Summary of the invention
It is an object of the invention to overcome the deficiencies of the prior art and provide a kind of rubbish from cooking harmlessness disposing devices.
The present invention is achieved by the following technical solutions: a kind of rubbish from cooking harmlessness disposing device, it is characterised in that:
Including suffocating sterilization bucket, rotor filters pressing conveying device, waste liquid barrel, dry crushing device and incinerator, suffocating sterilization bucket is by fumigating
Inner cylinder and the collet being set on the outside of stifling inner cylinder form, and stifling hole are provided on the barrel of stifling inner cylinder, in suffocating sterilization bucket
Top be provided with feeding packing auger and smoked vapor outlet port, the bottom of suffocating sterilization bucket is provided with discharge port;Rotor filters pressing conveying
Device includes the jujube type compression chamber being obliquely installed and Le Luo triangle compression rotor, and compression rotor compresses in compression chamber around jujube type
Chamber center revolve while, compression rotor itself again rotation, in compression rotor motion process, three of them apex angle always with jujube type
Cavity wall contact is compressed, vertical feeder pipe, the top of feeder pipe and suffocating sterilization bucket are provided at the top of jujube type compression chamber
Discharge port connection, the bottom of jujube type compression chamber is provided with guide inclined tube, guide inclined tube is from jujube type compression chamber bottom along jujube
The tangential direction of type compression chamber side wall is stretched out, and filter press plate, the mesh on filter press plate are additionally provided on the side wall of jujube type compression chamber
Side wall through jujube type compression chamber is connected to waste liquid barrel, and filter press plate is set to feeder pipe along the downstream one of rotor rotation direction
Side, on jujube type compression chamber be provided with stifling tracheae in the middle part of the side wall that filter press plate is opposite, with the rotation of rotor, fumigate gas
Pipe is successively connected to guide inclined tube and feeder pipe;Dry crushing device main body is a tilting drying drum, the end of guide inclined tube
End is protruded into drying drum, and the angle between the axis and horizontal line of drying drum is less than the folder between guide inclined tube and horizontal line
Angle is provided with cloth wind shaft on the central axes of drying drum, and cloth wind shaft is the hollow tubular structures that hole is arranged in side wall,
It is provided with broken blade on cloth wind shaft, cloth wind shaft rotates under the drive of broken motor, cloth wind shaft and drying drum
Direction of rotation is opposite;The hopper of the discharge gate connection incinerator of drying drum;The hollow cavity of cloth wind shaft by air blower with
The flue of incinerator connects, and stifling tracheae is connected to the collet of suffocating sterilization bucket, smokes vapor outlet port and passes through air-introduced machine and incinerator
Burner hearth connection;Oil water separator is arranged in waste liquid barrel bottom, and the moisture outlet of oil water separator is connect with wastewater treatment equipment, oil
The oil outlet of separator is connected to by petroleum pipeline with the burner hearth of incinerator.
As further improvement of these options, helical blade, the leaf of helical blade are provided in suffocating sterilization bucket
Piece diameter is less than the radius of stifling inner cylinder, digs rubbish upwards when helical blade chooses to install driven by the motor, helical blade
Axis be the porose hollow tubular structures of wall surface, the inner cavity of the axis is connected to stifling tracheae.
As further improvement of these options, two end faces on the inside of drying drum are provided with microwave emitter.
As further improvement of these options, guide inclined tube is sleeve type structure, the tube wall setting hole of inner tube with
Outer tube connection, the both ends of inner tube are connected to respectively at jujube type compression chamber with drying drum, and one end of outer tube is connected to drying drum, separately
One end is towards the one side closed setting of jujube type compression chamber.
As further improvement of these options, it is provided with charging fire grate and blanking fire grate in incinerator, feeds fire grate
First section be located at hopper lower ends and protrude into burner hearth center, the first section of blanking fire grate is located at the underface end of charging fire grate end
Ash discharging hole is stretched to, the vertical range fed between fire grate and blanking fire grate is greater than the 2/5 of incinerator furnace width.
As further improvement of these options, spray material port is provided in incinerator, spray material port is obliquely installed upwards
In the underface of charging fire grate end, spray material port is connect with petroleum pipeline, flue gas set is provided on the outside of petroleum pipeline, flue gas set passes through
Thermal chimney is connected to stifling tracheae, and the end of flue gas set is protruded into burner hearth, and spray material port is located at flue gas set exit.
As further improvement of these options, air distribution outlet, the outlet of flue gas set are provided on the furnace wall of incinerator
It is protruded into burner hearth by air distribution outlet, the opening diameter of air distribution outlet is greater than the caliber of flue gas set outlet.
The present invention has the advantage that compared with prior art through stifling filters pressing separating most moisture and grease, so that
Garbage energy accesses quick drying, while the oil recovery in isolated waste liquid is participated in burning, and harmlessness disposing is more thorough
Bottom;Filters pressing is realized using rotor filters pressing conveying device and material conveys, while using the setting of stifling tracheae, being gone out to stifling
The air-flow of pulsed is provided in bacterium bucket and incinerator, help to promote heat transfer effect and upsets the effect of fire box temperature field distribution;Needle
To broken little particle rubbish, two-stage fire grate is set to shed fuel, promote conflagration and promotes fire box temperature.
Specific embodiment
It elaborates below to the embodiment of the present invention, the present embodiment carries out under the premise of the technical scheme of the present invention
Implement, the detailed implementation method and specific operation process are given, but protection scope of the present invention is not limited to following implementation
Example.
A kind of rubbish from cooking harmlessness disposing device, it is characterised in that: including suffocating sterilization bucket, rotor filters pressing conveying dress
It sets, waste liquid barrel 3, dry crushing device and incinerator 5, suffocating sterilization bucket is by stifling inner cylinder 13 and is set to stifling 13 outside of inner cylinder
Collet 12 form, be provided with stifling hole on the barrel of stifling inner cylinder 13, be provided with feeding packing auger at the top of suffocating sterilization bucket
11 and smoked vapor outlet port 16, the bottom of suffocating sterilization bucket is provided with discharge port;Rotor filters pressing conveying device includes being obliquely installed
Jujube type compression chamber 21 and Le Luo triangle compression rotor 22, (central axes of jujube type compression chamber 21 and the angle of horizontal direction are
45 °~80 °) compression rotor 22 in compression chamber around 21 center of jujube type compression chamber revolve while, compression rotor 22 itself again oneself
Turn, in 22 motion process of compression rotor, three of them apex angle is contacted with 21 inner wall of jujube type compression chamber always, in jujube type compression chamber 21
Top be provided with vertical feeder pipe 17, the top of feeder pipe 17 is connect with the discharge port of suffocating sterilization bucket, jujube type compress
The bottom of chamber 21 is provided with guide inclined tube 25, (axis of guide inclined tube 25 and horizontal angle are 10~30 °) guide inclined tube
25 stretch out from 21 bottom of jujube type compression chamber along the tangential direction of 21 side wall of jujube type compression chamber, on the side wall of jujube type compression chamber 21
It is additionally provided with filter press plate 23, the mesh on filter press plate 23 is connected to through the side wall of jujube type compression chamber 21 with waste liquid barrel 3, filter press plate 23
Feeder pipe 17 is set to along the downstream side of rotor rotation direction, the side wall opposite with filter press plate 23 on jujube type compression chamber 21
Middle part be provided with stifling tracheae 24, with the rotation of rotor, fumigate tracheae 24 and successively connect with guide inclined tube 25 and feeder pipe 17
It is logical;Dry crushing device main body is a tilting drying drum 4, and the end of guide inclined tube 25 is protruded into drying drum 4, dry to turn
Angle between the axis and horizontal line of cylinder 4 is less than the angle between guide inclined tube 25 and horizontal line, the central axes of drying drum 4
On be provided with cloth wind shaft 41, cloth wind shaft 41 is the hollow tubular structures that hole is arranged in side wall, is set on cloth wind shaft 41
It is equipped with broken blade 42, cloth wind shaft 41 rotates under the drive of broken motor, the rotation side of cloth wind shaft 41 and drying drum 4
To opposite;The discharge gate 43 of drying drum 4 connects the hopper 51 of incinerator 5;The hollow cavity of cloth wind shaft 41 passes through air blower
62 connect with the flue of incinerator 5, and stifling tracheae 24 is connected to the collet 12 of suffocating sterilization bucket, and smoked vapor outlet port 16 passes through air inducing
Machine 61 is connected to the burner hearth of incinerator 5;3 bottom of waste liquid barrel be arranged oil water separator 31, the moisture outlet of oil water separator 31 with
The oil outlet of wastewater treatment equipment connection, oil water separator 31 is connected to by petroleum pipeline 72 with the burner hearth of incinerator 5.
Due to not only containing large quantity of moisture in rubbish from cooking, there are also many greases to be mixed in wherein, directly burns without processing
It is difficult burning if burning sufficiently, will cause the secondary pollution to air.Rubbish from cooking is heated up by stifling means, makes grease
Partial liquefaction, while hot filters pressing make to be respectively processed again after being separated by solid-liquid separation.The rotor filters pressing conveying device that this programme uses utilizes
The special rotation mode of Lip river triangle is strangled, while realizing compression filtering and conveying, rubbish is entering jujube type pressure via feeder pipe 17
After contracting chamber 21, be pushed through on filter press plate 23 by compression rotor 22, at the same time, with compression rotor 22 and jujube type compression chamber 21 it
Between position variation, rubbish, which is compressed, is discharged to liquid portion in waste liquid barrel 3 by filter press plate 23, solid portion again by compression turn
Son 22 is pushed to be discharged into dry broken bucket by guide inclined tube 25, since liquid phase part has been extruded discharge, the rubbish of solid phase
It can be dried quickly in drying drum 4, and be broken into more little particle by counter-rotational broken blade 42, finally by arranging
Material mouth 43 is sent into incinerator 5 and is burned.It burns the high-temperature flue gas generated to be sent into drying drum 4 by air blower 62, with rubbish
Jujube type compression chamber 21 is directly entered by guide inclined tube 25 after heat exchange.Since feeder pipe 17 and guide inclined tube 25 are located at jujube type pressure
The both ends of contracting chamber 21, feeder pipe 17 is separated by rotor rotor always with guide inclined tube 25 during rotation, and stifling tracheae 24
Be set to the middle part of the side wall opposite with filter press plate 23, with the rotation of rotor, fumigate tracheae 24 successively with guide inclined tube 25 and
Feeder pipe 17 is connected to.By the rotation of rotor, guide inclined tube 25 is connected to stifling 24 intermittence of tracheae, and flue gas enters in pulse feature
In suffocating sterilization bucket.The gas of pulse feature in this way flows, and keeps flue gas elongated in the residence time of drying drum 4, in this way
Intermittent drying process can prevent the water loss of rubbish surface from forming very much hard shell fastly, so that the moisture inside granulated garbage obtains
Efficiently to scatter and disappear.The flue gas for being passed through the pulsed in suffocating sterilization bucket by fumigating tracheae 24 is distributed equal in stifling inner cylinder 13
Even, the ventilation of pulsed can prevent " bias current " phenomenon, so that placement and diabatic process are more equal at suffocating sterilization process
It is even.In the rotation process of compression rotor 22, feeder pipe 17 intermittent can be also connected to stifling tracheae 24, can be balanced in this way
Air pressure, so that blanking process is more smooth.It generates due to having pernicious gas during dry and stifling, finally will
Exhaust gas is passed through in burner hearth and realizes harmlessness disposing through pyrolytic;Grease, which is also finally passed through in burner hearth, in waste liquid barrel 3 participates in burning
Realize harmlessness disposing.
Helical blade 14 is provided in suffocating sterilization bucket, the blade diameter of helical blade 14 is less than the half of stifling inner cylinder 13
Diameter digs rubbish when helical blade 14 rotates driven by the motor upwards, and the axis 15 of helical blade 14 is that wall surface has hole
Hollow tubular structures, the inner cavity of the axis 15 is connected to stifling tracheae 24.In order to realize that suffocating sterilization gives full play in the process
The advantage of the flue gas of pulsed, needs to minimize the vapour lock in stifling inner cylinder 13, stirs rubbish upwards by helical blade 14
So that rubbish is more relaxed and comfortable, vapour lock can be substantially reduced, while being also passed into the flue gas of pulsed on axis 15, can be increased smoked
The treating capacity of steaming enhances treatment effect.
Two end faces of 4 inside of drying drum are provided with microwave emitter 44.Due to seldom containing gold in rubbish from cooking
Belong to ingredient, microwave emitter 44 can further be rapidly heated to rubbish, make it dry faster, after having raised simultaneously drying
The temperature of rubbish improves the feeding temperature of incinerator 5, the temperature of burner hearth is made to be further enhanced, and harmful substance is promoted to decompose.
Microwave emitter 44 also helps to improve the temperature of the flue gas flowed into guide inclined tube 25 simultaneously, improves the process of suffocating sterilization
Efficiency.
Guide inclined tube 25 is sleeve type structure, and the tube wall setting hole of inner tube 27 is connected to outer tube 26, the both ends of inner tube 27
It is connected to respectively with jujube type compression chamber 21 and drying drum 4, one end of outer tube 26 is connected to drying drum 4, and the other end is towards jujube type
The one side closed setting of compression chamber 21.Setting in this way, flue gas can be contacted from side with rubbish, increase flue gas and rubbish
On the one hand the way of contact in guide inclined tube 25 enhances heat exchange, on the other hand also reduces vapour lock, so that rubbish blanking is more
Add smooth.
Charging fire grate 52 and blanking fire grate 53 are provided in incinerator 5, the first section of charging fire grate 52 is located at 51 lower section of hopper
Burner hearth center is protruded into end, and ash discharging hole is stretched in the underface end that the first section of blanking fire grate 53 is located at charging 52 end of fire grate, into
Expect that the vertical range between fire grate 52 and blanking fire grate 53 is greater than the 2/5 of 5 furnace width of incinerator.Since rubbish is dry broken
Be broken into little particle in device, when accumulation inside gap can smaller, air cannot be introduced into, and burning is caused to delay
Slowly, by shedding between two-stage fire grate, the material of the burning in burner hearth center is shed and is come, it can be when very short
Interior realization after-flame effectively improves the temperature in burner hearth, realizes full combustion.
Be provided with spray material port 54 in incinerator 5, spray material port 54 be obliquely installed upwards in charging 52 end of fire grate just under
Side, spray material port 54 are connect with petroleum pipeline 72, and the outside of petroleum pipeline 72 is provided with flue gas set 71, and flue gas set 71 passes through thermal chimney 73
It is connected to stifling tracheae 24, the end of flue gas set 71 is protruded into burner hearth, and spray material port 54 is located at flue gas and covers 71 exits.Flue gas set 71
Effect be on the one hand to prevent grease from condensing during transportation, another aspect flue gas cover 71 exits pulsed it is fast
Fast air-flow can manufacture subnormal ambient, be sent into burner hearth after grease is drawn atomization from nozzle opening, spray into burner hearth to pulsed
The fuel of atomization.Spray material port 54 is set to the lower section of charging 52 end of fire grate, the flame gas formed after the ignited fuel ejected
Stream is directly contacted with the rubbish of whereabouts, is upset distribution of the rubbish in burner hearth, is spread out burner hearth fuel in disperse shape, entire furnace
Uniform distribution of temperature field in thorax will not generate nitrogen oxides or cause to burn because temperature is too low because individual sites temperature is excessively high
It is insufficient.
Air distribution outlet is provided on the furnace wall of incinerator 5, the outlet of flue gas set 71 is protruded into burner hearth by air distribution outlet, air distribution outlet
Opening diameter be greater than flue gas set 71 outlet calibers.Negative pressure caused by the air-flow that flue gas set 71 sprays can be inhaled from air distribution outlet
Enter combustion air, and the supplement rhythm of combustion air is consistent with the rhythm that grease sprays into is atomized.
The above is merely preferred embodiments of the present invention, be not intended to limit the invention, it is all in spirit of the invention and
Made any modifications, equivalent replacements, and improvements etc., should all be included in the protection scope of the present invention within principle.