CN205717221U - Organic waste incineration system - Google Patents
Organic waste incineration system Download PDFInfo
- Publication number
- CN205717221U CN205717221U CN201620318390.1U CN201620318390U CN205717221U CN 205717221 U CN205717221 U CN 205717221U CN 201620318390 U CN201620318390 U CN 201620318390U CN 205717221 U CN205717221 U CN 205717221U
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- China
- Prior art keywords
- heat
- combustor
- gas
- incinerator
- pipe
- Prior art date
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- Expired - Fee Related
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- 239000010815 organic waste Substances 0.000 title claims abstract description 26
- 238000004056 waste incineration Methods 0.000 title claims abstract description 16
- 239000007789 gas Substances 0.000 claims abstract description 54
- 239000002912 waste gas Substances 0.000 claims abstract description 42
- 239000007788 liquid Substances 0.000 claims abstract description 22
- 238000004227 thermal cracking Methods 0.000 claims abstract description 19
- 238000000746 purification Methods 0.000 claims abstract description 17
- 239000002910 solid waste Substances 0.000 claims abstract description 7
- 239000002699 waste material Substances 0.000 claims abstract description 7
- 238000007599 discharging Methods 0.000 claims abstract description 6
- 238000009825 accumulation Methods 0.000 claims description 9
- 238000010521 absorption reaction Methods 0.000 claims description 7
- 239000005457 ice water Substances 0.000 claims description 4
- 238000005336 cracking Methods 0.000 claims 1
- 230000008014 freezing Effects 0.000 claims 1
- 238000007710 freezing Methods 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 16
- 230000008569 process Effects 0.000 abstract description 15
- 239000007787 solid Substances 0.000 abstract description 14
- 239000000446 fuel Substances 0.000 abstract description 13
- 230000000694 effects Effects 0.000 abstract description 9
- 230000008859 change Effects 0.000 description 5
- 239000010808 liquid waste Substances 0.000 description 3
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 239000003973 paint Substances 0.000 description 2
- 210000003437 trachea Anatomy 0.000 description 2
- 230000003796 beauty Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000010813 municipal solid waste Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000010422 painting Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Incineration Of Waste (AREA)
Abstract
This utility model is relevant a kind of organic waste incineration system, it includes: a waste gas incinerator, there is one first combustor, and this first combustor relatively arranges an exhaust inlet pipe and a purification gas exhaustor, arranges one first burner in this first combustor；One thermal cracking incinerator, there is one second combustor, and this second combustor relatively arranges a solid waste input port, an incineration waste gas airway, one second burner and an ash discharging hole, and the tail end of this incineration waste gas airway is made to be incorporated into the first combustor of this waste gas incinerator；And a waste liquid nozzle, it is arranged at this first combustor and/or this second combustor.Whereby, the problem that cannot simultaneously process liquid, gas and solid organic castoff in order to solve prior art, and there is liquid, gas and solid organic castoff and can process simultaneously and reduce the effect incinerating demand for fuel.
Description
Technical field
This utility model is relevant a kind of organic waste incineration system, and espespecially one borrows thermal cracking to burn
Change stove and process solid and liquid organic waste, and organic with liquid by waste gas incinerator process gases
The design of garbage.
Background technology
In commercial production operation in addition to processing product, also can produce the organic waste of many
Thing, as the most widely used spray process, though can be gone out outside beauty by product painting expeditiously
See, but in spraying operation, the coating cloud of high degree of dispersion, the solvent evaporated and paint vehicle are unattached
In the paint slag that workpiece is formed, respectively become the organic waste of liquid, gas and solid, these
Industrial organic wastes will be collected and be acted upon avoiding polluting environment；But, at incineration
Reason has goodish treatment effect for industrial organic wastes, but existing cremation facilities there is no
Method meets the incineration process demand with liquid, gas and solid organic castoff.
Utility model content
Asking of liquid, gas and solid organic castoff cannot be processed for solving prior art simultaneously
Topic, this utility model provides a kind of organic waste incineration system, and it has liquid, gas and consolidates
Effect that body organic waste can process simultaneously；Have and reduce the effect incinerating demand for fuel.
This utility model solves its technical problem and be the technical scheme is that
A kind of organic waste incineration system, includes: a waste gas incinerator, has one first combustion
Burning room, and this first combustor relatively arranges an exhaust inlet pipe and a purification gas exhaustor, this is the years old
One first burner is set in one combustor；One thermal cracking incinerator, has one second combustor,
And relatively this second combustor arrange a solid waste input port, one incinerate waste gas airway, one
Second burner and an ash discharging hole, and make the tail end of this incineration waste gas airway be incorporated into this waste gas burning
Change the first combustor of stove；And a waste liquid nozzle, be arranged at this first combustor and/or this second
Combustor.This thermal cracking incinerator is rotary kiln incinerator.
Additionally, this exhaust inlet pipe maybe this purification gas exhaustor arranges a blower fan.This waste gas incinerator
For direct-fired waste gas incinerator.This waste gas incinerator further combined with a gas to gas-heat exchanger.
Furthermore, this waste gas incinerator is heat accumulation type off-gas incinerator.This first combustor and this waste gas
There is between air inlet pipe and this purification gas exhaustor one first regenerator and one second regenerator, and in
This exhaust inlet pipe and this purification gas exhaustor are provided with flow direction control valve.One used heat is set further
Acquisition unit, bypasses the heat supply side of a convection heater and is linked to above this first combustor, and
Heat side in this convection heater be linked with used heat capture pipe, this used heat capture pipe low-temperature zone with
Hot bypass pipe is picked in the intersegmental link of high temperature one, and this low-temperature zone is picked hot bypass pipe with this and is respectively arranged with and picks heat
Flow control valve, this high temperature section be provided with pick heat detect temperature device, and by this pick heat flow control valve with should
Picking heat to detect temperature device and be linked to one and pick heat flow controller, this picks heat flow controller is to pick heat according to this
Detecing the temperature temperature detected of device and control this ratio aperture picking heat flow control valve, it is right by this to adjust
The used heat of stream heater captures air-flow ratio, picks hot temperature with control that this used heat captures pipe, separately in
This used heat acquisition pipe is provided with picks hot-air blower；And a steam thermal source absorption refrigerating machine, order is internal
Generator and this used heat capture the high temperature section of pipe and link and produce heat exchange, and outside is linked with cold
Radiator cooler and refrigerating plant, separately the ice water circulation pipe in this refrigerating plant is provided with cold degree and detects temperature device,
And this cold degree detectd temperature device pick hot-air blower with this and be linked to a cold degree controller, this cold degree controller is
Detect the temperature temperature detected of device according to this cold degree and control this air output picking hot-air blower, adjust this used heat
The used heat capturing pipe captures air quantity.This used heat acquisition pipe is sent out with this steam thermal source absorption refrigerating machine
Raw device produces the discharge section after heat exchange, links back this entrance side picking hot-air blower further and reclaims remaining
Temperature.
Whereby, this thermal cracking incinerator processes solid and liquid organic waste, and is burnt by this waste gas
Change process gases and liquid organic waste at stove, and order is by means of the incineration after the process of this thermal cracking incinerator
Waste gas enters back into this first combustor, and allows organic liquid waste regard fuel, and has liquid, gas
Can process simultaneously and reduce the effect incinerating demand for fuel with solid organic castoff.
The beneficial effects of the utility model are, it has liquid, gas and solid organic castoff can
The effect simultaneously processed；Have and reduce the effect incinerating demand for fuel.
Accompanying drawing explanation
With embodiment, this utility model is further illustrated below in conjunction with the accompanying drawings.
Fig. 1 is the structural representation of this utility model first embodiment.
Fig. 2 is the structural representation of this utility model the second embodiment.
Label declaration in figure:
The direct-fired waste gas incinerator of 10a
10b heat accumulation type off-gas incinerator
11a, 11b first combustor
12a, 12b exhaust inlet pipe
13a, 13b purify gas exhaustor
14a, 14b first burner
15a, 15b blower fan
16 gas are to gas-heat exchanger
16a the first regenerator
16b the second regenerator
17 flow direction control valves
20 thermal cracking incinerators
21 second combustor
22 solid waste input ports
23 incinerate waste gas airway
24 second burners
25 ash discharging holes
30 waste liquid nozzles
50 used heat acquisition units
51 convection heaters
511 heat supply sides
512 heat sides
52 used heat capture pipe
521 low-temperature zone
522 high temperature section
523 discharge section
53 pick hot bypass pipe
54a, 54b pick heat flow control valve
55 pick heat detects temperature device
56 pick heat flow controller
57 pick hot-air blower
60 steam thermal source absorption refrigerating machines
70 chillers
80 refrigerating plants
81 ice water circulation pipes
82 cold degree detect temperature device
83 cold degree controllers
Detailed description of the invention
First, referring to Fig. 1, this utility model first embodiment includes: a direct-fired waste gas burns
Change stove 10a, there is one first combustor 11a, and this first combustor 11a relatively arranges a waste gas and enters
Trachea 12a and one purifies gas exhaustor 13a, arranges one first burner in this first combustor 11a
14a, and one blower fan 15a is set in this exhaust inlet pipe 12a maybe this purification gas exhaustor 13a, this is years old
One burner 14a can be with gas as fuel, and this direct-fired waste gas incinerator 10a is further combined with a gas
To gas-heat exchanger 16；One thermal cracking incinerator 20, has one second combustor 21, and relatively should
Second combustor 21 arranges a solid waste input port 22, and incinerates waste gas airway 23,1 the
Two burner 24 and ash discharging holes 25, and it is straight to make the tail end of this incineration waste gas airway 23 be incorporated into this
The first combustor 11a of combustion waste gas incinerator 10a, this thermal cracking incinerator 20 can be that rotary kiln burns
Changing stove, this second burner 24 can be with gas as fuel；And a waste liquid nozzle 30, it is arranged at this
First combustor 11a and/or this second combustor 21.
Furthermore, referring to Fig. 2, this utility model the second embodiment includes: a heat accumulation type off-gas burns
Change stove 10b, there is one first combustor 11b, and this first combustor 11b relatively arranges a waste gas and enters
Trachea 12b and one purifies gas exhaustor 13b, arranges one first burner in this first combustor 11b
14b, and one blower fan 15b is set in this exhaust inlet pipe 12b maybe this purification gas exhaustor 13b, this is years old
One burner 14b can be with gas as fuel, this first combustor 11b and this exhaust inlet pipe 12b and should
Purify, between gas exhaustor 13b, there is one first regenerator 16a and one second regenerator 16b, and in this
Exhaust inlet pipe 12b and this purification gas exhaustor 13b is provided with flow direction control valve 17, this traffic organising
Valve 17 in order to control air-flow to be incinerated from this exhaust inlet pipe 12b enter this first regenerator 16a (or
Second regenerator 16b), and after controlling to incinerate air-flow via (or the first accumulation of heat of this second regenerator 16b
Room 16a) enter this purification gas exhaustor 13b；One used heat acquisition unit 50, by a convection heater 51
Heat supply side 511 bypass be linked to above the first combustor 11b of this heat accumulating type incinerator 10b, and be somebody's turn to do
The heat supply side 511 of the first combustor 11b and this convection heater 51 is because of (this heat supply side 511, relative position
It is positioned at above this first combustor 11b) and temperature difference (chamber temperature is up to 700～850 DEG C) generation
Free convection heat passes phenomenon, and is linked with used heat in the heat side 512 of this convection heater 51 and captures pipe
52, this used heat captures link one between the low-temperature zone 521 of pipe 52 and high temperature section 522 and picks hot bypass pipe 53,
This low-temperature zone 521 is picked hot bypass pipe 53 with this and is respectively arranged with and picks heat flow control valve 54a, 54b, should
High temperature section 522 be provided with pick heat detect temperature device 55, and this is picked heat flow control valve 54a, 54b picks with this
Heat is detectd temperature device 55 and is linked to one and picks heat flow controller 56, and this picks heat flow controller 56 is according to should
Pick heat to detect the temperature temperature detected of device 55 and control this ratio aperture picking heat flow control valve 54a, 54b,
Adjust and capture air-flow ratio by the used heat of this convection heater 51, to control this used heat acquisition pipe 52
Pick hot temperature (can be 450 DEG C), separately capture pipe 52 in this used heat and be provided with and pick hot-air blower 57；One heat
Gas thermal source absorption refrigerating machine 60, the generator within order captures the high temperature section 522 of pipe 52 with this used heat
Link and produce heat exchange, and outside is linked with chiller 70 and refrigerating plant 80, separately in this system
The ice water circulation pipe 81 of device for cooling 80 is provided with cold degree and detects temperature device 82 (circulation frozen water is usually 7 DEG C of outflows
12 DEG C flow back to), and this cold degree is detectd temperature device 82 pick hot-air blower 57 with this and be linked to a cold degree controller
83, this cold degree controller 83 is to detect the temperature temperature detected of device 82 according to this cold degree to control this and pick hot blast
The air output of machine 57, adjusts this used heat and captures the used heat acquisition air quantity of pipe 52；Wherein, this used heat is picked
Take the discharge section after the generator generation heat exchange of pipe 52 and this steam thermal source absorption refrigerating machine 60
523, can link back the remaining temperature of this entrance side picking hot-air blower 57 recovery further (the most still has 165 DEG C
Yu Wen)；One thermal cracking incinerator 20, has one second combustor 21, and this second combustor relatively
21 arrange a solid waste input port 22, incinerates waste gas airway 23,1 second burner 24
With an ash discharging hole 25, and make the tail end of this incineration waste gas airway 23 be incorporated into this heat accumulation type off-gas burning
Changing the first combustor 11b of stove 10b, this thermal cracking incinerator 20 can be rotary kiln incinerator, and this is the years old
Two burners 24 can be with gas as fuel；And a waste liquid nozzle 30, it is arranged at this first combustor
11b and/or this second combustor 21.
Based on above-mentioned composition, solid organic castoff can put into from this solid waste input port 22 should
Thermal cracking incinerator 20, and carry out thermal cracking oxidation in this second combustor 21, SOLID ORGANIC is discarded
Thing is oxidized to incinerate waste gas and lime-ash by thermal cracking, incinerates waste gas again from this incineration waste gas airway 23
This first combustor 11a or this heat accumulation type off-gas that are directed to this direct-fired waste gas incinerator 10a incinerate
This first combustor 11b of stove 10b, purification of again burning；Furthermore, organic exhaust gas then can give up from this
Gas air inlet pipe 12a, 12b import this direct-fired waste gas incinerator 10a or this heat accumulation type off-gas incinerator
10b, and the incineration aoxidized by thermal cracking with solid organic castoff in this first combustor 11a, 11b
Waste gas together burns purification, burning purify after purifying gas flow then from this purification gas exhaustor 13a, 13b
Discharge；But, organic liquid waste then can by this waste liquid nozzle 30 be sprayed on this first combustor 11a,
11b and/or this second combustor 21, not only can be burned purification and also can regard fuel.
Therefore this utility model can borrow this thermal cracking incinerator 20 to process solid and liquid organic waste
Thing, and by this direct-fired waste gas incinerator 10a or this heat accumulation type off-gas incinerator 10b process gases with
Liquid organic waste, and there is the merit that liquid, gas and solid organic castoff can process simultaneously
Effect；Additionally, the incineration waste gas after borrowing this thermal cracking incinerator 20 to process enters back into this first combustor
11a, 11b, except can again burn purification in addition to, may also provide heat energy to this first combustor 11a,
11b, reduces fuel (gas) usage amount of this first burner 14a, 14b, adds that organic liquid waste is also
Fuel can be regarded, all have and reduce the effect incinerating demand for fuel.
The above, be only preferred embodiment of the present utility model, not to this utility model
Make any pro forma restriction, every according to technical spirit of the present utility model to above example institute
Any simple modification, equivalent variations and the modification made, all still falls within technical solutions of the utility model
In the range of.
In sum, this utility model designs in structure, uses in practicality and cost benefit, complete
Structure needed for entirely meeting industry development and disclosed is also to have unprecedented innovative structure,
There is novelty, creativeness, practicality, meet the regulation about utility model patent important document, therefore
Mention application in accordance with the law.
Claims (10)
1. an organic waste incineration system, it is characterised in that including:
One waste gas incinerator, has one first combustor, and this first combustor relatively arranges one and gives up
Gas air inlet pipe purifies gas exhaustor with one, arranges one first burner in this first combustor；
One thermal cracking incinerator, has one second combustor, and this second combustor arranges one relatively
Solid waste input port, an incineration waste gas airway, one second burner and an ash discharging hole, and
The tail end making this incineration waste gas airway is incorporated into the first combustor of this waste gas incinerator；And
One waste liquid nozzle, is arranged at this first combustor and/or this second combustor.
Organic waste incineration system the most according to claim 1, it is characterised in that described useless
Gas air inlet pipe maybe this purification gas exhaustor arranges a blower fan.
Organic waste incineration system the most according to claim 1 and 2, it is characterised in that institute
Stating waste gas incinerator is direct-fired waste gas incinerator.
Organic waste incineration system the most according to claim 3, it is characterised in that described useless
Gas incinerator further combined with a gas to gas-heat exchanger.
Organic waste incineration system the most according to claim 4, it is characterised in that described heat
Cracking incinerator is rotary kiln incinerator.
Organic waste incineration system the most according to claim 1 and 2, it is characterised in that institute
Stating waste gas incinerator is heat accumulation type off-gas incinerator.
Organic waste incineration system the most according to claim 6, it is characterised in that described
Between one combustor and this exhaust inlet pipe and this purification gas exhaustor, there is one first regenerator and
Second regenerator, and this exhaust inlet pipe and this purification gas exhaustor are provided with flow direction control valve.
Organic waste incineration system the most according to claim 7, it is characterised in that further
One used heat acquisition unit is set, the heat supply side of a convection heater is bypassed and is linked to this first burning
Above room, and being linked with used heat in the heat side of this convection heater and capture pipe, this used heat captures pipe
Low-temperature zone and the intersegmental link of high temperature one pick hot bypass pipe, this low-temperature zone is picked hot bypass pipe with this and is distinguished
Being provided with and pick heat flow control valve, this high temperature section is provided with picks heat and detects temperature device, and this is picked heat flow
Control valve is picked heat with this and is detectd temperature device and be linked to one and pick heat flow controller, and this is picked heat flow controller and is
Pick heat according to this to detect the temperature temperature detected of device and control this ratio aperture picking heat flow control valve, adjust
The whole used heat by this convection heater captures air-flow ratio, picks heat with control that this used heat captures pipe
Temperature, is separately provided with in this used heat acquisition pipe and picks hot-air blower；And the absorption freezing of steam thermal source
Machine, the high temperature section that the generator within order captures pipe with this used heat links and produces heat exchange, and outer
Portion is linked with chiller and refrigerating plant, and separately the ice water circulation pipe in this refrigerating plant is provided with cold
Degree detects temperature device, and this cold degree is detectd temperature device picks hot-air blower with this and be linked to a cold degree controller, and this is cold
Degree controller is to detect the temperature temperature detected of device according to this cold degree to control this air output picking hot-air blower,
Adjust this used heat and capture the used heat acquisition air quantity of pipe.
Organic waste incineration system the most according to claim 8, it is characterised in that described useless
Heat captures the discharge section after the generator generation heat exchange of pipe and this steam thermal source absorption refrigerating machine,
Link back this entrance side picking hot-air blower further and reclaim remaining temperature.
Organic waste incineration system the most according to claim 9, it is characterised in that described
Thermal cracking incinerator is rotary kiln incinerator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620318390.1U CN205717221U (en) | 2016-04-15 | 2016-04-15 | Organic waste incineration system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620318390.1U CN205717221U (en) | 2016-04-15 | 2016-04-15 | Organic waste incineration system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205717221U true CN205717221U (en) | 2016-11-23 |
Family
ID=57307960
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620318390.1U Expired - Fee Related CN205717221U (en) | 2016-04-15 | 2016-04-15 | Organic waste incineration system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205717221U (en) |
-
2016
- 2016-04-15 CN CN201620318390.1U patent/CN205717221U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20161123 Termination date: 20200415 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |