CN107270300A - A kind of house refuse living area tupe - Google Patents
A kind of house refuse living area tupe Download PDFInfo
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- CN107270300A CN107270300A CN201710547527.XA CN201710547527A CN107270300A CN 107270300 A CN107270300 A CN 107270300A CN 201710547527 A CN201710547527 A CN 201710547527A CN 107270300 A CN107270300 A CN 107270300A
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- CN
- China
- Prior art keywords
- living area
- house refuse
- alkali lye
- sedimentation tank
- flue gas
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/08—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating
- F23G5/14—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
- F23J15/04—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material using washing fluids
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/06—Arrangements of devices for treating smoke or fumes of coolers
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/30—Technologies for a more efficient combustion or heat usage
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The present invention relates to a kind of house refuse living area tupe, divide living area, and the house refuse of the generation in each living area marked off is carried out integrating sorting, the combustiblerefuse sub-elected is subjected to burning disposal using the burning facility in the living area, simultaneously by the organic waste sub-elected directly using pulp degraded equipment progress pulp processing, and organic waste after pulp is handled is discharged into degraded pond nearby.The beneficial effects of the invention are as follows：Save a large amount of human and material resources, financial resources and land resource, effectively control pollution spread diffusion, waste volumes are reduced, many pollution of the rubbish to soil, river, underground water, air and our visible space is reduced, the rubbish residence time is short, the non-complete fermentation of organic substance, repeated contamination is few, and sorting classification is easy, reduces house refuse gaseous contamination, visual pollution, more than 95% pollution, can give full play to existing degraded pond in living area between reduction garbage substance.
Description
Technical field
The present invention relates to technical field of domestic garbage treatment, more particularly to a kind of house refuse living area tupe.
Background technology
As China's Urbanization Construction is accelerated, China human mortality is increasingly concentrated, and adds abundant, the life of our life products
Articles for use are various, convenient, and we increase considerably the quantity of refuse of daily life.
Rubbish is the derivative of our daily lifes：Swill raffinate, beverage washing raffinate, food processing additives,
Disposable daily necessities, packaging group etc., volume is small, and recovery utilization rate is not high.The processing method of current house refuse has：Landfill
Processing, burning disposal, compost treatment, the processing of part synthetical recovery etc..
The processing of current house refuse is usually to arrive the consumer waste transferring in living area first with rubbish van
Large-scale incineration plant beyond the living area of people is gone to concentrate and completed, and house refuse is the drawbacks of focus on：
1) intensive quantity is bigger, and the related smell of generation is bigger, and spread scope is also bigger, also easier appearance mutually pollution；
2) intensive quantity is more, and visual pollution is bigger；
3) central incineration, organic matter and inorganic matter therein are obscured, and fuel value is very low, corresponding burning cost nor
Chang Gao；
4) house refuse centralized burning, the recirculated water (acidity) and flue gas of generation can not controls up to par；
5) house refuse is focused on, the volatilization of its offensive gases, poisonous and harmful flue gas, has quite big to local resident's life
Harm and influence；
6) house refuse is focused on, many unfavorable shadows such as infectious disease, spread of germs, air pollution, Land Environment pollution
Ring；
7) rubbish focuses on inherently regional pollution；
8) rubbish can be stopped a very long time during outward transport is concentrated, and most of organic waste can start fermentation, easily
There is the growth of rubbish pest and disease damage, it may appear that cross pollution, it has not been convenient to which inorganic refuse is burned.
The content of the invention
The technical problems to be solved by the invention are to provide a kind of house refuse living area tupe, above-mentioned to overcome
Deficiency of the prior art.
The technical scheme that the present invention solves above-mentioned technical problem is as follows：A kind of house refuse living area tupe, draws
Divide living area, and the house refuse of the generation in each living area marked off is carried out integrating sorting, will sub-elect
Combustiblerefuse carry out burning disposal using the burning facility in the living area, while by the organic waste sub-elected
Directly pulp processing is carried out using pulp degraded equipment, and the organic waste after pulp is handled is discharged into degraded pond nearby
It is interior.
The beneficial effects of the invention are as follows：Direct incineration of combustible rubbish timely in living area, saves a large amount of manpowers, thing
Power, financial resources and land resource, form garbage disposal terminal, can improve resident's environmental consciousness and quality of life, effectively control pollution
Spreading and diffusion, reduces waste volumes, reduces rubbish to many of soil, river, underground water, air and our visible space
Pollution, greatly purifies our living space, improves urban environmental hygiene quality and city integral image；By directly at me
Organic waste is timely and effectively handled in living area, such rubbish residence time is short, and organic substance is not sent out completely
Ferment, repeated contamination is few, and sorting classification is easy, greatly reduces between house refuse gaseous contamination, visual pollution, reduction garbage substance
The growth of more than 95% pollution, effectively control rubbish pest and disease damage, it is to avoid cross pollution, it is to avoid the propagation of infectious disease, and can carry
High garbage reclamation amount, facilitates combustiblerefuse to burn；Existing degraded pond in living area can be given full play to, accomplishes that rubbish is not outer
Fortune.
On the basis of above-mentioned technical proposal, the present invention can also do following improvement.
Further, it is that a standard is carried out by 4000-7000 resident family when dividing living area.
Further, the amount of burning facility day incineration of combustible rubbish is/8h.
Further, when carrying out integrating sorting to house refuse, recyclable rubbish is also sub-elected, and it is carried out at recovery
Reason.
Further, burning facility includes CIU, waste heat boiler, system for cleaning fume；The smoke evacuation of CIU
Mouth is connected with the air inlet of waste heat boiler；System for cleaning fume is followed including one-level spray dust device, lye pump and alkali lye
Ring sedimentation basin, the exhaust outlet of waste heat boiler is connected with the air inlet of one-level spray dust device, and lye pump is used to circulate alkali lye
Alkali lye in sedimentation basin is supplied in one-level spray dust device and sprayed, and leakage fluid dram and the alkali lye of one-level spray dust device are circulated
Sedimentation basin is connected.
Further, system for cleaning fume also includes the second-class impact dust settler, blower unit, and the second-class impact dust settler is set
Put on alkali lye circulating sedimentation tank, the smoke inlet of the second-class impact dust settler is connected with alkali lye circulating sedimentation tank, one-level spray drop
The exhaust opening of dirt device is connected by blower unit with the smoke inlet of alkali lye circulating sedimentation tank, the smoke inlet on alkali lye circulating sedimentation tank
Below the metal line of the alkali lye circulating sedimentation tank.
Further, system for cleaning fume also includes smoke eliminator, the exhaust opening and cigarette of the second-class impact dust settler
The air inlet of air purifying apparatus is connected.
Further, combustiblerefuse carries out comprising the following steps that for burning disposal using burning facility：
S101, the combustiblerefuse sub-elected burned using CIU, the flue gas after burning is discharged into by flue
Into waste heat boiler；
After S102, flue gas are entered in waste heat boiler, cold and hot exchange is carried out in waste heat boiler, heat, release heat is discharged
Flue gas after amount is entered in one-level spray dust device by flue；
Alkali lye in alkali lye circulating sedimentation tank is supplied in one-level spray dust device by S103, lye pump, and to entering
Flue gas in one-level spray dust device is sprayed；
S104, the flue gas after spray process are entered in alkali lye circulating sedimentation tank by blower unit, and are followed with alkali lye
Alkali lye water-bath type contact in ring sedimentation basin, the fully flue gas after washing are entered in the second-class impact dust settler, then by two grades of punchings
Dust settler is hit to be drained into smoke eliminator；
S105, smoke eliminator are purified to the flue gas entered in it, and low-altitude discharged is to air after the completion of purification
In.
It is using above-mentioned further beneficial effect：The quality of discharge flue gas is ensure that, it is consistent with hotel food and beverage discharge, do
To low latitude qualified discharge, i.e., the resident in living area is not impacted, can so set up and burn in each living area
Equipment is burnt, so as to solve the problems, such as waste incineration in populated areas, disperses quantitative burning, in addition, whole equipment is transported daily
The row time is 8 hours, and it is 1.2T-1.5T that it, which handles quantity of refuse, is burned by quantitative timing, produced very small amount recirculated water can
To accomplish only change within every 100 days 30kg recirculated waters, waste water is directly discharged into degraded pond, reduces the pollution to environment.
Further, pulp degraded equipment includes movable carrier, shear, grinding mechanism, transfer tank；Transfer tank is set
On movable carrier；Shear is arranged on transfer tank, the discharge gate of shear and the intracavity inter-connection of transfer tank；Mill
Crushing device is arranged on transfer tank, the discharge gate of grinding mechanism and the intracavity inter-connection of transfer tank；Transfer tank is provided with and transfer
The blow-off pipe of the intracavity inter-connection of tank.
Further, comprising the following steps that for pulp processing is carried out using pulp degraded equipment：
S201, organic waste is sheared or ground using shear or grinding mechanism granulate, and will be obtained granular
Organic waste carries out interim storage by transfer tank.
It is using above-mentioned further beneficial effect：Be conducive to material smooth discharge and quick effectively degraded.
Brief description of the drawings
Fig. 1 is the structural representation of the burning facility；
Fig. 2 is the structural representation of smoke eliminator；
Fig. 3 is the theory diagram of the burning facility；
Fig. 4 is the structural representation of pulp degraded equipment.
Embodiment
The principles and features of the present invention are described below, and the given examples are served only to explain the present invention, is not intended to limit
Determine the scope of the present invention.
A kind of house refuse living area tupe, divides living area, and in each living area marked off
The house refuse of the generation is carried out integrating sorting, and the combustiblerefuse sub-elected is utilized to the burning being arranged in the living area
Equipment carries out burning disposal, while the organic waste sub-elected is directly subjected to pulp processing using pulp degraded equipment, and will
Organic waste after pulp processing is discharged into degraded pond nearby.
Carried out when dividing living area by 4000-7000 resident family for a standard, wherein, cell：4000-5000 families
For a standard living area, residents from villages and towns：5000-7000 families are a standard living area, rural area：5000-7000 families are
One standard living area.
As shown in Figure 1, Figure 2, Figure 3 shows, a kind of burning facility, including CIU 1, waste heat boiler 2, gas cleaning processing system
System 3.
Wherein, CIU 1 includes the first combustion chamber 110, the second combustion chamber 120, blast apparatus 130, the first combustor
140th, the second combustor 150, the 3rd combustor 160, the exhaust opening of the first combustion chamber 110 pass through flue and the second combustion chamber 120
Smoke inlet be connected, the exhaust opening of the second combustion chamber 120 is connected by flue with the air inlet of waste heat boiler 2.Blast apparatus 130
For the air feed into the first combustion chamber 110, the second combustion chamber 120, wherein, blast apparatus 130 is air blower, and air blower is using low
Noise Middle pressure draught fan, voltage is 220V, and blast is 2300Pa, and power is 0.75KW.
First combustor 140 and the second combustor 150 are arranged on the first combustion chamber 110, and the 3rd combustor 160 is set
On the second combustion chamber 120, wherein, the first combustor 140 has igniting, flame-out and decompression automatic protection functions using be
Light diesel fuel combustor, the second combustor 150 has igniting, the light diesel fuel burning of flame-out and decompression automatic protection functions using be
Machine, the 3rd combustor 160 is lighted a fire using having of being, the light diesel fuel combustor of flame-out and decompression automatic protection functions.In addition, burning
It is the first combustor 140, the second combustor 150, the fuel tank of the fuel feeding of the 3rd combustor 160 that burning system 1, which also includes being used for,.
The body of heater internal diameter of first combustion chamber 110 is 900mm, is highly 1.8m, and the shell of the first combustion chamber 110 is carbon steel knot
Structure, the liner of the first combustion chamber 110 includes heat-insulation layer and flame retardant coating, and flame retardant coating uses disposal pouring technique.Second burning
The cross-sectional area of the body of heater of room 120 is 0.64 ㎡, is highly 1.8m, and the shell of the second combustion chamber 120 is carbon steel structure, liner
Including heat-insulation layer and flame retardant coating, wherein, flame retardant coating uses disposal pouring technique.
Offered on the first combustion chamber 110 and the position of charge door is being set provided with use on charge door, the first combustion chamber 110
In the gallery ports 111 of sealing charge door, the rotation of one end of gallery ports 111 and the first combustion chamber 110 is connected, gallery ports 111 it is another
One end is flexibly connected with the first combustion chamber 110.
Offered in the lower section of the first combustion chamber 110 is setting the position of ash hole to set on ash hole, the first combustion chamber 110
There is the ashpit 112 for sealing grey mouth, one end of ashpit 112 rotates with the first combustion chamber 110 and is connected, ashpit 112
The other end be flexibly connected with the first combustion chamber 110.
Waste heat boiler 2 is provided with cooling water inlet and hot water outlet, wherein, cooling water inlet is located at the lower section of waste heat boiler 2, heat
Water out is located at the top of waste heat boiler 2, and the flue gas entered in waste heat boiler 2 can be realized cold in waste heat boiler 2 with cold water
Heat exchange, that is, discharge heat.The shell of waste heat boiler 2 is made up of carbon steel, and the inner bag of waste heat boiler 2 is made of stainless steel.
System for cleaning fume 3 includes one-level spray dust device 310, the second-class impact dust settler 320, smoke eliminator
330th, lye pump, alkali lye circulating sedimentation tank 350 and blower unit 360.
The exhaust outlet of waste heat boiler 2 is connected by flue with the air inlet of one-level spray dust device 310.The second-class impact drops
Dirt device 320 is arranged on alkali lye circulating sedimentation tank 350, and the smoke inlet and alkali lye circulating sedimentation tank of the second-class impact dust settler 320
350 are connected.Lye pump is used to the alkali lye in alkali lye circulating sedimentation tank 350 being supplied to progress in one-level spray dust device 310
Spray, so that alkali lye is fully contacted with flue gas in one-level spray dust device 310, effectively eliminates the sour gas in flue gas
Body, prevents corrosion and environmental pollution of the pickling flue gas to follow-up flue.The leakage fluid dram of one-level spray dust device 310 is circulated with alkali lye
Sedimentation basin 350 is connected, and the alkali lye after so spraying is flowed directly back into alkali lye circulating sedimentation tank 350, and profit is circulated after precipitation
With non-secondary pollution.One-level spray dust device 310 is made of 316L stainless steels.The exhaust opening of one-level spray dust device 310 leads to
The smoke inlet that blower unit 360 is crossed with alkali lye circulating sedimentation tank 350 is connected.Smoke inlet on alkali lye circulating sedimentation tank 350 is located at
Below the metal line of the alkali lye circulating sedimentation tank 350, i.e., the flue gas that blower unit 360 is discharged in alkali lye circulating sedimentation tank 350 is
It is discharged into below metal line, such flue gas can be contacted with alkali lye water-bath type in alkali lye circulating sedimentation tank 350, and then thoroughly eliminate cigarette
Flue dust and sour gas in gas.The exhaust opening of the second-class impact dust settler 320 is connected with the air inlet of smoke eliminator 330.
Smoke eliminator 330 includes air inducing pipeline 331, clarifier 332, blower fan 333, blast cap 334.Air inducing pipeline 331
One end be connected with the exhaust opening of the second-class impact dust settler 320, the other end of air inducing pipeline 331 and the air inlet of clarifier 332
Mouth is connected, and the exhaust outlet of clarifier 332 is connected by exhaust duct with the air inlet of blower fan 333, and blast cap 334 is arranged on wind
On the exhaust outlet of machine 333.Have necessarily between the air inlet of air inducing pipeline 331 and the exhaust opening of the second-class impact dust settler 320
Difference in height, both differences are 35cm to 50cm, so can be effectively to entering air inducing pipeline by the second-class impact dust settler 320
Flue gas in 331 is cooled, and effectively extends the service life of whole equipment.
Blower unit 360 includes air-introduced machine 361, the first induced duct 362, the second induced duct, one end of the first induced duct 362
It is connected with the exhaust opening of one-level spray dust device 310, the other end of the first induced duct 362 and the air inlet phase of air-introduced machine 361
Connection；One end of second induced duct is connected with the smoke inlet on alkali lye circulating sedimentation tank 350, and the other end of the second induced duct is with drawing
The exhaust outlet of blower fan 361 is connected, and air-introduced machine 361 is low noise Middle pressure draught fan, and power is 1.5KW.
Burning facility also include control cabinet 4, control cabinet 4 include controller and be electrically connected with the controller control panel,
Alarm, power-off protection apparatus, safety guard.It is provided with the first combustion chamber 110 for measuring the first combustion chamber 110
In-furnace temperature the first temperature measuring equipment, be provided with the second combustion chamber 120 for measure the second combustion chamber 120 stove in temperature
Second temperature measuring equipment of degree.The signal input part electricity that the signal output part of first temperature measuring equipment passes through data line and controller
Connection.The signal output part of second temperature measuring equipment is electrically connected by data line with the signal input part of controller.Lye pump
Signal input part electrically connected by data line with the signal output part of controller.The signal input of first combustor 140
End is electrically connected by data line with the signal output part of controller.The signal input part of second combustor 150 passes through data
Transmission line is electrically connected with the signal output part of controller.The signal input part of 3rd combustor 160 passes through data line and control
The signal output part electrical connection of device processed.The signal input part of blast apparatus 130 is defeated by the signal of data line and controller
Go out end electrical connection.The signal input part of air-introduced machine 361 is electrically connected by data line with the signal output part of controller.Purification
The signal input part of device 332 is electrically connected by data line with the signal output part of controller.The signal input part of blower fan 333
Electrically connected by data line with the signal output part of controller.
In addition, every is connected to be provided with data line with control cabinet 4 and is connected protection device, it to avoid Lou
Electricity, when relative temperature is more than 85%, electrical circuit insulaion resistance is not less than 2M Ω, and has ground wire transmission electric leakage power supply, number
According to there is metal hose protection outside transmission line.Before burning facility is out of service, burning facility has to the first combustion chamber 110, second
The detection of the cooling program of combustion chamber 120, when making the first combustion chamber 110, the temperature drop of the second combustion chamber 120 to design temperature, burns
Burn equipment and stop all operations.The detection of cooling program is carried out by the first temperature measuring equipment and the second temperature measuring equipment.In the first burning
When machine 140, the second combustor 150 or the 3rd combustor 160 light a fire abnormal after starting, controller can control burning facility to stop
Operation.
Control cabinet 4 not only carries out closed-loop control to the ignition temperature of the first combustion chamber 110, the second combustion chamber 120, and
Also closed-loop control is carried out to their oxygen-supplying amount, the control of wherein oxygen-supplying amount is the air by controlling blast apparatus 130 to blast
Amount complete, coordinate the control between them, making the control of the whole control result and each process of burning facility can reach
It is required that, whole burning facility is in closed-loop control.
When the calorific value that the first temperature measuring equipment detects combustiblerefuse in the first combustion chamber 110 is higher than average value, control cabinet 4
The first combustor 140, the second combustor 150 is controlled to play igniting peace weighing apparatus furnace temperature.When the second temperature measuring equipment detects
When the calorific value of flue gas is higher than average value in two combustion chambers 120, control cabinet 4 controls the 3rd combustor 160 to play igniting peace weighing apparatus stove
Temperature effect.Control cabinet 4 ensure that to different materials, the optimal control in different combustion processes, so as to ensure that material
Abundant burning and exclude flue gas quality.For the first combustor 140, the second combustor 150, the 3rd combustor 160 it is excellent
Change control and also reduce the first combustor 140, the second combustor 150, the use oil mass of the 3rd combustor 160, make operating cost big
Width is reduced.
Combustiblerefuse carries out comprising the following steps that for burning disposal using burning facility：
S101, in living area directly the house refuse produced by the living area is carried out integrating sorting, and will divided
The combustiblerefuse selected is burned using the CIU 1 in the equipment in the living area, after burning
Flue gas is drained into waste heat boiler 2 by flue；
After S102, flue gas are entered in waste heat boiler 2, cold and hot exchange is carried out in waste heat boiler 2, heat, release is discharged
Flue gas after heat is entered in one-level spray dust device 310 by flue；
Alkali lye in alkali lye circulating sedimentation tank 350 is supplied in one-level spray dust device 310 by S103, lye pump, and right
The flue gas entered in one-level spray dust device 310 is sprayed；
S104, the flue gas after spray process are entered in alkali lye circulating sedimentation tank 350 by blower unit 360, and with
Alkali lye water-bath type contact in alkali lye circulating sedimentation tank 350, the fully flue gas after washing enter the second-class impact dust settler 320
It is interior, then be drained into by the second-class impact dust settler 320 in smoke eliminator 330；
S105,330 pairs of flue gases entered in it of smoke eliminator are purified, and low-altitude discharged is to big after the completion of purification
In gas.
Wherein, comprising the following steps that when being burned using CIU 1：
S1011, charge door of the combustiblerefuse sub-elected on the first combustion chamber 110 be added to the first combustion chamber 110
It is interior, gallery ports 111 are then shut off, then by flammable in the first combustor 140,150 pair of first combustion chamber 110 of the second combustor
Rubbish carries out igniting burning, wherein, the temperature of the first combustion chamber 110 operationally is 300 DEG C to 500 DEG C；
S1012, combustiblerefuse flue gas produced after being burnt in the first combustion chamber 110 enter the second combustion by flue
Room 120 is burnt, is lighted a fire using 160 pairs of flue gases entered in the second combustion chamber 120 of the 3rd combustor, allows flue gas to burn away
Decompose, wherein, the temperature of the second combustion chamber 120 operationally is 900 DEG C to 1100 DEG C；
S1013, treat that the abundant combustion decomposition relief flue gas of flue gas is entered in waste heat boiler 2 by flue.
After whole equipment installation, overall floor space is 30-50m2, the disposal ability of the first combustion chamber 110 is
100-150kg/h, the disposal ability of the second combustion chamber 120 is 100-150kg/h, the first combustion chamber 110 and the second combustion chamber 120
It is operationally negative pressure state, so facilitates the flowing of flue gas, the daily run time of whole equipment is 8 hours, and it handles rubbish
Rubbish amount is 1.2T-1.5T, is burned by quantitative timing, produced very small amount recirculated water when whole equipment is run, and can accomplish every
30kg recirculated waters need to be only changed within 100 days, waste water (recirculated water) is directly discharged into degraded pond (septic tank), and recirculated water is mainly by alkali lye
Circulating sedimentation tank 350 is produced.Daily waste heat boiler 2 can go out 85 DEG C of hot water 2.4T-3.5T.Combustiblerefuse is burned than being (5000-
8000):1。
After being burned using house refuse living area tupe to combustiblerefuse, the technical indicator of test is as follows：
| Project | Test result | National standard limit |
| Burn furnace temperature DEG C | 900~1200 | ≥850 |
| Gas residence time s | 2.05 | ≥2 |
| Dust concentration mg/m3 | 66.6 | 100 |
| Nitrogen oxides mg/m3 | 24 | 500 |
| Hydrogen chloride mg/m3 | 19.7 | 100 |
| Hydrogen fluoride mg/m3 | Do not detect | 9 |
| Sulfur dioxide mg/m3 | 50.4 | 400 |
| O in flue gas2Concentration % | 10 | 6~10 |
| CO concentration in flue gas mg/m3 | 7.2 | ≤100 |
Wherein, O in the dust concentration, nitrogen oxides, hydrogen chloride, hydrogen fluoride, sulfur dioxide, flue gas2In concentration, flue gas
CO concentration is the flue gas finally discharged surveyed.
As shown in figure 4, a kind of pulp degraded equipment, including movable carrier, shear 5, grinding mechanism 6, transfer tank
7。
Transfer tank 7 is arranged on movable carrier.Shear 5 is arranged on transfer tank 7, the discharge gate of shear 5
With the intracavity inter-connection of transfer tank 7.Grinding mechanism 6 is arranged on transfer tank 7, and the discharge gate of grinding mechanism 6 is interior with transfer tank 7
Chamber is connected.Transfer tank 7 is provided with the blow-off pipe 710 with the intracavity inter-connection of transfer tank 7.
In the present embodiment, the bottom wall of transfer tank 7 is in circular arc, and one end of blow-off pipe 710 and the bottom of transfer tank 7
The minimum point of circular arc is connected.
Facilitate the dredge pump 720 that the organic waste in transfer tank 7 is discharged in addition, being provided with blow-off pipe 710.
Organic waste living area pulp degraded equipment also includes the workbench being arranged on movable carrier, and work is flat
Platform mainly facilitates movable carrier above and below operating personnel, and facilitates operating personnel to be delivered into shear 5, grinding mechanism 6
Organic waste.
Organic waste living area pulp degraded equipment also includes the cleaning device being arranged on movable carrier, cleaning dress
Put and be mainly used in cleaning shear 5, grinding mechanism 6, transfer tank 7 in time, it is to avoid repeated contamination, keep organic waste
Living area pulp degraded equipment it is clean and tidy.
Comprising the following steps that for pulp processing is carried out using pulp degraded equipment：
S201, in living area the house refuse in the living area is carried out integrating sorting, and by having for sorting out
Cut using the shear 5 or grinding mechanism 6 in organic waste living area pulp degraded equipment at machine rubbish directly scene
Cut or grind so that organic waste granulates, and obtained granular organic waste is subjected to interim storage by transfer tank 7；
S202, the organic waste in transfer tank 7 are reached after certain amount of storage, and the organic waste in transfer tank 7 is discharged into
Carried out in degraded pond in living area after natural degradation, degraded some cycles, form stable organic fertilizer.
Wherein, when the organic waste in transfer tank 7 is discharged into degraded pond, floss hole needs to extend into degraded pond
Under liquid level at 8-10cm.
Although embodiments of the invention have been shown and described above, it is to be understood that above-described embodiment is example
Property, it is impossible to limitation of the present invention is interpreted as, one of ordinary skill in the art within the scope of the invention can be to above-mentioned
Embodiment is changed, changed, replacing and modification.
Claims (10)
1. a kind of house refuse living area tupe, it is characterised in that divide living area, and to each life marked off
The house refuse of the generation is carried out integrating sorting in region living, and the combustiblerefuse sub-elected is utilized and is arranged on the living area
Interior burning facility carries out burning disposal, while the organic waste sub-elected is directly carried out at pulp using pulp degraded equipment
Reason, and organic waste after pulp is handled is discharged into degraded pond nearby.
2. a kind of house refuse living area tupe according to claim 1, it is characterised in that dividing living area
Carried out during domain by 4000-7000 resident family for a standard.
3. a kind of house refuse living area tupe according to claim 2, it is characterised in that the burning facility
The amount of day incineration of combustible rubbish is (1.2T-1.5T)/8h.
4. a kind of house refuse living area tupe according to claim 1, it is characterised in that to house refuse
When progress integrates sorting, recyclable rubbish is also sub-elected, and it is recycled.
5. a kind of house refuse living area tupe according to claim 1, it is characterised in that the burning facility
Including CIU (1), waste heat boiler (2), system for cleaning fume (3)；The exhaust opening and waste heat of the CIU (1)
The air inlet of boiler (2) is connected；The system for cleaning fume (3) include one-level spray dust device (310), lye pump and
Alkali lye circulating sedimentation tank (350), the exhaust outlet of the waste heat boiler (2) is connected with the air inlet of one-level spray dust device (310)
Connect, the lye pump is used to the alkali lye in alkali lye circulating sedimentation tank (350) being supplied to progress in one-level spray dust device (310)
Spray, the leakage fluid dram of one-level spray dust device (310) is connected with alkali lye circulating sedimentation tank (350).
6. a kind of house refuse living area tupe according to claim 5, it is characterised in that the gas cleaning
Processing system (3) also includes the second-class impact dust settler (320), blower unit (360), and the second-class impact dust settler (320) sets
Put on alkali lye circulating sedimentation tank (350), smoke inlet and the alkali lye circulating sedimentation tank of the second-class impact dust settler (320)
(350) it is connected, the exhaust opening of one-level spray dust device (310) passes through blower unit (360) and alkali lye circulating sedimentation tank
(350) smoke inlet is connected, and the smoke inlet on the alkali lye circulating sedimentation tank (350) is located at the alkali lye circulating sedimentation tank (350)
Metal line below.
7. a kind of house refuse living area tupe according to claim 6, it is characterised in that the gas cleaning
Processing system (3) also includes smoke eliminator (330), the exhaust opening of the second-class impact dust settler (320) and gas cleaning
The air inlet of device (330) is connected.
8. a kind of house refuse living area tupe according to claim 7, it is characterised in that combustiblerefuse is utilized
Burning facility carries out comprising the following steps that for burning disposal：
S101, the combustiblerefuse sub-elected burned using CIU (1), the flue gas after burning is drained into by flue
In waste heat boiler (2)；
After S102, flue gas are entered in waste heat boiler (2), cold and hot exchange is carried out in waste heat boiler (2), heat, release is discharged
Flue gas after heat is entered in one-level spray dust device (310) by flue；
Alkali lye in alkali lye circulating sedimentation tank (350) is supplied in one-level spray dust device (310) by S103, lye pump, and right
The flue gas entered in one-level spray dust device (310) is sprayed；
S104, the flue gas after spray process are entered in alkali lye circulating sedimentation tank (350) by blower unit (360), and with
Alkali lye water-bath type contact in alkali lye circulating sedimentation tank (350), the fully flue gas after washing enter the second-class impact dust settler
(320) in, then it is drained into by the second-class impact dust settler (320) in smoke eliminator (330)；
S105, smoke eliminator (330) are purified to the flue gas entered in it, and low-altitude discharged is to air after the completion of purification
In.
9. a kind of house refuse living area tupe according to claim 1, it is characterised in that the pulp degraded
Equipment includes movable carrier, shear (5), grinding mechanism (6), transfer tank (7)；The transfer tank (7) is arranged on removable
On dynamic load body；The shear (5) is arranged on transfer tank (7), discharge gate and the transfer tank (7) of the shear (5)
Intracavity inter-connection；The grinding mechanism (6) is arranged on transfer tank (7), discharge gate and the transfer tank of the grinding mechanism (6)
(7) intracavity inter-connection；The transfer tank (7) is provided with the blow-off pipe (710) with the intracavity inter-connection of transfer tank (7).
10. a kind of house refuse living area tupe according to claim 9, it is characterised in that utilize pulp drop
Solution equipment carries out comprising the following steps that for pulp processing：
S201, organic waste is sheared or ground using shear (5) or grinding mechanism (6) granulate, and by obtained grain
Shape organic waste carries out interim storage by transfer tank (7).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710547527.XA CN107270300A (en) | 2017-07-06 | 2017-07-06 | A kind of house refuse living area tupe |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710547527.XA CN107270300A (en) | 2017-07-06 | 2017-07-06 | A kind of house refuse living area tupe |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107270300A true CN107270300A (en) | 2017-10-20 |
Family
ID=60071750
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710547527.XA Pending CN107270300A (en) | 2017-07-06 | 2017-07-06 | A kind of house refuse living area tupe |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107270300A (en) |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102261661A (en) * | 2011-06-22 | 2011-11-30 | 宜昌市九天环保科技有限公司 | House refuse incineration boiler |
| CN102901107A (en) * | 2011-08-29 | 2013-01-30 | 河南省澳斯迪环保机械有限责任公司 | Smoke processing device matched with household garbage incinerator |
-
2017
- 2017-07-06 CN CN201710547527.XA patent/CN107270300A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102261661A (en) * | 2011-06-22 | 2011-11-30 | 宜昌市九天环保科技有限公司 | House refuse incineration boiler |
| CN102901107A (en) * | 2011-08-29 | 2013-01-30 | 河南省澳斯迪环保机械有限责任公司 | Smoke processing device matched with household garbage incinerator |
Non-Patent Citations (1)
| Title |
|---|
| 付灿华: "深圳：餐厨垃圾分区处理"盐田模式"", 《环卫科技网》 * |
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