CN111500305B - Waste plastic treatment equipment - Google Patents
Waste plastic treatment equipment Download PDFInfo
- Publication number
- CN111500305B CN111500305B CN202010351935.XA CN202010351935A CN111500305B CN 111500305 B CN111500305 B CN 111500305B CN 202010351935 A CN202010351935 A CN 202010351935A CN 111500305 B CN111500305 B CN 111500305B
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- reaction kettle
- carbon
- tank
- hopper
- outlet
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- 229920003023 plastic Polymers 0.000 title claims abstract description 44
- 239000004033 plastic Substances 0.000 title claims abstract description 44
- 239000002699 waste material Substances 0.000 title claims abstract description 37
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 132
- 238000006243 chemical reaction Methods 0.000 claims abstract description 100
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 89
- 239000002994 raw material Substances 0.000 claims abstract description 56
- 238000003860 storage Methods 0.000 claims abstract description 53
- 230000003197 catalytic effect Effects 0.000 claims abstract description 45
- 239000000428 dust Substances 0.000 claims description 32
- 238000001816 cooling Methods 0.000 claims description 27
- 238000003756 stirring Methods 0.000 claims description 14
- 238000010438 heat treatment Methods 0.000 claims description 11
- 238000007790 scraping Methods 0.000 claims description 10
- 239000000463 material Substances 0.000 claims description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 6
- 239000010439 graphite Substances 0.000 claims description 5
- 229910002804 graphite Inorganic materials 0.000 claims description 5
- 239000002184 metal Substances 0.000 claims description 5
- 238000003825 pressing Methods 0.000 claims description 4
- 230000005855 radiation Effects 0.000 claims description 4
- 230000009467 reduction Effects 0.000 claims description 4
- 230000007423 decrease Effects 0.000 claims description 3
- 238000007599 discharging Methods 0.000 claims description 3
- 238000007789 sealing Methods 0.000 claims description 3
- 238000010276 construction Methods 0.000 claims description 2
- 239000004579 marble Substances 0.000 claims description 2
- 238000012856 packing Methods 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 abstract description 5
- 238000010924 continuous production Methods 0.000 abstract description 3
- 238000007670 refining Methods 0.000 description 11
- 238000000926 separation method Methods 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- 230000009471 action Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 230000033228 biological regulation Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000007306 turnover Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
- C10G1/10—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal from rubber or rubber waste
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
The invention relates to waste plastic treatment equipment, which comprises a feeding unit, a conveying unit and a control unit, wherein the feeding unit comprises a propeller and a raw material distributor; the raw material distributor is used for conveying raw materials to the first reaction kettle and the second reaction kettle at intervals; the first catalytic tank is connected with one end of the first reaction kettle, and the first carbon outlet device is connected with the other end of the first reaction kettle; the second catalytic tank is connected with one end of the second reaction kettle, and the second carbon outlet device is connected with the other end of the second reaction kettle; one end of the coil pipe is connected with the top of the first catalytic tank through an automatic control valve; the first oil tank dedusting tower is respectively connected with the top of the second catalytic tank and the first oil tank; and a second oil storage tank. According to the waste plastic treatment equipment, the raw material distributor is arranged at the lower end of the pusher and is respectively connected with the first reaction kettle and the second reaction kettle, so that the first reaction kettle and the second reaction kettle can be sequentially fed at regular time intervals, the continuous production of the equipment can be ensured, and the production efficiency is improved.
Description
Technical Field
The invention relates to the technical field of chemical industry, in particular to the technical field of plastic oil refining, and particularly relates to waste plastic treatment equipment.
Background
With the rapid development of the plastic industry, the application of plastic products is also becoming more and more widespread, and the plastic products have penetrated into various fields of national economy and daily life of people. The plastic has the characteristics of heat insulation, corrosion resistance and the like, and the characteristics of the plastic can be utilized, but the characteristics can prevent the plastic from decomposing when the waste plastic is treated, so that the problem of environmental pollution is not easy to rot.
And the waste plastics are used as raw materials for oil refining treatment, so that the treatment problem of the waste plastics can be effectively solved. However, the waste plastic oil refining requires special attention to the process flow, otherwise leakage pollution is caused. More importantly, the process flow is different, which causes great difference in oil refining efficiency and oil refining precision. The existing waste plastic oil refining equipment has lower efficiency, mixed oil gas and carbon powder and lower oil refining purity.
Disclosure of Invention
The invention aims to solve the problems and provide high-efficiency waste plastic treatment equipment.
To achieve the above object, the present invention provides a waste plastic treatment apparatus comprising:
the feeding unit comprises a propeller and a raw material distributor which is positioned at the tail end of the propeller and connected with the propeller;
the first reaction kettle and the second reaction kettle are respectively connected with the raw material distributor through a feed pipeline, and the raw material distributor is used for conveying raw materials to the first reaction kettle and the second reaction kettle at intervals;
the first catalytic tank is connected with one end of the first reaction kettle, and the first carbon outlet device is connected with the other end of the first reaction kettle;
the second catalytic tank is connected with one end of the second reaction kettle, and the second carbon outlet device is connected with the other end of the second reaction kettle;
one end of the coil pipe is connected with the top of the first catalytic tank through an automatic control valve;
the first oil storage tank is connected with the other end of the coil pipe;
the dust removing tower is respectively connected with the top of the second catalytic tank and the first oil storage tank;
the second oil storage tank is connected with the first oil storage tank through a pipeline, and a condenser is arranged on the pipeline;
the inlet end of the compressor is connected with the second oil storage tank;
and the combustible gas storage tank is connected with the outlet end of the compressor.
According to one aspect of the invention, the propeller comprises a hopper, a motor positioned above the hopper, a stirring rod with one end connected with the motor and the other end extending into the hopper and provided with a spiral pressing plate, and a raw material conveying belt positioned on one side of the hopper.
According to one aspect of the invention, the outer wall of the hopper is provided with an electric frequency heating device or an infrared radiation heating device for heating the hopper in a partitioning way, and the temperature gradually rises along the direction approaching the raw material distributor.
According to one aspect of the invention, the raw material distributor comprises a feed inlet connected with the hopper, and a first discharge outlet and a second discharge outlet respectively connected with the first reaction kettle and the second reaction kettle;
a damper is arranged between the feeding hole and the hopper.
According to one aspect of the invention, the damper is respectively connected with the hopper and the raw material distributor through flanges, and a metal graphite gasket is also arranged between the damper and the hopper and between the damper and the raw material distributor;
the inner diameter of the damper gradually decreases in a direction from the hopper to the raw material distributor.
According to one aspect of the invention, the feed line is provided with a one-way valve.
According to one aspect of the present invention, the first reaction kettle and the second reaction kettle have the same structure, and each comprises:
the device comprises a central shaft arranged in a kettle body, a driving component positioned on the kettle body and used for driving the central shaft to rotate, a distributing plate arranged on the central shaft, a film forming and blade and a scraping plate;
a mechanical seal is arranged at the joint of the driving assembly and the kettle body;
the material distributing plate is spaced from the inner wall of the kettle body, and the scraping plate is arranged on the inner wall of the kettle body close to the material distributing plate;
the film forming blade is positioned below the material separating plate and the scraping plate.
According to one aspect of the invention, the first reaction kettle and the second reaction kettle are respectively provided with an oil gas outlet connected with the first catalytic tank and the second catalytic tank and a carbon outlet connected with the first carbon outlet and the second carbon outlet respectively.
According to one aspect of the present invention, the first catalytic tank and the second catalytic tank are identical in structure, and each include: the device comprises a tank body, a central rotating shaft positioned in the tank body, a coupler positioned on the tank body (41) and a driving motor connected with the coupler;
a mechanical sealing element is arranged between the coupler and the tank body;
the top of the tank body is provided with an oil gas outlet pipe.
According to one aspect of the invention, the oil gas outlet pipe of the first catalytic tank is connected with the coil pipe, and the oil gas outlet pipe of the second catalytic tank is connected with the dust removal tower;
the dust removing tower comprises a first dust removing tower and a second dust removing tower which are communicated with each other, the bottoms of the first dust removing tower and the second dust removing tower are connected with a first oil storage tank through pipelines, and the top of the second dust removing tower is connected to a second oil storage tank through a pipeline provided with a condenser, and high-frequency oscillators are arranged inside the first oil storage tank and the second oil storage tank.
According to one aspect of the invention, the first carbon outlet and the second carbon outlet have the same structure, and each carbon outlet comprises an electric valve arranged at the carbon outlet, an electric sliding rail, a carbon outlet driving motor arranged on the electric sliding rail, a carbon outlet screw rod connected with the carbon outlet driving motor, carbon outlet pipes arranged on the periphery of the carbon outlet screw rod, and a carbon powder cooling barrel arranged below the carbon outlet pipes.
According to one aspect of the invention, a stirring device is arranged in the carbon powder cooling barrel.
According to one aspect of the invention, the toner cooling barrel comprises a first barrel wall and a second barrel wall, wherein the first barrel wall and the second barrel wall are provided with a space, and circulating water cooling is arranged in the space.
According to one aspect of the invention, a carbon release valve is arranged at the lower end of the carbon powder cooling barrel and is connected to the closed carbon storage barrel through a packing auger pipeline.
According to the waste plastic treatment equipment, the raw material distributor is arranged at the lower end of the pusher and is respectively connected with the first reaction kettle and the second reaction kettle, so that the first reaction kettle and the second reaction kettle can be sequentially fed at regular time intervals, the continuous production of the equipment can be ensured, and the production efficiency is improved.
According to the waste plastic treatment equipment, in the reaction process of the reaction kettle, oil gas, carbon powder and other particles can be effectively separated, so that the purity of subsequent oil refining is improved, and meanwhile, the oil refining efficiency is improved. In addition, the structural arrangement between the reaction kettle and the catalytic tank enables the reaction to be more sufficient, and the oil gas conversion rate is improved.
According to the waste plastic treatment equipment, before the oil gas enters the first oil storage tank, the oil gas enters the dust removal tower, so that the separation of the oil gas and carbon powder can be further realized, and the separation precision is ensured.
According to the waste plastic treatment equipment, the electric valve is arranged at the carbon outlet, and the carbon outlet spiral rod is extended into the carbon outlet to carry out carbon outlet operation when carbon outlet is needed.
The waste plastic treatment equipment disclosed by the invention is used for treating waste plastic to form separated carbon powder, oil and combustible gas, so that the pollution is prevented and the production energy is realized.
Drawings
FIG. 1 schematically shows a construction view of a waste plastic treatment apparatus according to an embodiment of the present invention;
FIG. 2 schematically shows a block diagram of a feeder unit according to one embodiment of the invention;
fig. 3 schematically shows an enlarged view of the portion a in fig. 2;
FIG. 4 schematically shows a structural view of a first reaction vessel and a second reaction vessel according to an embodiment of the present invention;
FIG. 5 schematically illustrates a block diagram of a first carbon generator and a second carbon generator in accordance with one embodiment of the present invention;
FIG. 6 schematically illustrates a block diagram of a first catalytic tank and a second catalytic tank according to one embodiment of the invention;
fig. 7 schematically shows a structure of a dust removing tower according to an embodiment of the present invention;
fig. 8 schematically shows a block diagram of a first tank and a second tank according to an embodiment of the invention.
Detailed Description
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings that are required to be used in the embodiments will be briefly described below. It is apparent that the drawings in the following description are only some embodiments of the present invention, and that other drawings may be obtained from these drawings without inventive effort for a person of ordinary skill in the art.
The present invention will be described in detail below with reference to the drawings and the specific embodiments, which are not described in detail herein, but the embodiments of the present invention are not limited to the following embodiments.
As shown in fig. 1, the waste plastic treatment apparatus of the present invention includes a feeding unit 1, a first reaction kettle 2, a second reaction kettle 3, a first catalytic tank 4, a first carbon generator 5, a second catalytic tank 6, a second carbon generator 7, a coil pipe 8, a first oil storage tank 9, a dust removal tower 10, a second oil storage tank 11, a compressor 13, a combustible gas storage tank, and a combustible gas storage tank 14.
In the present invention, the feeding unit 1 includes a pusher 1a and a raw material dispenser 1b connected thereto at the end of the pusher 1a for the conveyance of waste plastics. The first reaction kettle 2 and the second reaction kettle 3 are respectively connected with a raw material distributor 1b through a feeding pipeline, and the raw material distributor 1b is used for conveying raw materials to the first reaction kettle 2 and the second reaction kettle 3 at intervals. The first catalytic tank 4 is connected with one end of the first reaction kettle 2, and the first carbon outlet device 5 is connected with the other end of the first reaction kettle 2. The second catalytic tank 6 is connected with one end of the second reaction kettle 3, the second carbon outlet device 7 is connected with the other end of the second reaction kettle 3, one end of the coil pipe 8 is connected with the top of the first catalytic tank 4 through an automatic control valve, and the other end of the coil pipe is connected with the first oil storage tank 9. The dust removal tower 10 is respectively connected with the top of the second catalytic tank 5 and the first oil storage tank 9. The second oil storage tank 11 is connected with the first oil storage tank 9 through a pipeline, and a condensation 12 is arranged on the pipeline. The inlet end of the compressor 13 is connected with the second oil storage tank 11, and the outlet end of the compressor 13 is connected with the combustible gas storage tank 14.
According to the waste plastic treatment equipment, the raw material distributor 1b is arranged at the lower end of the pusher 1a and is respectively connected with the first reaction kettle 2 and the second reaction kettle 3, so that the first reaction kettle 2 and the second reaction kettle 3 can be sequentially fed at regular time intervals, the continuous production of the equipment can be ensured, and the production efficiency is improved.
Referring to fig. 1 to 3, the propeller 1a of the present invention includes a hopper 111, a motor 111 disposed above the hopper 111, a stirring rod 13 having one end connected to the motor 112 and the other end extending into the hopper 111 and provided with a screw pressing plate, and a raw material conveying belt 114 disposed on one side of the hopper 111.
According to one embodiment of the invention, the motor 112 drives the belt pulley on the reduction gearbox through the belt pulley and the belt to drive the stirring rod 13 with the spiral pressing plate in the hopper 111 to rotate, and the conveying belt 114 conveys the waste plastic raw material into the hopper 111 and to the raw material distributor 1 b. In fig. 2, the bottom of the reduction box is arranged on a cylindrical marble sliding block, and when the feeding system expands with heat and contracts with cold, the sliding block can be freely stretched or contracted, so that the raw material distributor and the feeding pipe of the reaction kettle can be protected from deformation along with the expansion with heat and contraction with cold.
The hopper 111 of the present invention is provided with an electric frequency heating or an infrared radiation heating device on the outer wall thereof to heat the hopper 111 in a partitioned manner, and the temperature gradually increases in the direction approaching the raw material distributor 1 b. The raw material distributor 1b comprises a feed inlet connected with the hopper 111, and a first discharge outlet and a second discharge outlet respectively connected with the first reaction kettle 2 and the second reaction kettle 3; a damper 12a is provided between the inlet and the hopper 111.
Specifically, the damper 12a is connected to the hopper 111 and the raw material distributor 1b via flanges, respectively, and a metal graphite gasket is further provided between the damper 12a and the hopper 111 and between the damper 12a and the raw material distributor 1 b. The inner diameter of the damper 12a gradually decreases in the direction from the hopper 111 to the raw material distributor 1 b. The raw materials are introduced in a spray state by increasing the pressure when they pass through the damper 12a and by introducing the raw materials into the second reaction vessel 3 of the first reaction vessel 2 through the raw material distributor 1 b.
As shown in fig. 3, the raw material distributor 1B is a feeder for feeding raw materials in a fixed direction (timing unidirectional feeding in the direction of fig. 3, a or B), and when the connected reaction vessel (for example, the first reaction vessel 2) is placed with a carbon empty barrel in the ready state, the supply of raw materials to the connected reaction vessel (for example, the second reaction vessel 4) is stopped, and the raw material distributor 1B automatically changes the feeding direction a to enable the feeding of raw materials to the reaction vessel to start to enter the reaction state. At this time, the reaction kettle in the direction B enters into a carbon baking device, and after the raw materials in the reaction kettle are completely reacted in a timing time, all the raw materials are changed into carbon powder, a carbon discharging device is automatically started to discharge carbon, and after the reaction kettle is cleared, the reaction kettle in the direction A stops feeding, and the reaction kettle in the direction B is fed. The raw material distributor 1b ensures the turnover feeding of two (or more than 2) reaction kettles and ensures the continuous feeding of equipment.
As shown in fig. 1 and 4, check valves are provided on the feed lines of the raw material distributor 1b and the first and second reaction kettles 2 and 3. Only feeding is allowed, and reverse feeding cannot be performed (oil gas is prevented from returning to a feeding system, material backflow is prevented, and feeding cannot be performed).
In the invention, the first reaction kettle 2 and the second reaction kettle 3 have the same structure and both comprise: a central shaft 21 arranged in the kettle body, a driving component 22 positioned on the kettle body and used for driving the central shaft 21 to rotate, a distributing plate 23 arranged on the central shaft 21, a film forming blade 24 and a scraping plate; the joint of the driving component 22 and the kettle body is provided with a mechanical seal 25. The distributing plate 23 is spaced from the inner wall of the kettle body, and the scraping plates are arranged on the inner wall of the kettle body close to the distributing plate 23. The film forming blade 24 is located below the distributing plate 23 and the scraper.
Specifically, the reaction kettle is driven to rotate through a driving component 22, specifically, the driving component comprises a motor with frequency conversion, the motor drives a central shaft 21 to rotate through a coupler, a mechanical seal 25 (high-temperature-resistant and leakage-proof) is arranged below the coupler, circulating water is used for cooling the inside of the mechanical seal 25, the protection seal is normal, and the temperature is prevented from being transferred upwards. The upper part of the kettle body is provided with a hollow carbon-gas separation cavity, and a larger airflow stabilizing space is provided for oil gas to pass through so as to separate carbon powder from oil gas.
The raw materials are sprayed on the distributing plate 23 in a spraying mode after passing through the raw material distributor 1b, the distributing plate 23 rotates along with the central shaft 21 of the reaction kettle, a plurality of scraping plates are arranged on the inner wall of the reaction kettle around the distributing plate 23, the raw materials of the distributing plate 23 are scraped down on the film forming blades 24 rotating along with the shaft after encountering the scraping plates, a certain gap is set between the film forming blades 24 and the inner wall of the reactor, and a film is formed on the inner wall along with the rotation of the film forming blades 24. The outside of the reaction kettle is provided with an electric variable-frequency heating or infrared radiation heating device (zone heating), the temperature is increased from top to bottom in a zone, and the temperature regulation setting is set according to the requirement that raw materials enter the reaction kettle.
The first reaction kettle 2 and the second reaction kettle 3 are respectively provided with an oil gas outlet 26 connected with the first catalytic tank 4 and the second catalytic tank 6 and a carbon outlet 27 connected with the first carbon outlet 5 and the second carbon outlet 7. The film formed on the inner wall of the reaction kettle is gasified immediately due to the set temperature, and the oil gas rises upwards in the reaction kettle and enters the catalytic tank through the oil gas outlet 26. Carbon powder is arranged at the lower part of the reaction kettle. A carbon scraper is arranged at the lower part of the central shaft 21, so that carbon powder can be uniformly scraped into the carbon outlet 27.
As shown in fig. 4 and 6, the first catalytic tank 4 and the second catalytic tank 6 have the same structure, and each includes: the tank 41, a central rotating shaft 42 positioned in the tank 41, a coupler 43 positioned on the tank 41, and a driving motor 44 connected with the coupler 43. A mechanical sealing element is arranged between the coupler 43 and the tank 41, and an oil gas outlet pipe 45 is arranged at the top of the tank 41. The oil gas outlet pipe 45 of the first catalytic tank 4 is connected with the coil pipe 8, and the oil gas outlet pipe 45 of the second catalytic tank 6 is connected with the dust removing tower 10.
Referring to fig. 7 and 8, the coil pipe 8 is only cooled, the outside of the whole pipeline can be controlled at constant temperature, and the whole pipeline is automatically controlled at constant temperature by a temperature controller after a certain temperature is set. The dust removal tower 10 includes a first dust removal tower 101 and a second dust removal tower 102 that communicate with each other, the bottoms of the first dust removal tower 101 and the second dust removal tower 102 are connected to the first oil storage tank 9 through a pipeline, and the top of the second dust removal tower 102 is connected to the second oil storage tank 11 through a pipeline provided with a condenser 12.
Oil gas in the catalytic tank enters the tower through a tangent line and then centrifugally rotates, so that carbon powder taken away by a part and the tower bottom enter the first oil storage tank 9, and enter the first oil storage tank 9 through a pipeline after dust removal twice, and all the pipelines entering the first oil storage tank are provided with one-way valves, so that carbon powder and oil gas can only enter the first oil storage tank 9 and cannot return, and intercommunication oil gas between reaction kettles is prevented.
103 in fig. 7 is for being used for the oil gas intake pipe clearance ware, after the oil gas intake pipe used certain time, the inner wall had the carbon dust to pile up, the outside motor that is equipped with of intake pipe clearance ware, the multiunit synthetic blade is equipped with to the inside other end, the blade is stopped on the top of intake pipe in ordinary, do not influence the intake of intake pipe, when the carbon dust of oil gas pipe inner wall piles up, the clearance ware starts the motor, rotatory blade, simultaneously the blade stretches into along with the inlet pipe along with rotatory the inside to the catalytic tank gas outlet for oil gas pipe inner wall carbon dust clean up.
The outside of the first oil storage tank 9 and the second oil storage tank 11 adopts constant temperature control, after a certain temperature is set, the automatic constant temperature control is realized by a temperature controller, a plurality of condensers 12 on a pipeline between the first oil storage tank 9 and the second oil storage tank 11 can be arranged, after cooling for many times, oil in oil gas is completely changed into liquid, and the rest cannot be changed into oil gas, which is combustible gas. The remaining gas (combustible gas) which cannot be liquefied through the first and second oil tanks 9 and 11 is drawn into the combustible gas storage tank 14 through the compressor 13. The first and second oil tanks 9 and 91 are internally provided with a high frequency oscillator to store carbon powder in the bottom of the tank, and the bottom carbon powder is removed by a slag removal valve. After the oil is stored to a certain set height, the electronic valve is automatically opened to start the external oil pump to pump oil, when the oil level reaches a certain set low level, the electronic valve is closed to continue the oil storage, the above actions are automatically repeated, and the automatic oil pumping is ensured. When the gas pressure in the second gas storage tank 11 is higher than the set pressure, the compressor is automatically started to draw gas to the gas storage tank for storage, and when the pressure reaches the set low pressure, the compressor is automatically stopped, so that the action is automatically repeated.
Referring to fig. 1 and 5, the first carbon dispenser 5 and the second carbon dispenser 7 have the same structure, and each of them includes an electric valve 52 disposed at the carbon outlet 27, an electric slide rail 53, a carbon-out driving motor 54 disposed on the electric slide rail 53, a carbon-out screw 55 connected to the carbon-out driving motor 54, a carbon outlet tube 56 disposed at the periphery of the carbon-out screw 55, and a carbon powder cooling barrel 57 disposed below the carbon outlet tube 56. The toner cooling tub 57 is provided with a stirring device 58. The toner cooling tub 57 includes a first tub wall and a second tub wall having a space in which circulating water cooling is provided. The carbon powder cooling barrel 57 is provided with a carbon release valve 571 at the lower end, and the carbon release valve 571 is connected to the closed carbon storage barrel 59 through an auger pipeline.
When carbon powder is uniformly scraped into the carbon outlet 27 by the carbon scraper, the electric valve 52 of the carbon outlet is automatically opened, and the electric slide rail drives the carbon outlet driving motor 54 to move forwards, so that when the carbon outlet screw rod 55 extends into a set position in the carbon outlet 27, the carbon outlet driving motor 54 drives the carbon outlet screw rod 55 to rotate to discharge carbon, and the carbon powder enters the carbon powder cooling barrel 57 through the carbon outlet pipe 56. The carbon powder is connected with a carbon powder cooling barrel 57 through a carbon outlet pipe 56 by using a flange (the middle is prevented from flowing by using a high-temperature-resistant metal graphite gasket), and an air outlet valve 5-16 is opened before the carbon powder enters the carbon powder, so that air is discharged. The toner cooling barrel 57 includes a first barrel wall and a second barrel wall, which have a space, and a circulating water cooling is provided in the space to ensure that the internal toner is cooled to normal temperature in a set time. In order to ensure uniform cooling of the carbon powder in the carbon powder cooling barrel 57, a stirring device is arranged, the stirring device comprises an explosion-proof motor, the stirring shaft is driven to rotate through a shaft coupling, a plurality of stirring blades (different in length) are arranged on the stirring shaft, the upper part of the carbon powder cooling barrel and the stirring shaft are sealed by a mechanical seal (cooled by circulating water), and the carbon powder cooling barrel is connected by a flange (the middle of the carbon powder cooling barrel is prevented from flowing by a high-temperature-resistant metal graphite gasket). When carbon is discharged within the set time in the reaction kettle, the electric slide rail 53 acts reversely, so that the carbon discharge screw rod 55 exits the reaction kettle, and the electric valve 52 is closed. When the carbon powder cooling barrel 57 is cooled for a set time, the carbon valve 571 is automatically opened, and the carbon powder enters the closed carbon storage barrel through the dragon for storage.
According to the waste plastic treatment equipment, in the reaction process of the reaction kettle, oil gas, carbon powder and other particles can be effectively separated, so that the purity of subsequent oil refining is improved, and meanwhile, the oil refining efficiency is improved. In addition, the structural arrangement between the reaction kettle and the catalytic tank enables the reaction to be more sufficient, and the oil gas conversion rate is improved.
According to the waste plastic treatment equipment, before the oil gas enters the first oil storage tank 9, the oil gas enters the dust removal tower, so that the separation of the oil gas and carbon powder can be further realized, and the separation precision is ensured.
According to the waste plastic treatment equipment, the electric valve is arranged at the carbon outlet 27, and the carbon outlet screw rod is extended into the carbon outlet to carry out carbon outlet operation when carbon outlet is needed.
The waste plastic treatment equipment disclosed by the invention is used for treating waste plastic to form separated carbon powder, oil and combustible gas, so that the pollution is prevented and the production energy is realized.
The above description is only one embodiment of the present invention, and is not intended to limit the present invention, but various modifications and variations can be made to the present invention by those skilled in the art. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present invention should be included in the protection scope of the present invention.
Claims (9)
1. A waste plastic treatment apparatus, comprising:
the feeding unit (1) comprises a propeller (1 a) and a raw material distributor (1 b) which is positioned at the tail end of the propeller (1 a) and connected with the propeller;
the device comprises a first reaction kettle (2) and a second reaction kettle (3), wherein the first reaction kettle (2) and the second reaction kettle (3) are respectively connected with a raw material distributor (1 b) through a feed pipeline, and the raw material distributor (1 b) is used for conveying raw materials to the first reaction kettle (2) and the second reaction kettle (3) at regular intervals;
the device comprises a first catalytic tank (4) and a first carbon outlet device (5), wherein the first catalytic tank (4) is connected with one end of a first reaction kettle (2), and the first carbon outlet device (5) is connected with the other end of the first reaction kettle (2);
the second catalytic tank (6) and the second carbon outlet device (7), wherein the second catalytic tank (6) is connected with one end of the second reaction kettle (3), and the second carbon outlet device (7) is connected with the other end of the second reaction kettle (3);
one end of the coil pipe (8) is connected with the top of the first catalytic tank (4) through an automatic control valve;
the first oil storage tank (9) is connected with the other end of the coil pipe (8);
the dust removal tower (10) is respectively connected with the top of the second catalytic tank (6) and the first oil storage tank (9);
the second oil storage tank (11) is connected with the first oil storage tank (9) through a pipeline, and a condenser (12) is arranged on the pipeline;
a compressor (13), the inlet end of which is connected with the second oil storage tank (11);
a flammable gas storage tank (14) connected to the outlet end of the compressor (13);
the first carbon outlet device (5) and the second carbon outlet device (7) have the same structure and comprise an electric valve (52) arranged at a carbon outlet (27), an electric sliding rail (53), a carbon outlet driving motor (54) arranged on the electric sliding rail (53), a carbon outlet screw rod (55) connected with the carbon outlet driving motor (54), a carbon outlet pipe (56) arranged at the periphery of the carbon outlet screw rod (55) and a carbon powder cooling barrel (57) arranged below the carbon outlet pipe (56);
a stirring device (58) is arranged in the carbon powder cooling barrel (57);
the carbon powder cooling barrel (57) comprises a first barrel wall and a second barrel wall, wherein the first barrel wall and the second barrel wall are provided with a space, and circulating water cooling is arranged in the space;
a carbon discharging valve (571) is arranged at the lower end of the carbon powder cooling barrel (57), and the carbon discharging valve (571) is connected to the closed carbon storage barrel (59) through a packing auger pipeline;
the propeller (1 a) comprises a hopper (111), a motor (112) positioned above the hopper (111), a stirring rod (113) with one end connected with the motor (112) and the other end extending into the hopper (111) and provided with a spiral material pressing plate, and a raw material conveying belt (114) positioned at one side of the hopper (111);
the motor (112) drives a belt pulley on a reduction gearbox through the belt pulley and a belt to drive the stirring rod (113) in the hopper (111) to rotate, and the bottom of the reduction gearbox is arranged on the cylindrical marble sliding block.
2. Waste plastic treatment plant according to claim 1, characterized in that the outer wall of the hopper (111) is provided with an electric frequency heating or an infrared radiation heating device for zone heating of the hopper (111), the temperature gradually increasing in the direction approaching the raw material distributor (1 b).
3. Waste plastic treatment plant according to claim 1 or 2, characterized in that the raw material distributor (1 b) comprises a feed inlet connected to the hopper (111) and a first discharge outlet and a second discharge outlet connected to the first reactor (2) and to the second reactor (3), respectively;
a damper (12 a) is arranged between the feeding hole and the hopper (111).
4. A waste plastic treatment plant according to claim 3, characterized in that the damper (12 a) is flanged to the hopper (111) and the raw material distributor (1 b) respectively, and that a metal graphite gasket is also provided between the damper (12 a) and the hopper (111), the raw material distributor (1 b);
the inner diameter of the damper (12 a) gradually decreases in the direction from the hopper (111) to the raw material distributor (1 b).
5. Waste plastic treatment plant according to claim 1, characterized in that the feed line is provided with a one-way valve.
6. Waste plastic treatment plant according to claim 5, characterized in that said first reactor (2) and said second reactor (3) are identical in structure, each comprising:
the device comprises a central shaft (21) arranged in a kettle body, a driving assembly (22) positioned above the kettle body and used for driving the central shaft (21) to rotate, a distributing plate (23) arranged on the central shaft (21), a film forming and blade (24) and a scraping plate;
a mechanical seal (25) is arranged at the joint of the driving assembly (22) and the kettle body;
the material dividing plate (23) is spaced from the inner wall of the kettle body, and the scraping plate is arranged on the inner wall of the kettle body close to the material dividing plate (23);
the film forming blade (24) is positioned below the distributing plate (23) and the scraping plate.
7. Waste plastic treatment device according to claim 6, characterized in that the first reaction kettle (2) and the second reaction kettle (3) are each provided with an oil gas outlet (26) connected to the first catalytic tank (4) and the second catalytic tank (6), respectively, and the carbon outlet (27) connected to the first carbon outlet (5) and the second carbon outlet (7), respectively.
8. Waste plastic treatment plant according to claim 1 or 7, characterized in that said first catalytic tank (4) and said second catalytic tank (6) are of identical construction, each comprising: the device comprises a tank body (41), a central rotating shaft (42) positioned in the tank body (41), a coupler (43) positioned on the tank body (41) and a driving motor (44) connected with the coupler (43);
a mechanical sealing element is arranged between the coupler (43) and the tank body (41);
an oil gas outlet pipe (45) is arranged at the top of the tank body (41).
9. Waste plastic treatment plant according to claim 8, characterized in that the oil gas outlet pipe (45) of the first catalytic tank (4) is connected to the coil (8), the oil gas outlet pipe (45) of the second catalytic tank (6) being connected to the dust removal tower (10);
the dust removing tower (10) comprises a first dust removing tower (101) and a second dust removing tower (102) which are communicated with each other, the bottoms of the first dust removing tower (101) and the second dust removing tower (102) are connected with a first oil storage tank (9) through pipelines, and the top of the second dust removing tower (102) is connected with a second oil storage tank (11) through a pipeline provided with a condenser (12); the first oil storage tank (9) and the second oil storage tank (11) are internally provided with a high-frequency oscillator (91).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010351935.XA CN111500305B (en) | 2020-04-28 | 2020-04-28 | Waste plastic treatment equipment |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010351935.XA CN111500305B (en) | 2020-04-28 | 2020-04-28 | Waste plastic treatment equipment |
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| CN111500305A CN111500305A (en) | 2020-08-07 |
| CN111500305B true CN111500305B (en) | 2024-02-20 |
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| CN114541450A (en) * | 2022-03-03 | 2022-05-27 | 北京中岩大地环境科技有限公司 | Barrier wall construction device and construction method thereof |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2006012800A1 (en) * | 2004-08-06 | 2006-02-09 | Hao Jiang | An apparatus for preparing oil from waste plastics in continuous and industrial production |
| JP2013103998A (en) * | 2011-11-14 | 2013-05-30 | Tossmic Kk | Waste plastic catalytic cracking liquefaction apparatus and catalytic cracking liquefaction method |
| CN106118707A (en) * | 2016-07-28 | 2016-11-16 | 徐效奇 | Waste plastics innocent treatment equipment and method |
| CN110358569A (en) * | 2018-04-10 | 2019-10-22 | 杭州润承新能源科技有限公司 | Waste plastic oil-refining equipment |
| CN212982883U (en) * | 2020-04-28 | 2021-04-16 | 徐宗胜 | Waste plastic treatment equipment |
-
2020
- 2020-04-28 CN CN202010351935.XA patent/CN111500305B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2006012800A1 (en) * | 2004-08-06 | 2006-02-09 | Hao Jiang | An apparatus for preparing oil from waste plastics in continuous and industrial production |
| JP2013103998A (en) * | 2011-11-14 | 2013-05-30 | Tossmic Kk | Waste plastic catalytic cracking liquefaction apparatus and catalytic cracking liquefaction method |
| CN106118707A (en) * | 2016-07-28 | 2016-11-16 | 徐效奇 | Waste plastics innocent treatment equipment and method |
| CN110358569A (en) * | 2018-04-10 | 2019-10-22 | 杭州润承新能源科技有限公司 | Waste plastic oil-refining equipment |
| CN212982883U (en) * | 2020-04-28 | 2021-04-16 | 徐宗胜 | Waste plastic treatment equipment |
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