- CN221192076U CN221192076U CN202323141381.9U CN202323141381U CN221192076U CN 221192076 U CN221192076 U CN 221192076U CN 202323141381 U CN202323141381 U CN 202323141381U CN 221192076 U CN221192076 U CN 221192076U
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- Prior art keywords
- layer
- carbonization
- flue gas
- cooling
- drying
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- 238000003763 carbonization Methods 0.000 title claims abstract description 67
- 239000002028 Biomass Substances 0.000 title claims abstract description 32
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 55
- 239000003546 flue gas Substances 0.000 claims abstract description 55
- 238000001035 drying Methods 0.000 claims abstract description 43
- 238000001816 cooling Methods 0.000 claims abstract description 28
- 239000007789 gas Substances 0.000 claims abstract description 25
- 238000002485 combustion reaction Methods 0.000 claims abstract description 22
- 239000000498 cooling water Substances 0.000 claims abstract description 12
- 238000003756 stirring Methods 0.000 claims description 24
- 239000002912 waste gas Substances 0.000 claims description 6
- 238000004321 preservation Methods 0.000 claims description 4
- 239000005539 carbonized material Substances 0.000 abstract description 4
- 239000000463 material Substances 0.000 abstract description 4
- 239000010410 layer Substances 0.000 description 101
- 238000012545 processing Methods 0.000 description 9
- 238000005265 energy consumption Methods 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- 239000002154 agricultural waste Substances 0.000 description 3
- 239000011229 interlayer Substances 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 238000012271 agricultural production Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 230000017525 heat dissipation Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000009413 insulation Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000010000 carbonizing Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 244000144972 livestock Species 0.000 description 1
- 239000010871 livestock manure Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 238000009304 pastoral farming Methods 0.000 description 1
- 238000009374 poultry farming Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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- Processing Of Solid Wastes (AREA)
Abstract
The utility model discloses carbonization equipment for biomass garbage treatment, which relates to the technical field of garbage treatment, wherein biomass garbage enters a drying layer through a feed inlet, a heat source in the drying layer adopts heat of combustion flue gas, and the dried gas is discharged through an air outlet pipe; the dried biomass garbage enters a carbonization layer, a heat source in the carbonization layer adopts the heat of burning flue gas, and carbonized gas is discharged into an incinerator again through an exhaust pipe to remove harmful gas; and the carbonized material enters a cooling layer, and cooling water cools the material and then is discharged out of the equipment. The utility model is effectively combined with the incinerator, effectively utilizes the heat generated by the incinerator, and simultaneously removes the harmful gas generated by the carbonization layer through the incinerator.
Description
Technical Field
The utility model relates to the technical field of garbage treatment, in particular to carbonization equipment for biomass garbage treatment.
Background
Agricultural waste is a general term for waste discharged from agricultural production, agricultural product processing, livestock and poultry farming and rural residents. The agricultural waste is also called agricultural waste, and comprises two types of plant fibrous waste and livestock manure according to the components, is the difference between the input and output substances and energy of resources in the agricultural production and reproduction chain links, and is the energy loss share of the substances output in the resource utilization.
In garbage treatment, organic materials can be carbonized into coal through a carbonization system for recycling. The carbonization system generally connects a plurality of treatment containers in a horizontal connection mode, then pushes garbage to be treated into the treatment containers, evaporates water in the garbage to be treated in a heating mode, dries, and then performs carbonization and cooling. However, this horizontal connection facilitates control of the deformation of the treatment vessel in its axial direction during operation, but it results in a large floor area for the treatment layer, resulting in high land costs. In addition, the heating units are arranged independently in the drying, drying and carbonizing treatment containers, so that the energy utilization rate is low, and the heat energy loss is high.
The utility model discloses a garbage carbonization system heat utilization device, publication No. CN206033674U, publication day 2017.03.22's chinese patent discloses a garbage carbonization system heat utilization device, and it includes five along the processing layer of vertical direction range upon range of distribution, every processing layer disposes the support frame, the feed inlet has been arranged to the one end upside of processing layer, and the discharge gate has been arranged to the other end downside of processing layer, and the feed inlet of the processing layer that is located the top is relative with the discharge gate of the processing layer that is located its below, install the inlet pipe on the feed inlet, install the discharging pipe on the discharge gate, be located the inlet pipe and the discharging pipe in two adjacent processing layers between install the connecting pipe, five processing layer is from last drying layer, carbonization layer and the cooling layer down in proper order, install the heater in the carbonization layer, carbonization layer inner space, drying layer inner space and drying layer inner space communicate in proper order and form hot-blast exhaust passage. The device still needs to be additionally provided with a heater, and has the defects of higher equipment investment, high energy consumption and the like.
Disclosure of utility model
The utility model aims to solve the problems of higher equipment investment, high energy consumption and the like in the prior art, provides carbonization equipment for biomass garbage treatment, biomass garbage enters a drying layer through a feed inlet, a heat source in the drying layer adopts heat of combustion flue gas, and the dried gas is discharged through an air outlet pipe; the dried biomass garbage enters a carbonization layer, a heat source in the carbonization layer adopts the heat of burning flue gas, and carbonized gas is discharged into an incinerator again through an exhaust pipe to remove harmful gas; and the carbonized material enters a cooling layer, and cooling water cools the material and then is discharged out of the equipment. The utility model is effectively combined with the incinerator, effectively utilizes the heat generated by the incinerator, and simultaneously removes the harmful gas generated by the carbonization layer through the incinerator.
The utility model aims at realizing the following technical scheme:
The utility model provides a biomass waste handles with carbomorphism equipment, includes dry layer, carbomorphism layer and the cooling layer that from top to bottom set gradually, dry layer top is provided with feed inlet, rabbling mechanism and outlet duct, the lower part is provided with first burning flue gas and advances the pipe in the dry layer, first burning flue gas advances to manage and sets up first burning flue gas admission valve, the lower part is provided with second burning flue gas and advances the pipe in the carbomorphism layer, second burning flue gas advances to manage and sets up second burning flue gas admission valve, upper portion is provided with the waste gas exit tube in the carbomorphism layer, first burning flue gas advances pipe and second burning flue gas and advances that the pipe all links to each other with burning flue gas intake manifold, be provided with the cooling intermediate layer outside the cooling layer, be provided with cooling water and cooling water exit tube on the cooling intermediate layer.
Preferably, the lower end of the drying layer is provided with a first blanking valve, the lower end of the carbonization layer is provided with a second blanking valve, and the lower end of the cooling layer is provided with a third blanking valve.
Preferably, a plurality of first combustion flue gas inlet pipes are arranged at the middle lower part of the drying layer.
Preferably, a plurality of second combustion flue gas inlet pipes are arranged at the middle lower part of the carbonization layer.
Preferably, the outer walls of the drying layer and the carbonization layer are both provided with heat insulation layers.
Preferably, the drying layer and the carbonization layer are both provided with manholes.
Preferably, the air outlet pipe is provided with an air outlet valve.
Preferably, the waste gas outlet pipe is provided with a waste gas valve.
Preferably, the stirring mechanism comprises a stirring motor, a stirring shaft and a stirring paddle arranged on the stirring shaft, wherein the stirring motor is arranged above the drying layer, the stirring motor is connected with the stirring shaft, and the stirring shaft penetrates into the drying layer.
The beneficial effects of this technical scheme are as follows:
1. According to the carbonization equipment for biomass garbage treatment, biomass garbage enters the drying layer through the feed inlet, a heat source in the drying layer adopts heat of burning smoke, and the dried gas is discharged through the gas outlet pipe; the dried biomass garbage enters a carbonization layer, a heat source in the carbonization layer adopts the heat of burning flue gas, and carbonized gas is discharged into an incinerator again through an exhaust pipe to remove harmful gas; and the carbonized material enters a cooling layer, and cooling water cools the material and then is discharged out of the equipment. The utility model is effectively combined with the incinerator, effectively utilizes the heat generated by the incinerator, and simultaneously removes the harmful gas generated by the carbonization layer through the incinerator.
2. According to the carbonization equipment for biomass garbage treatment, provided by the utility model, the first blanking valve, the second blanking valve and the third blanking valve are arranged, so that the blanking of the drying layer to the carbonization layer, the blanking of the carbonization layer to the cooling layer and the blanking of the cooling layer to the outside of the equipment are facilitated.
3. According to the carbonization equipment for biomass garbage treatment, provided by the utility model, the plurality of first combustion flue gas inlet pipes and the second combustion flue gas inlet pipes can enable the combustion flue gas to be more uniform in inlet, and can effectively control the temperatures in the drying layer and the carbonization layer.
4. According to the carbonization equipment for biomass garbage treatment, disclosed by the utility model, the heat dissipation is avoided due to the arrangement of the heat preservation layer, and the energy consumption is reduced.
Drawings
FIG. 1 is a schematic diagram of the structure of the present utility model;
In the figure: 100. drying the layer; 101. a feed inlet; 102. an air outlet pipe; 103. an air outlet valve; 104. a first combustion flue gas inlet pipe; 105. a first combustion flue gas inlet valve; 106. a first blanking valve; 110. a stirring mechanism; 111. a stirring motor; 112. a stirring shaft; 113. stirring paddles; 200. a charring layer; 210. a second combustion flue gas inlet pipe; 202. a second combustion flue gas inlet valve; 203. an exhaust gas outlet pipe; 204. an exhaust valve; 205. a second blanking valve; 300. a cooling layer; 301. cooling the interlayer; 302. a cooling water inlet pipe; 303. a cooling water outlet pipe; 304. a third blanking valve; 400. a combustion flue gas inlet header pipe; 500. a heat preservation layer; 600. and (5) a manhole.
Detailed Description
The present utility model will be described in further detail with reference to examples, but embodiments of the present utility model are not limited thereto.
It is noted that when an element is referred to as being "mounted," "secured," or "disposed" on another element, it can be directly on the other element or intervening elements may also be present. When an element is referred to as being "connected to" another element, it can be directly connected to the other element or intervening elements may also be present.
It should be noted that, in the embodiments of the present utility model, terms such as left, right, up, and down are merely relative concepts or references to normal use states of the product, and should not be construed as limiting.
Example 1
As shown in fig. 1, the carbonization device for biomass garbage treatment comprises a drying layer 100, a carbonization layer 200 and a cooling layer 300 which are sequentially arranged from top to bottom, wherein a feed inlet 101, a stirring mechanism 110 and an air outlet pipe 102 are arranged above the drying layer 100, the air outlet pipe 102 is connected with a tail gas treatment system, the tail gas treatment system is in the prior art, and the tail gas treatment system is arranged for reducing dust and cooling; the lower part is provided with first burning flue gas intake pipe 104 in the dry layer 100, set up first burning flue gas admission valve 105 on the first burning flue gas intake pipe 104, the lower part is provided with second burning flue gas intake pipe 210 in the carbomorphism layer 200, set up second burning flue gas admission valve 202 on the second burning flue gas intake pipe 210, the upper part is provided with waste gas exit tube 203 in the carbomorphism layer 200, waste gas exit tube 203 links to each other with the burning furnace, first burning flue gas intake pipe 104 and second burning flue gas intake pipe 210 all link to each other with burning flue gas intake manifold 400, burning flue gas intake manifold 400 links to each other with the burning furnace, effectively retrieves the heat of the burning flue gas that burns the burning furnace and produce, be provided with cooling interlayer 301 outward in cooling layer 300, be provided with cooling water intake pipe 302 and cooling water exit tube 303 on the cooling interlayer 301.
Example 2
The difference between this embodiment and embodiment 1 is that: the lower end of the drying layer 100 is provided with a first blanking valve 106, the lower end of the carbonization layer 200 is provided with a second blanking valve 205, the lower end of the cooling layer 300 is provided with a third blanking valve 304, the drying time of the drying layer 100 is 1-4h, the temperature of the drying layer 100 is controlled to be 180-220 ℃, and the temperature is controlled through a temperature sensor in the drying layer 100 and the air inflow of combustion flue gas; the temperature in the carbonization layer 200 is 400-600 ℃ (the temperature is controlled by a temperature sensor in the carbonization layer 200 and the air inflow of combustion flue gas), and the carbonization time is 1-2h.
Wherein, the drying layer 100 is provided with a plurality of first combustion flue gas inlet pipes 104 at the middle and lower parts thereof.
Wherein, the carbonization layer 200 is provided with a plurality of second combustion flue gas inlet pipes 210 at the middle lower part thereof.
Wherein, the outer walls of the drying layer 100 and the carbonization layer 200 are both provided with an insulation layer 500.
Wherein, the manhole 600 is provided on both the drying layer 100 and the carbonization layer 200.
Wherein, the air outlet pipe 102 is provided with an air outlet valve 103.
Wherein, the exhaust gas outlet pipe 203 is provided with an exhaust gas valve 204.
Wherein, rabbling mechanism 110 includes agitator motor 111, (mixing) shaft 112 and sets up the stirring rake 113 on (mixing) shaft 112, agitator motor 111 sets up in dry layer 100 top, agitator motor 111 links to each other with (mixing) shaft 112, inside (mixing) shaft 112 penetrated dry layer 100.
The beneficial effects of this technical scheme are as follows:
1. According to the carbonization equipment for biomass garbage treatment, biomass garbage enters the drying layer 100 through the feeding hole 101, a heat source in the drying layer 100 adopts heat of combustion flue gas, and the dried gas is discharged through the gas outlet pipe 102; the dried biomass garbage enters a carbonization layer 200, a heat source in the carbonization layer 200 adopts the heat of burning flue gas, and carbonized gas is discharged into an incinerator again through an exhaust pipe to remove harmful gas; the carbonized material enters the cooling layer 300, and the cooling water cools the material and then is discharged out of the device. The present utility model is effectively combined with the incinerator, effectively utilizes heat generated from the incinerator, and simultaneously removes harmful gas generated from the char layer 200 through the incinerator.
2. The carbonization equipment for biomass garbage disposal provided by the utility model is convenient for the drying layer 100 to discharge the carbonization layer 200, the carbonization layer 200 to discharge the cooling layer 300 and the cooling layer 300 to discharge the equipment.
3. The carbonization equipment for biomass garbage treatment provided by the utility model has the advantages that the plurality of first combustion flue gas inlet pipes 104 and the second combustion flue gas inlet pipes 210 can enable the combustion flue gas to be more uniform in inlet, and the temperatures in the drying layer 100 and the carbonization layer 200 can be effectively controlled.
4. According to the carbonization equipment for biomass garbage treatment, disclosed by the utility model, the heat dissipation is avoided by arranging the heat preservation layer 500, and the energy consumption is reduced.
The foregoing description is only a preferred embodiment of the present utility model, and is not intended to limit the present utility model in any way, and any simple modification, equivalent variation, etc. of the above embodiment according to the technical matter of the present utility model fall within the scope of the present utility model.
Claims (9)
1. Carbonization equipment for biomass garbage treatment, which is characterized in that: including drying layer (100), carbonization layer (200) and cooling layer (300) that set gradually from top to bottom, drying layer (100) top is provided with feed inlet (101), rabbling mechanism (110) and outlet duct (102), the lower part is provided with first burning flue gas intake pipe (104) in drying layer (100), set up first burning flue gas admission valve (105) on first burning flue gas intake pipe (104), the lower part is provided with second burning flue gas intake pipe (210) in carbonization layer (200), set up second burning flue gas admission valve (202) on second burning flue gas intake pipe (210), well upper portion is provided with waste gas exit tube (203) in carbonization layer (200), first burning flue gas intake pipe (104) and second burning flue gas intake pipe (210) all link to each other with burning flue gas air intake manifold (400), cooling layer (300) are provided with cooling intermediate layer (301) outward, be provided with cooling water intake pipe (302) and cooling water exit tube (303) on cooling intermediate layer (301).
2. The carbonization device for biomass refuse treatment according to claim 1, characterized in that: the drying layer (100) lower extreme is provided with first unloading valve (106), carbonization layer (200) lower extreme is provided with second unloading valve (205), cooling layer (300) lower extreme is provided with third unloading valve (304).
3. The carbonization device for biomass refuse treatment according to claim 1, characterized in that: the middle lower part of the drying layer (100) is provided with a plurality of first combustion flue gas inlet pipes (104).
4. The carbonization device for biomass refuse treatment according to claim 1, characterized in that: the middle lower part of the carbonization layer (200) is provided with a plurality of second combustion flue gas inlet pipes (210).
5. The carbonization device for biomass refuse treatment according to claim 1, characterized in that: and the outer walls of the drying layer (100) and the carbonization layer (200) are both provided with heat preservation layers (500).
6. The carbonization device for biomass refuse treatment according to claim 1, characterized in that: and manholes (600) are formed in the drying layer (100) and the carbonization layer (200).
7. The carbonization device for biomass refuse treatment according to claim 1, characterized in that: an air outlet valve (103) is arranged on the air outlet pipe (102).
8. The carbonization device for biomass refuse treatment according to claim 1, characterized in that: an exhaust valve (204) is arranged on the exhaust gas outlet pipe (203).
9. The carbonization device for biomass refuse treatment according to claim 1, characterized in that: the stirring mechanism (110) comprises a stirring motor (111), a stirring shaft (112) and a stirring paddle (113) arranged on the stirring shaft (112), wherein the stirring motor (111) is arranged above the drying layer (100), the stirring motor (111) is connected with the stirring shaft (112), and the stirring shaft (112) penetrates into the drying layer (100).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202323141381.9U CN221192076U (en) | 2023-11-21 | 2023-11-21 | Carbonization equipment for biomass garbage treatment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202323141381.9U CN221192076U (en) | 2023-11-21 | 2023-11-21 | Carbonization equipment for biomass garbage treatment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN221192076U true CN221192076U (en) | 2024-06-21 |
Family
ID=91527664
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202323141381.9U Active CN221192076U (en) | 2023-11-21 | 2023-11-21 | Carbonization equipment for biomass garbage treatment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN221192076U (en) |
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2023
- 2023-11-21 CN CN202323141381.9U patent/CN221192076U/en active Active
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