CN205272396U - Plastic refuse handles assembly line - Google Patents

Abstract

The utility model discloses a plastic refuse handles assembly line, its technical scheme main points are: including belt cleaning device for plastic refuse's disinfection and isolation and deodorization are washd, and it includes the washing tank, the washing tank includes pan feeding end and discharge end, the discharge end is provided with the automatic feeding drier, it is provided with the conveyer that is used for carrying plastic refuse to the direction of discharge end in to hold along the pan feeding in the washing tank, the reducing mechanism for plastic refuse smashes, and it includes rubbing crusher, metering device for plastic refuse weighs and the ratio of weighing of other auxiliary materials, and it is including the batching electronic scale, intensification agitating unit for the mix of raw materials, stirring, add gentle the stoving, it includes the intensification agitator, the suppression device for the press forming of raw materials, it includes filling device, embossing mold utensil and is used for the drive the actuating mechanism of embossing mold utensil action. The utility model provides a pollution problem of plastic refuse to the environment to to its regeneration, form virtuous circle.

Description

Plastic garbage processes streamline

Technical field

This utility model relates to a kind of plastic molding equipment, and in particular, it relates to a kind of plastic garbage and processes streamline.

Background technology

Plastics due to its drop resistant, wear-resisting, easy to use, cost is low etc., and premium properties is widely used in every field, along with social development, the development of plastics technology is maked rapid progress, increasing gradually of plastic, yield is substantially increased year by year, but owing to plastics variety is various, processing technology is different, the waste or used plastics after mixing causes recovery extremely difficult. Therefore technics of reclaim of plastic waste technique Yi Cheng world today significant problem. The packing material sorted out from domestic waste, as: plastic bag and other plastics, what wherein ratio was maximum is food packaging article and refuse bag. This part plastic garbage is not easy to individually reclaim and secondary go-on-go, and carry food residue thing, these nutrient substance are just as culture medium, once environment is suitable for growing substantial amounts of parasite and the antibacterial caused a disease, virus with surprising rapidity, and give out the gas (taste) of stench, the healthy of human body is constituted threat greatly simultaneously, environment is caused serious pollution.

Secondly, existing cement brick is widely used in various occasion, for instance building use, surface of the street laying, park road surfacing etc., and existing cement brick is outdoor laying mostly, it is affected by weather, through exposing to wind and rain, easy air slaking, and then airborne dust can be produced. This cement brick not only structural strength is low, service life is short, and the airborne dust produced is big for environment pollution.

Utility model content

For the deficiency that prior art exists, the purpose of this utility model is in that to provide a kind of plastic garbage to process streamline, plastic garbage can be recycled by it, and produce the plastic tile existing cement brick of replacement, the problem that solves existing cement brick easy-weathering, it is to avoid the environmental pollution that plastic garbage and cement brick air slaking produce.

For achieving the above object, this utility model provides following technical scheme: a kind of plastic garbage processes streamline, including

Rinser, sterilization and deodorization for plastic garbage clean, it includes rinse bath, described rinse bath includes feeding end and discharge end, described discharge end is provided with automatic charging drier, in described rinse bath along feeding end to the direction of discharge end on be provided with the conveyer for carrying plastic garbage;

Reducing mechanism, for the pulverizing of plastic garbage, it includes pulverizer;

Metering device, weighing and the weighing and proportioning of other adjuvants for plastic garbage, it includes dispensing electronic scale;

Intensification agitating device, for raw material mixing, stir, add gentle drying, it includes intensification agitator;

Pressure setting, compressing for raw material, it includes sizer, compacting tool set and for driving the driving mechanism of described compacting tool set action.

By adopting technique scheme, plastic garbage can be sterilized sterilizing in rinser and deodorization is cleaned, it is then delivered in reducing mechanism crush, can be transported in metering device after having crushed and measure, and the adjuvant coordinating other in metering device carries out metering proportion together, then mixed raw material can be transported in intensification agitating device and carry out the stirring that heats up, raw material is made to have plasticity, after intensification stirs, raw material is transported in pressure setting and is pressed, and then just obtain plastic tile, reach to utilize garbage reclamation, and form the effect of building material.

Preferably, described rinser is connected to wastewater treatment equipment, described wastewater treatment equipment includes filter tank, it is connected by sewage pump and pipeline between described filter tank and rinse bath, described filter tank includes the stillpot of part and the catch basin of lower part, by arranging filter course separation between described stillpot and catch basin.

By adopting technique scheme, it is possible to the waste water produced in plastic tile manufacture process is processed, thus reaching to reduce the purpose of environmental pollution.

Preferably, described intensification agitating device is connected to emission-control equipment, described emission-control equipment includes treatment box, air-introduced machine and filtration tank, the air intake of described air-introduced machine is connected to the air vent of intensification agitating device, the outlet air end of described air-introduced machine is connected to the inlet end of described treatment box, and described filtration tank is arranged at the described treatment box other end relative to described air-introduced machine.

By adopting technique scheme, it is possible to the waste gas produced in plastic tile manufacture process is processed, thus reaching to reduce the purpose of environmental pollution.

Preferably, in described treatment box, the position near inlet end is provided with humidifier, humidifier includes the second clarified water pump, pipeline and ultrasound atomizer, the outlet side of described treatment box is provided opposite to relative to inlet end, and described treatment box is provided with spraying mechanism and outlet in the position near outlet side.

By adopting technique scheme, it is possible to make the waste gas in entrance treatment box fully and moisture, and then reach better exhaust-gas treatment effect, and the waste water after processing is discharged from outlet.

Preferably, the second active carbon layer that described filtration tank includes setting gradually, the first axial flow blower, the 3rd active carbon layer, the second axial flow blower, the air outlet place of described first axial flow blower is provided with suction nozzle, and described suction nozzle is connected to the second oxygen source ozone all-in-one.

By adopting technique scheme, waste gas can be made absorbed more abundant in the second active carbon layer and the 3rd active carbon layer, and, when waste gas transporting velocity in the second active carbon layer and the 3rd active carbon layer is inadequate, first axial flow blower and the second axial flow blower can improve enough power, what make that waste gas can carry in filtration tank is more smooth and easy, improves the efficiency of exhaust-gas treatment.

It is also preferred that the left be provided with gas-liquid mixing pump in described rinse bath, described gas-liquid mixing pump is connected to the first oxygen source ozone all-in-one.

By adopting technique scheme, it is possible to use directly the plastic garbage in rinse bath is carried out disinfection sterilizing and deodorization of ozone to clean, and, the gas-liquid mixing pump of setting can increase ozone contact area in cleaning solution so that the better processing effect of ozone.

It is also preferred that the left described pulverizer is connected to charging belt conveyer, the discharge end of described charging belt conveyer is connected to the feeding mouth of described pulverizer.

By adopting technique scheme, it is possible to make plastic garbage be transported in pulverizer from the discharging opening of automatic charging drier automatically and pulverize, improve transfer efficiency, and save manpower.

It is also preferred that the left the upstream of described intensification agitator is connected to preheating agitator.

By adopting technique scheme, it is possible to original substep is carried out the stirring that heats up, is unlikely to just material to be warmed to significantly high temperature, it is to avoid raw material is charred quickly.

It is also preferred that the left the side of described compacting tool set is provided with conveyer.

By adopting technique scheme, it is possible to the convenient plastic tile suppressed is carried packing timely, saves manpower.

It is also preferred that the left described conveyer includes conveyer belt, described conveyer belt is provided with cooler bin.

By adopting technique scheme, it is possible to timely plastic tile is cooled down so that it is molding rapidly, it is to avoid it deforms after pressing.

This utility model has an advantage that plastic garbage can be turned waste into wealth by this utility model; plastic garbage harm to environment is greatly reduced, it addition, in the fabrication process the process of waste water and waste gas all to have been reached the effect recycled; and then, better protect environment.

Accompanying drawing explanation

Fig. 1 is the top view of embodiment;

Fig. 2 is the axonometric drawing one of embodiment;

Fig. 3 is the axonometric drawing two of embodiment;

Fig. 4 is the axonometric drawing three of embodiment;

Fig. 5 is the axonometric drawing four of embodiment;

Fig. 6 is the structural representation of waste water, exhaust-gas treatment in embodiment.

In figure: 1, rinser; 11, rinse bath; 12, automatic charging drier; 2, reducing mechanism; 21, pulverizer; 22, charging belt conveyer; 3, metering device; 31, speed governing conveying worm; 32, tubular type continuous batching electronic scale; 4, intensification agitating device; 41, preheating agitator; 42, intensification agitator; 5, pressure setting; 51, hydraulic press; 52, compacting tool set; 53, conveyer belt; 54, water cooling box; 55, sizer; 56, hydraulic thrust machine; 57, track; 58, die; 59, sliding block; 6, wastewater treatment equipment; 61, filter tank; 611, stillpot; 612, catch basin; 62, filter course; 7, emission-control equipment; 71, treatment box; 711, ultrasound atomizer; 712, shower nozzle; 72, filtration tank; 81, the first oxygen source ozone all-in-one; 82, gas-liquid mixing pump; 83, the first multifunctional pump; 84, sewage pump; 85, the 3rd water pump; 86, the second sewage pump; 87, the second oxygen source ozone all-in-one; 88, the second clarified water pump.

Detailed description of the invention

With reference to shown in accompanying drawing, this utility model is further illustrated.

Embodiment: a kind of plastic garbage processes streamline, including rinser 1, reducing mechanism 2, metering device 3, intensification agitating device 4, pressure setting 5, wastewater treatment equipment 6 and emission-control equipment 7. Wherein,

Rinser 1 includes rinse bath the 11, first oxygen source ozone all-in-one 81, gas-liquid mixing pump 82 and automatic charging drier 12.

Wherein, the rectangular setting of rinse bath 11, it is possible to be made of metal, for instance ferrum or rustless steel etc. The upper edge of rinse bath 11 is provided with multi-shaft stirring oar, it is therefore an objective to be ceaselessly stirred the refuse plastic swum in above cleanout fluid cleaning, and from the end that enters of cell body, refuse plastic is transported to out end. Wherein, multi-shaft stirring oar includes many shafts, shaft arranges multiple material toggling pawl, each material toggling pawl is made up of arc rod for stiring materials of three circumference array, the axle head extending rinse bath 11 outer at shaft is connected to sprocket wheel, and this shaft is by driven by motor chain drive and then realizes rotating.

Secondly, the outlet at rinse bath 11 is provided with initial filter screen cloth, and outlet is connected to the first multifunctional pump 83, and the sewage in rinse bath 11 can be discharged by the first multifunctional pump 83 timely. Initial filter screen cloth is as the filter before the first multifunctional pump 83, in order to separate needing the bulk rubbish thing being further processed.

Furthermore it is also possible to arrange neodymium iron boron fixed mount and permanent magnets in rinse bath 11, it is to accord with, in order to absorb, the ferrous metal thing carried in refuse plastic, in order to avoid the equipment of next step operation is caused damage.

First oxygen source ozone all-in-one 81 and gas-liquid mixing pump 82, this is the equipment that two sets are independent, but must in conjunction with use in the process technical process of this streamline. The former is separated the nitrogen in air, carbon dioxide by efficient molecular sieve, then more than 95% oxygen do source of the gas through high pressure, high frequency, be ionized into the ozone of high concentration. The latter is ozone gas after negative pressure sucks and is sufficiently stirred for cleanout fluid in the vane pump cavity of high speed rotating and smashes and mix, in the bottom being emitted back towards rinse bath 11 through high pressure spray. Mix with cleanout fluid further in rinse bath 11, increase aeration area and holdup time, and (its outlet is arranged on the rinse bath 11 other end relative to feeding end to form the adverse current contrary with refuse plastic moving direction, in the present embodiment, namely in one end of automatic charging drier 12), to strengthen cleaning performance. (belong to prior art about the ozone application in fields such as environmental protection, epidemic prevention, water process and effect, it is not described in detail herein) when the ozone concentration in cleanout fluid has reached the content of process stipulation, it is possible to play the effect of disinfection sterilization deodorizing at short notice. And play the Strong oxdiative to the heavy metal mixed wherein and nuisance and Degradation, it is suppressed that there is hazardous substance diffusivity in air, soil and water.

Automatic charging drier 12, it is mounted in the discharge end of rinse bath 11, including urceolus and the helical blade being arranged in urceolus, helical blade offered tank, additionally offers discharging opening on the top of urceolus. Plastic garbage can continuously upwards be pushed by helical blade, and cross tank can push process in dewatering so that the water of plastic garbage is dried. It continuously sucks the plastic garbage cleaned through sterilization, deodorization in spin dryer tube, completes to discharge after material water separates.

Reducing mechanism 2 includes two set units, i.e. charging belt conveyer 22 and pulverizer 21, the plastic garbage sorted out is sent on belt conveyor, insert in the spout of pulverizer 21 and pulverize, after reaching the specification of technological requirement, plastic garbage after crushed discharges pulverizer 21 cavity by the screen cloth of lower section, enters next step operation.

Metering device 3 includes two speed governing conveying worms 31 and tubular type continuous batching electronic scale 32, its main function is different raw materials, adjuvant, chemicals within the unit interval, in the ratio formula combination of technological requirement together, next step operation continuously it is transported to.

Intensification agitating device 4 includes preheating agitator 41 and intensification agitator 42, preheating agitator 41 includes shell and is arranged on the heater of outer casing bottom, heater includes some heating electrical equipment and heating wire etc., heater be provided above stirring inner core, axially arranged in stirring inner core have shaft, being provided with some stirring rod on shaft, these stirring rod are arranged along spiral path, thus reaching the effect advancing material with stirring material. Wherein stirring inner core can be in the cylindric setting sealed, or the setting that takes the shape of the letter U, and so conveniently can arrange sealing lid at the opening part of inner core, be easy to open the stirring and situation of heating that seal in lid inspection section. This sealing lid is that hollow is arranged, and arranges adiabator layer at the interior intracavity sealing lid so that seals lid and has heat insulation effect. Intensification agitator 42 includes columnar urceolus and the stirring vane being arranged in urceolus and heater, heats so that material obtains further stirring in this intensification agitator 42.

By conveying worm, the full formula siccative handled well in preheating agitator 41 is delivered in intensification agitator 42, carries out secondary heating and stir to the temperature range meeting process stipulation. Opens solenoid valve is discharged into the unit in sizer 55(pressure setting 5) in, the inlet valve of intensification agitator 42 is opened simultaneously, and virgin material joins by the equivalent given off and continues stirring of heating in intensification agitator 42. The volume of sizer 55 can fill up the compacting materials of 3-5 finished product, and the cycle just can meet in new raw material heated and stirred to the scope of process stipulation during this period of time. It has used time short advantage, and the used time is short is owing to also storing more than the 90% heated grog being stirred in intensification agitator 42, thus considerably increasing the thermal source of accumulation. So go round and begin again, move in circles and be achieved that the continuous continuous-flow type production operation that feeding works.

Pressure setting 5 includes sizer 55, hydraulic press 51, compacting tool set 52 and conveyer, compacting tool set 52 is connected to the underface of hydraulic press 51, sizer 55 is arranged on the side of compacting tool set 52, conveyer is arranged on the compacting tool set 52 opposite side relative to sizer 55, and conveyer is arranged on operation track 57, the support of conveyer is provided with roller, for conveyer sliding on track 57, conveyer includes conveyer belt, the surface of conveyer belt is provided with water cooling box 54, the top of water cooling box 54 is provided with spraying mechanism, conveyer belt 53 be arranged below outlet. when being transported in water cooling box 54 by conveyer belt 53 after plastic tile has been suppressed, plastic tile is carried out spraying cooling by spraying mechanism, and spray water out can flow out from the outlet below conveyer belt 53.

After being filled with raw material in sizer 55, die 58 chamber and sliding block 59 are moved to the lower section of sizer 55 by reciprocating hydraulic thrust machine 56. Now the stirring paddle in sizer 55 is ceaselessly rotating, and raw material is inserted in die 58 cavity uniformly, completes a filler job. Now hydraulic thrust machine about 56 oil cylinder starts following table die 58 cavity and sliding block 59 being back into simultaneously 400 t hydraulic press 51 along guide rail simultaneously, and now press top shoe drives in punch press-in die 58. Rise to complete after keeping several seconds pressure and once suppress work. Now 56 times oil cylinders of hydraulic thrust machine start lower slider cushion block pull-out die 58 position, conveyer has been moved to the underface of die 58 simultaneously, under this thing punch secondary, pressure handle finished product ejects die 58, fall on the conveyer belt 53 of conveyer, it is sent in water cooling box 54, spreading out of after spraying cooling, so far a pressing process process is fully completed.

Wastewater treatment equipment 6 includes filter tank 61, is connected by sewage pump 84 and pipeline between this filter tank 61 with rinse bath 11, is incorporated in filter tank 61 by the sewage produced and processes in rinse bath 11. This filter tank 61 includes the stillpot 611 of part and the catch basin 612 of lower part, it is provided with filter course 62(and filter course 62 between stillpot 611 and catch basin 612 and filter tank 61 is separated into the stillpot 611 of upside and the catch basin 612 of downside), certainly, stillpot 611 and catch basin 612 can also separate two independent grooves, it is contemplated that the problem that space is arranged, two grooves are integrated not only without influence on filter effect, occupation of land space can also be saved, so two grooves are preferably integrated by the present embodiment. Wherein, filter course 62 includes the first active carbon layer of bottom, the metalling in middle level, the thick river sand layer of surface layer.

When the contaminated wastewater degree in rinse bath 11 reaches can not to complete cleaning task, the sewage suction muddy by the first multifunctional pump 83 carries out precipitation filtration treatment in stillpot 611, sludge retention filter course 62 surface in stillpot 611, clear water after filtering is back to catch basin 612.

Rinse bath 11, stillpot 611 and catch basin 612 these three groove can continuously work, it is also possible to service intermittent. At running hours, when liquid level in rinse bath 11 is lower than the setting value of process requirements, open small pump (to connect with rinse bath 11 and catch basin 612, clear water in catch basin 612 is added in rinse bath 11) moisturizing, the first multifunctional pump 83 is opened when the water in rinse bath 11 has exceeded the turbidity of process requirements, the sewage of bottom is discharged to filter tank 61 and thus achieves recycling of water, reach the effect of zero-emission. After shutting down, the mud in filter tank 61 is trapped in the surface of filter course 62 with semi-moist state, just can reach the purpose cleared up when being cleaned to expose thick river sand layer every time. The mud cleared being backfilling in blender (subsequent handling) through drying, measuring to weigh in proportion, is pressed into brick as inserts again, this technical process just completes nuisanceless, zero discharge treatment to pollutant.

Emission-control equipment 7 includes treatment box 71, air-introduced machine and filtration tank 72, wherein, the air intake of air-introduced machine is connected to the air vent of intensification agitating device 4, the outlet air end of air-introduced machine is connected to the inlet end for the treatment of box 71, in treatment box 71, the position near inlet end is provided with humidifier, humidifier includes the second clarified water pump 88, pipeline and ultrasound atomizer 711, and clear water is extracted and then is atomized by ultrasound atomizer 711 by the second clarified water pump 88, so that waste gas and fog are sufficiently mixed. The outlet side for the treatment of box 71 is provided opposite to relative to inlet end, it is provided with spraying mechanism and outlet near the position of outlet side, the bottom for the treatment of box 71 is provided with the swash plate being gradually lowered by inlet end to outlet side so that the waste water after process can quickly flow out from outlet. Spraying mechanism includes the 3rd water pump 85, pipeline and shower nozzle 712, drainage excessively in catch basin 612 is drawn into and is sprayed by shower nozzle 712 by the 3rd water pump 85, the water after spray impurity in waste gas is combined and becomes waste water, waste water is discharged by outlet, this outlet is connected to the second sewage pump 86, waste water is extracted and is filtered to stillpot 611, then recycle. The second oxygen source ozone all-in-one 87 it is additionally provided with on the side for the treatment of box 71, it has two outlets, one outlet is to treatment box 71 so that the interior and fog of ozone entrance treatment box 71 and the water sprayed out are fully contacted, and then improve the effect of exhaust-gas treatment. Further, being additionally provided with filtration tank 72 in the position of outlet side, this filtration tank 72 includes the second active carbon layer, the first axial flow blower, the 3rd active carbon layer, the second axial flow blower from the bottom to top successively. And the air outlet place of the first axial flow blower is provided with suction nozzle, and another outlet of this suction nozzle and the second oxygen source ozone all-in-one 87 connects so that exhaust-gas treatment better effects if. Two axial flow blowers herein arranged enable to gas can be more smooth and easy in the second active carbon layer and the 3rd active carbon layer, are conducive to the gas after processing to discharge rapidly, improve the efficiency of exhaust-gas treatment.

Plastic garbage can produce toxic and harmful in the process of heating, and air, human body and environment are worked the mischief. For solving this difficult problem, have employed this emission-control equipment 7, the waste gas through its process meets discharging standards.

Automatic charging drier in the present embodiment, pulverizer, speed governing conveying worm, tubular type continuous batching electronic scale, preheating agitator, intensification agitator, hydraulic press, water cooling box, sizer, hydraulic thrust machine, ultrasound atomizer, oxygen source ozone all-in-one, gas-liquid mixing pump and each water pump belong to prior art, do not repeat them here.

This plastic garbage processes streamline and includes following production process: 1. matting; 2. material preparation section; 3. finished product suppression process; 4. waste gas integrated treatment operation. Below above several operations are described in detail:

1. matting: plastic garbage puts into the feeding end of rinse bath 11, is carried out in rinse bath 11, clean process in complete clean, sterilization, deodorization effect. It is then transmitted in automatic charging drier 12 dry.

The waste water produced in this process needs to process, by sewage pump 84, the waste water in rinse bath 11 is extracted to stillpot 611 precipitation filter, then the water after cleaning is concentrated in catch basin 612, and the clear water in catch basin 612 can be re-used in Rinsing Area.

2. material preparation section;

2.1 sorting operations: the plastic garbage after drying needs sorting, sorting is by manually carrying out on continuous sorting workbench, the purpose of this operation is there being the plastic sheeting recycling value to sort out by coloured, colourless, transparent, in order to being processed further utilizing. Capital equipment is made up of continuous sorting workbench and left and right conveyer belt 53. The thin film being sorted out packs standby respectively. The refuse plastic not being processed further value is detained on the table, is sent to pulverizing process.

2.2 pulverizing process: previous step sorts remaining plastic garbage and is sent on belt conveyor by continuous sorting workbench, insert in the spout of pulverizer 21 and pulverize, after reaching the specification of technological requirement, plastic garbage after crushed discharges pulverizer 21 cavity by the screen cloth of lower section, enters metering, proportioning operation.

2.3 meterings, proportioning operation: by speed governing conveying worm 31 and tubular type continuous batching electronic scale 32 within the unit interval different raw materials, adjuvant, chemicals, in the ratio formula combination of technological requirement together, intensification agitating procedure continuously it is transported to.

2.4 intensification agitating procedures: by preheating agitator 41 by various raw materials mix, stir, heat, dry after be continuously transported to intensification agitator 42, intensification agitator 42 material is carried out heat up stirring after enter suppression process.

3. finished product suppression process: material is delivered in sizer 55 by the agitator 42 that heats up, by sizer 55 to reinforced in die 58, then suppress, after having suppressed, being transported in water cooling box 54 to cool down by conveyer, the accumulating of follow-up finished product can also arrange the equipment and facility etc. such as stacking machine, supporting plate, guide rail.

4. waste gas integrated treatment operation: the waste gas produced by preheating agitator 41 and intensification agitator 42 is incorporated in treatment box 71 by air-introduced machine and processes, and the gas after process is discharged by filtration tank 72, it is possible to reach the discharge standard of national regulation. And the waste water produced in processing procedure is discharged by outlet, this outlet is connected to the second sewage pump 86, is extracted by waste water and is filtered to stillpot 611, then recycles. The water that spraying mechanism uses can by extracting in catch basin 612 to come to utilize, and whole wastewater treatment and exhaust-gas treatment form a complete circulating treating system.

In addition, along with developing rapidly of real estate cause, in China or even the whole world, substantial amounts of waste and old building is had every day to be removed, new building is established, and in the middle of this, will necessarily produce substantial amounts of building waste, such as dregs, spoir, rejected material and remaining mud etc., these building wastes will also result in environmental pollution. In this production line, it is possible to use these building wastes are as the adjuvant of plastic tile so that it is be mixed together compacting with plastic garbage and form composite plastic brick. Realize such purpose, have only to increase pulverizer 21 and vibrosieve on this production line, pulverize collecting the building waste come, then vibration screening, metering proportion then through metering device 3 is mixed in intensification agitating device 4 and is stirred mixing, being then able to make composite plastic brick, the structural strength of this composite plastic brick also is able to be strengthened. By such production line, not only make plastic garbage obtain regeneration, and also by construction refuse regenerated utilization, form new construction material, moreover it is possible to reduce environmental pollution.

It addition, for meet the market demand to a greater extent, secondary compacting coloured facing technique that native system is well-designed, it is possible to meet the market demand to multiple color and luster. Concrete scheme is just to increase a set of intensification agitating device 4, sizer 55 and reciprocating hydraulic thrust machine 56. Repeat process above process and complete filler and the pressing process of secondary colour raw material. What native system produced is physical article, and employing is bottom discharge pattern, if needing compacting porous or hollw article, is necessary for the top discharge pattern adopted after ejecting, and more mold exchange increases auxiliary equipment. Mistake described in new finished product pressing process (two), previous section, artificial separation operation, the majority being sorted out is food or vegetable packing plastics bag, material of this part is substantially PE(polyethylene) or LDPE(Low Density Polyethylene) material itself is nontoxic, it is possible to select the plastics being similar to veneer color or transparent plastic to do the special raw material of veneer. Transparent plastic bag through high temperature extrusion, makes regenerated granule after may also pass through secondary cleaning pulverizing, and the added value of itself is higher, it is possible to production cost is greatly lowered.

The above is only preferred implementation of the present utility model, and protection domain of the present utility model is not limited merely to above-described embodiment, and all technical schemes belonged under this utility model thinking belong to protection domain of the present utility model. It should be pointed out that, for those skilled in the art, without departing from the some improvements and modifications under this utility model principle premise, these improvements and modifications also should be regarded as protection domain of the present utility model.

Claims (10)

1. a plastic garbage processes streamline, it is characterised in that: include

Rinser, sterilization and deodorization for plastic garbage clean, it includes rinse bath, described rinse bath includes feeding end and discharge end, described discharge end is provided with automatic charging drier, in described rinse bath along feeding end to the direction of discharge end on be provided with the conveyer for carrying plastic garbage;

Reducing mechanism, for the pulverizing of plastic garbage, it includes pulverizer;

Metering device, weighing and the weighing and proportioning of other adjuvants for plastic garbage, it includes dispensing electronic scale;

Intensification agitating device, for raw material mixing, stir, add gentle drying, it includes intensification agitator;

Pressure setting, compressing for raw material, it includes sizer, compacting tool set and for driving the driving mechanism of described compacting tool set action.

2. plastic garbage according to claim 1 processes streamline, it is characterized in that: described rinser is connected to wastewater treatment equipment, described wastewater treatment equipment includes filter tank, it is connected by sewage pump and pipeline between described filter tank and rinse bath, described filter tank includes the stillpot of part and the catch basin of lower part, by arranging filter course separation between described stillpot and catch basin.

3. plastic garbage according to claim 1 processes streamline, it is characterized in that: described intensification agitating device is connected to emission-control equipment, described emission-control equipment includes treatment box, air-introduced machine and filtration tank, the air intake of described air-introduced machine is connected to the air vent of intensification agitating device, the outlet air end of described air-introduced machine is connected to the inlet end of described treatment box, and described filtration tank is arranged at the described treatment box other end relative to described air-introduced machine.

4. plastic garbage according to claim 3 processes streamline, it is characterized in that: in described treatment box, the position near inlet end is provided with humidifier, humidifier includes the second clarified water pump, pipeline and ultrasound atomizer, the outlet side of described treatment box is provided opposite to relative to inlet end, and described treatment box is provided with spraying mechanism and outlet in the position near outlet side.

5. plastic garbage according to claim 3 processes streamline, it is characterized in that: the second active carbon layer that described filtration tank includes setting gradually, the first axial flow blower, the 3rd active carbon layer, the second axial flow blower, the air outlet place of described first axial flow blower is provided with suction nozzle, and described suction nozzle is connected to the second oxygen source ozone all-in-one.

6. plastic garbage according to claim 1 processes streamline, it is characterised in that: being provided with gas-liquid mixing pump in described rinse bath, described gas-liquid mixing pump is connected to the first oxygen source ozone all-in-one.

7. plastic garbage according to claim 1 processes streamline, it is characterised in that: described pulverizer is connected to charging belt conveyer, and the discharge end of described charging belt conveyer is connected to the feeding mouth of described pulverizer.

8. plastic garbage according to claim 1 processes streamline, it is characterised in that: the upstream of described intensification agitator is connected to preheating agitator.

9. plastic garbage according to claim 1 processes streamline, it is characterised in that: the side of described compacting tool set is provided with conveyer.

10. plastic garbage according to claim 9 processes streamline, it is characterised in that: described conveyer includes conveyer belt, and described conveyer belt is provided with cooler bin.