City rubbish from cooking harmless treatment device
Technical field
The utility model belongs to technical field of waste treatment, specifically, is related to a kind of kitchen refuse processing apparatus.
Background technology
In the face of increasingly serious environmental problem and energy crisis, energy-saving and emission-reduction are all being advocated energetically in the whole world.It is especially right
For the city rubbish from cooking for easily causing environmental pollution and therewith the rubbish from cooking process of the generation power consumption of association, how
Energy-saving and emission-reduction transformation is carried out, those skilled in the art's problem demanding prompt solution is had become.
Include landfill, compost and burning currently for the processing mode of rubbish from cooking.Wherein, the effect of landfill is very slow, account for
Ground is also wide, easily produce secondary pollution to underground water.It is organic fertilizer that compost is rubbish from cooking fermentation, but this mode need to
The time wanted is longer, causes the efficiency comparison of garbage disposal low.In addition, although rubbish from cooking is heated by someone, with quickening
Garbage decomposition, but this mode not only can be caused power consumption high because of heating to large-scale rubbish from cooking, and in kitchen
It is unfavorable in the case that remaining rubbish temperature is too high that rubbish fermentation is organic fertilizer on the contrary.And the mode of burning rubbish from cooking is not only dirty
Dye air, and invest larger.
A kind of refuse disposal system as disclosed in Chinese patent application 201310675228.6, which is included at garbage dewatering
Reason equipment, garbage sorting equipment and incinerator, wherein, it is multiple that garbage dewatering processing equipment includes that distribution has thereon
The cylinder of apopore, in cylinder and it is provided with the airduct of multiple air outlets towards apopore, connection drum inlet and enters
Material device and the blower fan of connection airduct one end, incinerator include feed hopper at the top of body of heater, successively staggeredly pacify
Downward-sloping and per layer the lower end being mounted in body of heater is located at next layer of upper end rubbish loading plate, the position of multiple through holes that gather
In the combustion chamber of lower portion of furnace body and the exhanst gas outlet device of upper of furnace body side is arranged on, in organic matter rubbish via multiple rubbish
During rubbish loading plate glides, the heat that combustion chambers burn rubbish is produced organic matter rubbish successively to carrying on rubbish loading plate
Toasted, residual moisture in rubbish is dried, the rubbish for slipping down to combustion chamber is quickly burned.However, the patent is disclosed
Refuse disposal system there is following or deficiency:(1), simply simply rubbish is burned, burning is not disclosed
Garbage disposal situation afterwards;(2) waste incineration easily produces secondary pollution;(3) no reasonable recycling garbage energy, it is impossible to
Realize the effect of energy-conserving and environment-protective.
And for example a kind of kitchen, rubbish from cooking handling process and its place disclosed in Chinese patent application 201510168637.6
The mixture of kitchen, rubbish from cooking is put in pretreatment pulverizer to enter Jing after the sorting of automatic sorting platform by reason system, the technique again
Row is crushed, and the oil water mixture that the liquid phase mixture and size-reduced machine of Jing automatic sorting platforms are separated enters water-oil separating
In equipment, water-oil separating is carried out, the water separated from oily water separating equipment is mutually needed through filtration treatment, is finally poured to live
The form of filling water is discharged, and oil phase carries out bio-separation into bio-separation equipment, is finally made bio-oil;Preprocessed powder
During kitchen, rubbish from cooking after broken machine crushing is as source of nutrition input polypide breeding production line, the polypide of saprogen is carried out
Cultivation, the polypide that grows up carry out drying and processing in dryer, are then processed into the feeds such as poultry, fish, and polypide discards
Thing and residue carry out degradation treatment, the material Jing after degraded, and a part is used for generating electricity in the form of biomass fuel, another portion
The packing outward transport in the form of fertilizer is divided to use.However, processing system disclosed in the patent haves the shortcomings that following or deficiency:
(1), processing cost is high, is related to substantial amounts of filtering separation device;(2) degradation time is very long, and treatment effeciency is low;(3) following process
Process is numerous and diverse.
For another example a kind of restaurant garbage treating system disclosed in Chinese patent application 201510404242.1, including:Air heat
Source pump, is heated to liquid and with liquid as heat-conducting medium;Solar thermal collector, with heat pipe, is produced by solar energy
Heat is heated to the liquid in which;Heating jacket, with inner housing and shell body, the inner chamber that inner housing is formed is used for holding
Changing food waste, forms exocoel between inner housing and shell body, the liquid that the outer wall around inner housing spirals is provided with exocoel
Passage, heating jacket are provided with the first temperature sensor for stretching into inner chamber;Liquid line, connection air heat source pump, solar energy heating
Device and heating jacket;Control device, controls the opening and closing of each magnetic valve on air heat source pump and liquid line.However,
Restaurant garbage treating system disclosed in the patent haves the shortcomings that following or deficiency:(1) the extraneous heat energy that provides is needed to enter rubbish
Row heating simultaneously makes inner chamber remain the temperature of suitable microbial reproduction, generates greater energy consumption;(2), garbage decomposition is fermented into
Long for organic fertilizer process time, treatment effeciency is low;(5) the container floor space of decomposing and fermenting rubbish is big.
Therefore it provides it is a kind of can either effective process rubbish from cooking produce pollution problem can make full use of food waste rubbish again
The city rubbish from cooking harmless treatment device of rubbish self energy becomes urgent problem in the industry.
The content of the invention
The purpose of this utility model is to provide a kind of city rubbish from cooking harmless treatment device, after which can be using drying
Rubbish from cooking as biomass gasifying furnace fuel, and using biomass gasifying furnace produce biological fuel gas and drying kitchen
The flue gas that remaining rubbish is produced realizes the recycling of energy as the energy source for drying rubbish from cooking again.
To achieve these goals, the utility model provides a kind of city rubbish from cooking harmless treatment device, including:
Disintegrating machine, the conveyer belt for transmitting rubbish particle, drying unit and the life of rubbish particle are formed for crushing rubbish from cooking
Gasification substance stove, wherein, drying unit includes revolving drum and the combustion chamber being located at turn around below cylinder, and revolving drum is provided with for taking up
The revolution inner chamber of rubbish particle, the one end for turning round inner chamber are provided with feeding port, and the other end for turning round inner chamber is provided with feed opening and exhaust
Mouthful, feeding port is connected with conveyer belt, and feed opening is connected with biomass gasifying furnace, and exhaust outlet will turn round the waste gas row produced in inner chamber
Go out to chimney, combustion chamber includes at least three nozzles being arranged at intervals on the diapire of combustion chamber, and at least three nozzles are used for will combustion
Gas and combustion-supporting gas blowout are incident upon combustion chambers burn heat release to dry the rubbish particle turned round in inner chamber of revolving drum above;With
And biomass gasifying furnace is provided with the outlet of air intake, rubbish from cooking particle entrance and biological fuel gas, rubbish from cooking particle enters
Mouthful connect with the feed opening of revolving drum by pipeline, biological fuel gas export by burning line be connected with least three nozzles with
By biomass fuel gas jet to Indoor Combustion heat release of burning.
Selectively, revolving drum is obliquely installed, and revolving drum range of tilt angles with respect to the horizontal plane is 15 degree~30 degree.
Selectively, drying unit also includes drier, and drier includes main unit for dryer, and the inside of main unit for dryer is empty
Between by the ventilative board for being densely covered with multiple through holes be divided into positioned at bottom the dry section for transmitting hot blast and be located at middle and upper part
Stirring promote area, stirring promote area in be provided with least one along horizontal axis rotation auger pushing meanss, wherein, do
The roof of dry device body is provided with the feeding mouth being connected by pipeline with the feed opening of revolving drum, and the side wall of dry section is provided with hot blast
Entrance, promotes the side wall in area to be provided with discharging opening in stirring above ventilative board, and discharging opening passes through pipeline and biomass gasifying furnace
Rubbish from cooking particle entrance be connected so that dried rubbish particle to be gasified as biomass material.
Selectively, the side wall of combustion chamber is connected with the first flue gas exhausting pipe line, the first flue gas exhausting pipe line and first
The smoke inlet of blender is connected, and the air intake of the first blender is connected to the first air-introduced machine, the mixing of the first blender
Gas exports the warm-air supply being mixed to form with the heat smoke of spontaneous combustion in future room and air that is connected with the hot-wind inlet of dry section
To dry section.
Preferably, the heat smoke of 800 degrees Celsius in the first flue gas exhausting pipe line~900 degrees Celsius with from the first air inducing
The warm-air supply that the normal temperature air of machine forms 300 degrees Celsius~400 degrees Celsius after mixing in the first blender is to dry section.
Selectively, the roof of drier is also associated with the second flue gas exhausting pipe line, the second flue gas exhausting pipe line and second
The smoke inlet of blender is connected, and the exhaust gas entrance of the second blender is connected with the exhaust outlet of revolving drum by pipeline, the
The exhanst gas outlet of two blenders is connected with chimney by flue.
Selectively, the downstream connection in flue has smoke backflow pipeline, smoke backflow pipeline and at least three sprays
Mouth is connected the partial fume in flue is back at least three nozzles for combustion-supporting.
Preferably, smoke backflow pipeline is back at least three nozzles for combustion-supporting by the 40%~50% of amount of flue gas emission.
Preferably, the flue-gas temperature in smoke backflow pipeline is 150 degrees Celsius~200 degrees Celsius.
On the flue of neighbouring chimney it is provided with purifying and dedusting device to remove the dirt slag in flue gas.
Selectively, each auger pushing means includes the auger bar being placed in stirring promotion area and wears
The horizontal drive shaft that stirring promotes area side wall to be connected with auger bar is crossed, wherein, the outer wall of auger bar surround and sets
Propulsion spiral is equipped with so that the rubbish particle in revolving drum is acted in the hot blast of dry section with the rotation of auger bar
Lower drying is simultaneously pushed to discharge outlet.
Selectively, stirring promotes at least three auger pushing meanss of vertical equi-spaced apart arrangement in area.
Preferably, the side of each horizontal drive shaft is connected to drive horizontal drive shaft simultaneously by belt with driving means
Auger bar is driven to rotate.
Selectively, the roof of biomass gasifying furnace is additionally provided with supplementary biomass feed inlet to mend in biomass gasifying furnace
Biomass fuel is filled, an end wall of biomass gasifying furnace is provided with steam entry and makees so that water vapour is supplemented in biomass gasifying furnace
For gasifying agent.
Preferably, the air intake of biomass gasifying furnace is connected with to biomass gasifying furnace with the second air-introduced machine by pipeline
Middle introducing air.
Preferably, it is provided with the 3rd air-introduced machine between the second blender and purifying and dedusting device on flue to be beneficial to
Flue gas is expelled in flue from revolving drum and drier.
Preferably, burning line is provided with the 4th air-introduced machine biological fuel gas to be introduced at least three nozzles.
The beneficial effects of the utility model are:(1), using the rubbish from cooking particle after dried process as biomass gasifying furnace
Biomass fuel, the biological fuel gas of generation originate as combustion chamber combustion gas, are re-used for the drying and processing of rubbish from cooking, real
Show recycling for energy, reach the purpose of energy-saving and emission-reduction;(2) account for the drying rubbish from cooking generation of total amount 40~50%
It is combustion-supporting that waste gas and smoke backflow are delivered to nozzle, not only increases efficiency of combustion, and effectively reduces exhaust emission;(3) it is right
Rubbish from cooking carries out a large amount of steam that first time drying process can be discharged in rubbish, and carrying out second drying process then can be by rubbish
Rubbish particle is prepared into the particulate material for being suitable to biomass gasifying furnace, and drying process twice can be dried in rubbish for a full due
Moisture is to use as biomass fuel;(4) use of purifying and dedusting equipment, greatly reduces in the final flue gas of discharge
Dirt slag, carbon dioxide, the content of nitrogen oxides, are effectively protected environment.
Description of the drawings
Fig. 1 shows the organigram of rubbish from cooking harmless treatment device in city of the present utility model.
Specific embodiment
Fig. 1 is refer to, according to a kind of non-limiting embodiment of the present utility model, city rubbish from cooking harmless treatment
Device includes:Disintegrating machine 100, conveyer belt 200, revolving drum 300, combustion chamber 400 and biomass gasifying furnace 500.
Disintegrating machine 100 is formed rubbish from cooking broken after rubbish particle, and these rubbish particles are just sent to by conveyer belt 200
Revolving drum 300 is dried.Wherein, revolving drum 300 is provided with revolution inner chamber 310, and the one end for turning round inner chamber 310 is provided with feeding port
320, feeding port 320 is connected with conveyer belt 200, so as to the rubbish particle that transmission comes is taken up in revolution inner chamber 310, in revolution
The other end in chamber 310 is provided with feed opening 320 and exhaust outlet 330, and exhaust outlet 330 will turn round the waste gas discharge produced in inner chamber 310
To chimney 800.
Combustion chamber 400 includes three nozzles 410 being arranged at intervals on the diapire of combustion chamber.Biomass gasifying furnace 500 is provided with
Air intake 510, rubbish from cooking particle entrance 520 and biological fuel gas outlet 530, biological fuel gas outlet 530 is by combustion
Gas pipeline GL is connected with three nozzles 410, so as to by combustion heat release in biomass fuel gas jet to combustion chamber 400.
Used as a kind of alternative embodiments, revolving drum 300 inclines about 15 degree of settings, so not only beneficial to rubbish particle
Discharge, while the also discharge beneficial to waste gas.
As shown in figure 1, as another kind of alternative embodiments, through 300 dried rubbish particle of revolving drum by under
Material mouth 320 is emitted in drier 600.Wherein, drier 600 includes main unit for dryer (non-label), main unit for dryer it is interior
Portion space by the ventilative board 610 for being densely covered with multiple through holes be divided into positioned at bottom the dry section 620 for transmitting hot blast and
Stirring above dry section 620 promotes area 630, stirring to promote vertical equi-spaced apart in area 630 to arrange three around trunnion axis
The auger pushing meanss 640 of line rotation, wherein, the roof of main unit for dryer is provided with logical with the feed opening 320 of revolving drum 300
The feeding mouth 650 of piping connection, the side wall of dry section 620 are provided with hot-wind inlet 660, and stirring promotes the side wall in area 630
Bottom is provided with discharging opening 670, and discharging opening 670 is connected with the rubbish from cooking particle entrance 520 of biomass gasifying furnace 500 by pipeline
Connect, so as to the rubbish particle through redrying is gasified as biomass material.
In the non-limiting embodiment, auger pushing meanss 640 include that being placed in stirring promotes in area 630
Auger bar 641 and the horizontal drive shaft 642 being connected with auger bar 641 through stirring promotion 630 side wall of area,
The outer wall of auger bar 641 is surrounded with propulsion spiral (non-label), thus, the rubbish particle in revolving drum 300
Just under the hot blast effect of dry section 620 dry and be pushed at discharging opening 670 with the rotation of auger bar 641.
As shown in figure 1, used as another alternative embodiments, the side wall of combustion chamber 400 is connected with the first flue gas row
Pipeline L1 is put, the first flue gas exhausting pipe line L1 is connected with the smoke inlet of the first blender M1, the air of the first blender M1
Entrance is connected to the first air-introduced machine F1, and the mixed gas outlet of the first blender M1 is connected with the hot-wind inlet 660 of dry section 620
Connect, thus, the heat smoke from about 800 degrees Celsius of combustion chamber 400 mixes shape with the normal temperature air from the first air-introduced machine F1
Into about 300 degrees Celsius of hot blast provide and carry out second garbage drying particle to dry section 620.
Additionally, the roof of drier 600 is also associated with the second flue gas exhausting pipe line L2, the second flue gas exhausting pipe line L2 and
The smoke inlet of two blender M2 is connected, and the exhaust gas entrance of the second blender M2 is by pipeline and the exhaust outlet of revolving drum 300
330 are connected, and the exhanst gas outlet of the second blender M2 is connected with chimney 800 by flue FL.Flue FL's
Downstream connection has a smoke backflow pipeline RL, and smoke backflow pipeline RL is by the 40%~50% of amount of flue gas emission smoke backflow to three
It is used at nozzle 410 combustion-supporting.
In the non-limiting embodiment shown in Fig. 1, purifying and dedusting is provided with the flue FL of neighbouring chimney 800
Device 700 realizes the effect of environmental protection such that it is able to remove the dirt slag in flue gas.
Used as another alternative embodiments, the roof of biomass gasifying furnace 500 is additionally provided with supplementary biomass feed inlet
550 to supplement biomass fuel in biomass gasifying furnace 500, and which can start use when rubbish particle calorific value is not enough.Additionally,
One end wall of biomass gasifying furnace 500 can be provided with steam entry 540 using into biomass gasifying furnace 500 supplement water vapour as
Gasifying agent.
As shown in figure 1, in the non-limiting embodiment, the air intake 510 of biomass gasifying furnace 500 passes through pipeline
It is connected with the second air-introduced machine F2, the 3rd air-introduced machine F3 is provided with flue FL, the 4th air inducing is provided with gas pipeline GL
Machine F4.
Thus, rubbish from cooking passes through combustion chamber 400 first at revolving drum 300 after being broken into rubbish particle
Heating, drying be dried through for the first time, then rubbish particle carries out second drying at drier 600, is emitted into biomass
Use as gasified raw material particle in gasification furnace 500, the biological fuel gas of generation are supplied in 410 conduct of burner of combustion chamber 400
Combustion gas is used.Meanwhile, out about 800 degrees Celsius of heat smoke of the discharge of combustion chamber 400 is provided to drying after being mixed with air
Use as dried medium at device 600, after being dried the flue gas that cooling is for about 150 degrees Celsius, account for the cigarette of volume total amount 40~50%
Gas is back to the burner 410 of combustion chamber 400 again and is used as combustion-supporting gas after being mixed with the exhaust of revolving drum 300, solid so as to realize
The Two-way Cycle of body particle and gas is used.
Although here has described preferred embodiment of the present utility model in detail, it is to be understood that the utility model is not
The concrete structure for describing in detail here and illustrating is confined to, can be by the case of without departing from spirit and scope of the present utility model
Those skilled in the art realizes other modifications and variant.