CN101824332A - Comprehensive utilization production equipment for renewable energy sources of waste plastics, tires and waste engine oil - Google Patents

Abstract

The invention discloses a production device for comprehensively utilizing renewable energy resources of waste plastics, tires and waste engine oil, which comprises main equipment, a second-stage device, a third-stage device, a cracking furnace tail gas treatment environment-friendly system, a combustible gas power generation recycling system, a hot gas recovery system and an environment-friendly high-energy low-sulfur coal system which are matched with each other, thereby providing a whole set of production equipment for comprehensively utilizing renewable resources of the waste plastics, the tires and the waste engine oil.

Description

Production equipment for comprehensive utilization of renewable energy from waste plastics, tires, and waste engine oil

technical field

The invention discloses a set of production equipment for comprehensive utilization of renewable energy for waste plastics, tires, and waste engine oil. In particular, all kinds of substances produced by the equipment during the entire production process are directly converted to all remaining slag, gas, and water through the interconnection system of the equipment. All of these result in products with greater economic value.

Background technique

With the continuous development of the environmental protection industry, the practical application of environmental protection treatment has become increasingly commercialized, and the development of recycled resource utilization of waste plastics, tires, and waste engine oil has also become mature. However, most of these projects are currently in the single use and development. The remaining products in the recycling process have not been fully considered for recycling. For example: Taking a single waste plastic and tire refining equipment as an example, most of the equipment basically did not consider the real exhaust gas environmental protection treatment, nor did it consider the issue of hot gas recovery and reuse, and the safety and environmental protection treatment of rough and black oil refining residues It is an understatement or simply ignored. The combustible gas (non-toxic gas) produced in waste plastics and tire oil refining is only returned to the furnace for combustion, but in actual production, the time when the gas is produced and the time used for the combustion of the cracking furnace are two concepts, and the gas is returned to the furnace for combustion. During the time until the cracking is completed, only two-thirds of the gas will burn back, and the remaining combustible gas can only be discharged to the sky. From the above-mentioned environmentally friendly regeneration equipment, it is actually not environmentally friendly, and may cause serious damage to the environment again. The problem of secondary pollution and the waste of a large amount of economically valuable reusable resources are indeed a defect. The production equipment for the comprehensive utilization of renewable energy of the present invention generally includes a cracking catalytic furnace, which is a horizontal built-in and can rotate 360 degrees forward and reverse, and is equipped with an automatic random wall scraping type reactor, as the applicant first The applied patent application number is CN201010148298.2 and CN201010147465.1 mentioned in the application documents of the reactor wall scraper and a kind of horizontal waste plastics and tire pyrolysis furnace matched with it; meanwhile, the pyrolysis furnace body is connected with Exhaust gas environmental protection device system, such as the fuel cracking furnace exhaust gas treatment system mentioned in the application document of the applicant's previous patent application number CN201010168879.2; and a water scrubber with a double water seal safety device in order to ensure the safe movement of gas , the specific structure is mentioned in the patent application document CN200510037543.1 that the inventor applied for earlier and has been authorized; in addition, the heating method of the distillation catalytic tower used in the system equipment adopts the silicon controlled medium frequency heating method, The specific structure is mentioned in the patent application document CN200510101143.2 which was first applied by the inventor's direct subsidiary company; The patent application number of the application is already mentioned in the application documents of CN201010148172.5.

Contents of the invention

The purpose of the present invention is to solve the defects of the existing renewable environmental protection equipment, and provide a complete set of production equipment for the comprehensive utilization of renewable resources of waste plastics, tires, and waste engine oil. The circular development and utilization of gas and heat energy form a circular and environmentally friendly production chain with considerable economic value, which greatly changes the single function of existing equipment.

To achieve the above object, the present invention adopts the following technical solutions:

This production equipment for the comprehensive utilization of renewable energy from waste plastics, tires, and waste engine oil includes the main equipment, the second-level device, the third-level device, the environmental protection system for the tail gas treatment of the pyrolysis furnace, the reuse system for combustible gas power generation, and the hot gas Recovery system and environmentally friendly high-energy low-sulfur coal system.

The main equipment mentioned therein includes: starting from the conveyor belt, the petroleum product waste is transported to the pneumatic automatic feeder moved by the rail, and the raw material is pushed into the cracking catalytic furnace for cracking and catalysis to obtain an oil-gas mixture. The cracking catalytic furnace belt There is a reaction kettle with a scraper that is automatically and randomly set, and the furnace body is connected with a pyrolysis tail gas environmental protection device system, and then the sequence of subsequent equipment is a gas wax oil separator as the first separation of wax oil in the oil and gas produced by the cracking catalytic furnace The tool is connected in turn with the first-stage condenser, water-sealed gas-oil separator, water-sealed safety device, water-sealed negative pressure device, and heavy oil holding container. When the oil-gas mixture enters the mixed oil holding container through the horizontal condenser, The unliquefied combustible gas then enters the vertical gas neutralization water washer), the water washer is equipped with a double water seal safety device, and the combustible gas enters the reuse system of combustible gas power generation after being washed by the water washer.

The second-stage device includes a distillation catalytic tower. The distillate of this equipment comes from the mixed oil in the mixed oil holding container in the main equipment. The heating method of the distillation catalytic tower adopts a silicon controlled medium frequency heating method. There is an intermediate frequency heating The device is connected to the distillation catalytic tower. When the cracked waste plastic oil, tire oil or waste engine oil enters the distillation tower for treatment, it enters the vertical condenser according to the tangent of different gasification temperatures of various materials, and then passes through the water seal safety device, and then enters the diesel , Gasoline carrying container.

The third-level device is a diesel refiner gasoline degumming equipment, which starts from the first-level chemical decarburization and impurity removal synthesizer, and through the carbon removal and fine bleaching device, the dewaxing and degumming device, the second-level device The oil in the diesel and gasoline carrying container enters the dewaxing and degumming device through the input pipeline. The dewaxing and degumming device is a drum-conical agitator with a vertical baffle inside the agitator and an agitator at the bottom. Boiling device, the agitation flow is agitated in a tangential flow mode; the chemical agent device to be added is set in the additive container, and is divided into a chemical agent addition area and an alkaline liquid addition area, and the treated useful substances are then transported to the slag liquid Separator, the filter mesh of this machine is from 200 mesh to 350 mesh, and the filtered fluid is sent to the refined oil synthesis tank. The working form of this tank is divided into two stages of filtration. Directional filtration, the secondary filter layer is equipped with a filter medium bearing orifice plate, the filter medium is solid granular matter, the chemical additives to be added to the filtered material are placed in the additive container, and the oil obtained after the above treatment is qualified by inspection After entering the oil depot storage area, at the same time, the waste generated by each refining stage is transported to the environmental protection high-energy low-sulfur coal system by a special conveying device for reuse. The waste gas and waste odor generated by each refining stage pass through the water bath and the Activated carbon filter exhaust.

The lower ends of the decarbonization and impurity removal synthesizer, decarbonization fine bleaching device, and dewaxing and degumming device are all connected to the waste residue removal pipeline and sent to the environmental protection high-energy low-sulfur coal system by compressed air pressure, and are synthesized from the slag-liquid separator to the refined oil Additive containers are likewise arranged between the tanks.

The cracking furnace tail gas treatment environmental protection device system is connected with the smoke exhaust port of the thermal cracking furnace. The system includes an exhaust pipe with multiple water curtains. The exhaust port of the multiple water curtain exhaust pipes is connected to the combustion chamber of the furnace body. Equipped with a hot air water buffer chamber, the lower part of the buffer chamber is equipped with a double wet carbon particle filter, and the other end is connected to a double-tower wet gas-solid separator. The rear part of the water pipe, the water pipe uses the pressure of the air guide to push the water vapor into the chimney at the end of the equipment. The chimney is composed of three parts. The upper part of the heat exchanger is an exhaust pipe, and the middle part of the pipe is equipped with an alkaline water sprayer.

The combustible gas power generation and reuse system is connected to the gas pipeline in the main equipment, and the gas is compressed to 0.5MPA by a dedicated gas compressor and at the same time plays the role of dehydration of the first-stage gas, and then the gas is sent to the second-stage special gas Compressor, when this compressor compresses the gas to 1MPA and at the same time performs the second gas dehydration function, it sends the combustible gas to the gas storage container. The storage is equipped with two gas outlets, one of which leads to the heat of the main equipment The cracking furnace is used as the fuel of the furnace, and its gas is sent out through the second decompression. The first decompression is decompressed to 0.4-0.5MPA through the decompression equipment, and then the pressure is reduced from 0.4-0.5 MPA through the second decompression equipment. The MPA is reduced to 0.1-0.2MPA and sent to the furnace for combustion; the other gas outlet leads to the gas fuel generator (42), and its combustible gas passes through another decompression device to depressurize to 0.1-0.5MPA before entering the gas fuel Generator, generator adopts mechanical internal mixing method.

In the hot gas recovery system, the hot gas generated by the operation of the generator is collected through the gas-water exchanger. The gas-water exchanger adopts the heat conduction type of the heat conduction tube, and the heat transfer system of copper through the heat conduction tube is more than 1000 times The heat conducts to the circulating water, the hot water is sent to the wind cabinet by the heat pump, and then the hot air above 120 degrees is sent by the wind cabinet to the drying equipment of the environmental protection high-energy low-sulfur coal system through the hot air output pipe. The machine-heated air is then cooled by the heat exchanger and then discharged through the flue gas channel.

The heat conduction pipes are a plurality of vacuum heat pipes, a metal cooling wheel is arranged at one end of the vacuum heat conduction pipes, a smoke-water interlayer and an insulation layer are arranged between adjacent vacuum heat pipes, and one end of the air-water exchanger is arranged There is a hot gas introduction pipe and a muffler, a carbon dust cleaning port is provided at the bottom, and a sewage discharge port is provided at one end of the hot gas introduction pipe, and a circulating hot water pipe is used to connect the heat pump and the air-water heat exchanger. The heat exchange The air-water heat exchanger is installed at the opposite end of the sewage discharge port. The upper and lower ends of the heat exchanger are provided with a circulating cold water outlet, and the upper end is provided with a circulating cold water inlet. At the same time, this end is provided with a circulating hot water pipe and a wind cabinet. connected.

The environment-friendly high-energy low-sulfur coal system reuses waste plastics, waste tires, and the residue that cannot be gasified during the oil refining process, that is, coarse black carbon. It includes an artificial aging device for aging coarse carbon black, and then Treated in a hot steam processor, and then use the treated coarse carbon black as the main material, add compatible materials to it, the compatible materials are raw coal, ferrocene, hexamethylenetetraammonium, sodium hydroxide, quicklime and binder to form Coal-based material, wherein the weight percentage of the main material in the coal-based material is 45%-60%; then the coal-based material is made into finished coal, and the coarse carbon black is conveyed by the ground auger and the carbon black input belt .

Thus the invention has the following beneficial effects through the above technical scheme:

Integrating the individuality of the existing equipment, compared with the single environmental protection production concept of the existing single technology, can effectively prevent the secondary pollution of the land and air environment caused by the residue after the environmental protection production, or because of the single environmental protection mode of production The more harmful pollution before; the system equipment of the present invention is a group of circular environmental protection production and recycling equipment, from the first environmental protection production to the remaining slag, harmful gas and high temperature gas for the second environmental protection production Reuse can play a real circular economic chain of waste environmental protection production, which may achieve or achieve no sewage discharge, no smoke and dust discharge, no room temperature discharge, no harmful gas discharge, no foul smell, no irritating odor discharge, low noise, self-produced Good beneficial effect of energy recycling.

Description of drawings

Figure 1 is an overall diagram of the production equipment for the comprehensive utilization of renewable energy such as waste plastics, tires, and waste engine oil.

FIG. 2 is a front view of the main device in FIG. 1 .

Figure 3 Another view of the main device in Figure 2.

FIG. 4A is a cross-sectional view of the reactor shown in FIG. 1 .

Fig. 4B is a cracking furnace diagram coordinated with Fig. 4A.

Fig. 5 is a diagram of gasoline degumming equipment for a diesel refiner in the third stage.

Figure 6 is a system diagram of an environmental protection device for cracking furnace tail gas treatment.

Figure 7 is a diagram of the chimney in Figure 6 .

Figure 8 is a diagram of the hot gas recovery system.

Fig. 9 is a diagram of a combustible gas power generation and reuse system.

Figure 10 is a system diagram of environmentally friendly high-energy low-sulfur coal.

Detailed ways

The present invention will be further described below in conjunction with the accompanying drawings.

As shown in Figures 1 to 10, the production equipment for the comprehensive utilization of renewable energy for waste plastics, tires, and waste engine oil includes cooperating main equipment, second-level devices, third-level devices, cracking furnace tail gas treatment environmental protection systems, Combustible gas power generation reuse system, hot gas recovery system, and environmentally friendly high-energy low-sulfur coal system.

The main equipment described therein includes: starting from the conveyor belt 2, the petroleum product waste is transported to the pneumatic automatic feeder 1 moved by the rail, and the raw material is pushed into the cracking catalytic furnace 3 for cracking and catalysis to obtain an oil-gas mixture. The catalytic furnace is equipped with a reactor 5 with scraper 4 which is automatically and randomly arranged, and the furnace body is connected with a pyrolysis tail gas environmental protection device system, and then the sequence of subsequent equipment is a gas wax oil separator 6 as the gas produced by the cracking catalytic furnace. The first separation tool for wax oil in oil and gas is connected in turn with the first-stage condenser 7, water-sealed gas-oil separator 8, water-sealed safety device 9, water-sealed negative pressure device 10, and heavy oil holding container 11. When the oil-gas mixture Enter the mixed oil holding container 13 through the horizontal condenser 12, and the unliquefied combustible gas then enters the vertical gas neutralization water washer 14, which is equipped with a double water seal safety device 15, and the combustible gas enters after being washed by the water washer. Reuse system for combustible gas power generation.

The second-stage device includes a distillation catalytic tower 16. The distillate of this equipment comes from the mixed oil in the mixed oil holding container 13 in the main equipment. The heating method of the distillation catalytic tower adopts a silicon controlled medium frequency heating method. There is a The intermediate frequency heating device 17 is connected to the distillation catalytic tower. When the cracked waste plastic oil, tire oil or waste engine oil enters the distillation tower for treatment, it enters the vertical condenser 18 according to the tangent of different gasification temperatures of various materials, and then passes through the water seal for safety. Device 19, enters firewood, gasoline carrying container 20.

Described tertiary device is diesel oil refiner gasoline degumming equipment, and this equipment is starting point by first-stage chemical decarburization and impurity removal synthesizer 21, through decarbonization fine bleaching device 22, dewaxing degumming device 23, described first The oil in the diesel and gasoline holding container 11 in the secondary device enters the dewaxing and degumming device through the input pipeline. There is an agitating boiling device at the bottom, and the agitation flow pattern is agitated in a tangential flow mode; the chemical agent device to be added is arranged in the additive container 24, and is divided into a chemical agent addition area and an alkaline liquid addition area. It is then transported to the slag-liquid separator 25. The filter mesh of this machine is from 200 mesh to 350 mesh. The filtered fluid is sent to the refined oil synthesis tank 26. The working form of this tank is separated into two stages of filtration, and the first stage is reverse pressurization Filtration, the second stage is forward filtration, and the filter layers of this second stage are all provided with filter medium bearing orifice plates, and its filter medium is solid granular matter, and the chemical agent additive to be added to the filtered object is placed in the additive container 24, through the above After the treatment, the oil products obtained pass the inspection and enter the storage area of the oil depot. At the same time, the waste generated by each refining stage is transported to the environmental protection high-energy low-sulfur coal system by a special conveying device for reuse. The waste gas and waste odor generated by each refining stage are passed through The dedicated exhaust pipe is discharged through the water bath and activated carbon filter.

The lower ends of the decarbonization and impurity removal synthesizer 21, the decarbonization and fine bleaching device 22, and the dewaxing and degumming device 23 are all connected to the waste slag removal pipeline 49 and sent to the environmental protection high-energy low-sulfur coal system by compressed air 50. An additive container 24 is also arranged between the machine and the refined oil synthesis tank 26 .

Described pyrolysis furnace tail gas treatment environmental protection device system is connected with the exhaust outlet of thermal cracking furnace, and this system includes the exhaust pipe 27 with multiple water curtain, and the exhaust port of this multiple water curtain exhaust pipe is connected with furnace body combustion chamber, A hot air water buffer chamber 28 is installed in the middle, and a double wet carbon particle filter 29 is installed at the lower part of the buffer chamber. The other end is connected to a double-tower wet gas-solid separator 30. The pipe is connected to the rear part of the water pipe of the air inducer, and the water pipe uses the pressure of the air inducer to push the water vapor into the chimney 32 at the end of the equipment. The chimney is composed of three parts, and the lower part is the water and gas separator 33 of the drum tank. The middle part is a heat exchanger 34 for gas phase separation, the upper part is an exhaust pipe 35, and an alkaline water sprayer 36 is installed in the middle part of the pipe.

The combustible gas power generation and reuse system is connected to the gas pipeline 37 in the main equipment, and the gas is compressed to 0.5MPA by a dedicated gas compressor and at the same time plays the role of dehydration of the first-stage gas, and then the gas is sent to the second-stage dedicated Gas compressor 38, which compresses the gas to 1MPA and dehydrates the gas for the second time, and sends the combustible gas to the gas storage container 39. The storage is provided with two gas outlets, one of which leads to the main body The thermal cracking furnace of the equipment is used as the fuel of the furnace, and its gas passing method is to send out through the second decompression, the first decompression is to depressurize to 0.4-0.5MPA through the decompression device 40, and then pass through the second decompression device 41 is reduced from 0.4-0.5MPA to 0.1-0.2MPA and sent to the furnace for combustion; the other gas outlet leads to the gas fuel generator 42, and the method of passing the combustible gas is to reduce the pressure to 0.1-0.5MPA by another decompression device Entering the gas fuel generator, the generator adopts a mechanical internal mixing method.

In the hot gas recovery system, the hot gas generated by the generator 42 is collected through the gas-water exchanger 43. The gas-water exchanger adopts the heat conduction type of the heat pipe, and the copper heat transfer system is used through the heat pipe 51. More than 1000 times the heat conduction to the circulating water, the hot water is sent to the air cabinet 45 through the heat pump 44, and then the air cabinet sends the hot air above 120 degrees to the drying equipment of the environmental protection high-energy low-sulfur coal system through the hot air output pipe 62. After the heat exchanged generator hot air is cooled by the heat exchanger 46 , it is discharged through the flue gas channel 63 .

The heat conduction pipes are several vacuum heat pipes 51, a metal heat dissipation gun 54 is arranged at one end of the vacuum heat conduction pipes, and a smoke-water interlayer 55 and an insulation layer 64 are arranged between adjacent vacuum heat pipes. One end of the exchanger 43 is provided with a hot gas introduction pipe 52 and a muffler 53, the bottom is provided with a carbon dust cleaning port 56, and one end of the hot gas introduction pipe is provided with a sewage discharge port 57, and a circulating hot water pipe 58 is used to connect the heat pump 44 and The air-water heat exchanger 43, the heat exchanger 46 is arranged at the other end of the air-water heat exchanger opposite to the sewage discharge port, the upper and lower ends of the heat exchanger are provided with a circulating cold water outlet 59, and the upper end is provided with a circulating cold water outlet Inlet 60, meanwhile, this end is connected with wind cabinet by being provided with circulating hot water pipe 61.

The environment-friendly high-energy low-sulfur coal system reuses waste plastics, waste tires, and residues that cannot be gasified during the oil refining process, that is, coarse black carbon, and includes an artificial aging device 47 for aging coarse carbon black. After being treated by the hot steam processor 48, the treated coarse carbon black is used as the main material, and compatible materials are added therein, and the compatible materials are raw coal, ferrocene, hexamethylenetetraammonium, sodium hydroxide, quicklime and binder , forming a coal base material, wherein the weight percentage of the main material in the coal base material is 45%-60%; then the coal base material is made into finished coal, and the coarse carbon black passes through the ground auger 64 and the carbon black The input belt 65 conveys.

In the specific production and utilization process, in the first stage, after the waste plastics with a water content of 40% are dried by hot air drying equipment, the water content is reduced to 20%. The hot air comes from the hot air recovery system in Figure 8, and the specific collection The work is processed by the thermal energy collector 66, and the waste plastics after drying are continuously sent to the pyrolysis furnace 3 through the conveyor belt, and the feeding amount is 14 tons (calculated by two furnaces). From the beginning of heating to the completion of cracking, the fuel oil used 1100Kg, the additional materials are catalysts such as aluminum, zinc and calcium oxide, the proportion of which is 1.5% of the weight of the added raw materials after dehydration, the power consumption of the equipment is 336 degrees, the production cycle time is 28 hours, and the production of gas and diesel mixed oil is 11.62 tons, and the pyrolysis residue is 60Kg of crude carbon black. This crude carbon black, together with the wet carbon powder collected in the tail gas environmental protection treatment system of the thermal cracking furnace, is sent to the high-energy low-sulfur coal production system for reuse, and at the same time through the refining process The combustible gas produced is about 872m ³ , the combustible gas Co20-24%, carbon dioxide Co21-3%, hydrogen H28-12%, and CmHn are mainly methane 3-4.2%, etc. The combustible gas is cleaned and detarred and compressed into The gas storage container 39 is used for gas power generation.

In the second stage, the cracked mixed oil enters the second-stage device. The daily processing capacity of the system is 14 tons. The heating tool of the device is a 110KW thyristor intermediate frequency heating equipment. Need electricity 750 degrees.

In the third stage, after being treated by the second-stage device, the diesel and gasoline in the distillate are sent to the refining device for processing. After cleaning, deodorization, decolorization, degumming, dewaxing and other processes, the total amount of diesel and gasoline obtained is 10.67 tons , Diesel oil can reach National II standard after treatment and synthesis. Gasoline is 93# gasoline. The residues in the processing process are alkalized and sent to the high-energy low-sulfur coal production system for reuse by using fully sealed transportation tools. deal with.

In the fourth stage, the combustible gas output from the gas storage container enters the internal mixing gas generator after decompression. Specifically, the 500KW/h product of Jinan Diesel Generator Factory can be used. The 872m ³ of the above-mentioned second stage treatment The combustible gas can generate electricity at 3925 degrees. The hot gas generated during the power generation process is converted into hot air through the heat recovery and reuse system, and the remaining hot water from the tail gas treatment of the pyrolysis furnace is converted into hot air and sent to the initial stage of the first stage. Hot air drying equipment for reuse.

This implementation takes oil refining of waste plastics as an example, and all those with the same or similar principle and basic structure as this embodiment are within the protection scope of the present invention.

Compared with the existing technology, the individuality of the existing equipment is integrated, compared with the single environmental protection production concept of the existing single technology, it can effectively prevent the secondary pollution caused by the residue after the environmental protection production to the land and air environment, Or because of the more harmful pollution before the production of a single environmental protection method; the system equipment of the present invention is a group of recycling environmental protection production and recycling equipment, from the first environmental protection production to the recycling of residual slag and harmful gases and high-temperature gases For the second environmental protection production reuse, it can play a real circular economic chain of waste environmental protection production, and may achieve or achieve no sewage discharge, no smoke and dust discharge, no room temperature discharge, no harmful gas discharge, no foul smell, no irritating smell Good beneficial effects of emission, low noise, self-generated energy recycling.

Claims (10)

1. equipment is produced in the comprehensive utilization of the renewable energy resources of a waste or used plastics, tire, used oil, it is characterized in that: what comprise the main equipment that cooperatively interacts, second stage device, three-pole device, pyrolyzer vent gas treatment environment friendly system, inflammable gas generating utilizes system, hot gas recovery system and environment-friendly and high-energy low sulphur coal system again.

2. waste or used plastics as claimed in claim 1, tire, equipment is produced in the renewable energy resources comprehensive utilization of used oil, it is characterized in that: wherein said main equipment comprises: by conveying belt (2) is starting point, the petroleum products waste is transported to the air pressure type automatic feeding machine (1) that moves by rail, advance cracking and catalyzing stove (3) to carry out cracking and catalyzing raw material and obtain gas-oil mixture, there is an automated randomized reactor (5) of scraping wall cutter (4) in this cracking and catalyzing furnace zone, body of heater is connected to cracking tail gas environmental protecting device system simultaneously, with after level equipment produced in the oil gas wax oil separating tool first for gas wax oil separator (6) conduct by the cracking and catalyzing stove in proper order, be connected with first step condenser (7) again in turn, hydrolock oil separator (8), water seal security device (9), hydrolock negative pressure device (10), heavy oil carrying container (11), when gas-oil mixture enters mixing oil carrying container (13) through horizontal condenser (12), the inflammable gas of failing to liquefy enters in the vertical combustion gas and water scrubber (14) thereupon, this water scrubber is set up double seal security device (15), and what inflammable gas entered the inflammable gas generating after water scrubber washing utilizes system again.

3. waste or used plastics as claimed in claim 1, tire, equipment is produced in the renewable energy resources comprehensive utilization of used oil, it is characterized in that: described second stage device comprises distillation catalytic tower (16), the distilland of this equipment comes from the mixing oil in the mixing oil carrying container (13) in the main equipment, the type of heating of distillation catalytic tower adopts the silicon controlled rectifier intermediate frequency heating method, there is a frequency heating device (17) to link to each other with the distillation catalytic tower, waste or used plastics oil after cracking, tire oil or used oil enter distillation tower and handle the back and enter vertical (type) condenser (18) again through water seal cut out (19) according to the tangent line of the different gasification temperatures of various materials, enter bavin, gasoline carrying container (20).

4. waste or used plastics as claimed in claim 1, tire, equipment is produced in the renewable energy resources comprehensive utilization of used oil, it is characterized in that: described third stage device is the concise and gasoline degumming equipment of diesel oil, this equipment is starting point by first step chemistry decarburization removal of impurities synthesizer (21), float device (22) through removing carbon, dewaxing removes glue device (23), bavin in the device of the described second stage, oil product in the gasoline carrying container (20) enters this dewaxing through input channel and removes the glue device, it is drum taper agitator that this dewaxing removes the glue device, stir to be provided with in the device and stand to baffle plate, the bottom is provided with agitates the boiling device, stirs flow pattern and stirs to cut stream mode; The chemical agent device of required interpolation is arranged in the additive container (24), and be divided into that chemical agent adds the district and alkaline liquid adds the district, useful thing after treatment is transported to dreg-liquid separator (25) again, this machine filter order is from 200 order to 350 orders, be transported to refining oil synthesis tank (26) through filterable fluid, the working forms of this jar separates cascade filtration, the first step is that reverse plus-pressure filters, the second stage is for forward filtering, the filtering layer of this secondary is provided with filtration medium carrying orifice plate, its filtration medium is the solid particulate thing, being filtered thing will add the chemical agent additive and place in the additive container (24), after gained oil product after the above processing is qualified on inspection, enter the oil depot storage area, simultaneously be delivered to environment-friendly and high-energy low sulphur coal system by special transfer device and utilize again, through the waste gas that each refining stage produced by the waste material that each refining stage produced, useless flavor is discharged by sea water bath and charcoal filter through the dedicated vent pipes road.

5. equipment is produced in the renewable energy resources comprehensive utilization of waste or used plastics as claimed in claim 4, tire, used oil, it is characterized in that: described decarburization removal of impurities synthesizer (21), remove carbon and float device (22), dewaxing and remove glue device (23) lower end and all connect waste residue and get rid of pipeline (49) and adopt pressurized air (50) force feed, be provided with additive container (24) equally between the refining oil synthesis tank (26) at dreg-liquid separator toward environment-friendly and high-energy low sulphur coal system.

6. waste or used plastics as claimed in claim 1, tire, equipment is produced in the renewable energy resources comprehensive utilization of used oil, it is characterized in that: described pyrolyzer vent gas treatment environmental protecting device system links to each other with the smoke outlet of pyrocrack furnace, this system includes and is with multiple cascade gas exhaust duct (27), the venting port of this multiple cascade gas exhaust duct connects combustion chamber of furnace body, hot gas water surge chamber (28) is equipped with in the centre, dual wet carbon granules strainer (29) is equipped with in the surge chamber bottom, the other end connects double tower type wet type gas-solid separator (30), the gas-solid separator tail end is by pipe connection air inducing device (31), the lower end is by the rear section water pipe of pipe connection air inducing device, aqueduct utilizes the pressure of air inducing device aqueous vapor to be pushed the chimney (32) of equipment afterbody, chimney is made up of three parts, the bottom is the moisture separator (33) of drum tank-like body, in for being used for the heat exchanger (34) of gas phase separation, top is gas exhaust duct (35), and alkaline water liquid spray thrower (36) is equipped with at this pipeline middle part.

7. waste or used plastics as claimed in claim 1, tire, equipment is produced in the renewable energy resources comprehensive utilization of used oil, it is characterized in that: the generating of described inflammable gas utilizes system to be connected in gas pipeline (37) in the main equipment again, when special-purpose gas compressor is reduced to gas pressure 0.5MPA and plays first step combustion gas dehydration simultaneously, again gas is delivered to the special-purpose gas compressor (38) in the second stage, this compressor is compressed to combustion gas 1MPA again when playing for the second time the combustion gas dehydration simultaneously, inflammable gas is delivered to combustion gas storage vessel (39), holder is provided with two air outlets, an air outlet leads to the fuel of the pyrocrack furnace of main equipment as this stove, its gas is to send through the secondary decompression by method, decompression for the first time is through pressure regulating equipment (40) 0.4-0.5MPA that reduces pressure, and reduces to 0.1-0.2MPA through second pressure regulating equipment (41) by 0.4-0.5MPA again and delivers to the burner hearth burning; Another air outlet leads to gaseous fuel generator (42), and its inflammable gas is to enter gaseous fuel generator after another pressure regulating equipment reduces pressure 0.1-0.5MPA again by method, and generator adopts the mode of mixing in the machinery.

8. waste or used plastics as claimed in claim 1, tire, equipment is produced in the renewable energy resources comprehensive utilization of used oil, it is characterized in that: described hot gas recovery system is collected hot gas by air-water interchanger (43) by the red-hot gas that generator (42) work operation is produced, this air-water interchanger adopts the heat pipe heat-conducting, the heat pipe that passes through (43) with the heat transfer coefficient of copper more than 1000 times heat conduction to recirculated water, hot water is delivered to wind cabinet (45) through heat pump (44), by warm air output tube (62) the above warm air of 120 degree is delivered to the drying plant utilization of environment-friendly and high-energy low sulphur coal system again by the wind cabinet, the generator warm air of the heat exchange of passing through after heat exchanger (46) cooling, is discharged through gas flue (63) again.

9. waste or used plastics as claimed in claim 8, tire, equipment is produced in the renewable energy resources comprehensive utilization of used oil, it is characterized in that: described thermal conductive pipe is some vacuum thermal pipes (51), be provided with heat dissipation metal wheel (54) at vacuum heat-conduction Guan Yiduan, between adjacent vacuum thermal pipe, be provided with cigarette water interlayer (55) and thermal insulation layer (64), described air-water interchanger (43) one ends are provided with hot gas inlet tube (52) and sourdine (53), the bottom is provided with carbon dust cleaning mouthful (56), and be provided with Sewage outlet (57) at the end that the hot gas inlet tube is set, and circulating hot water pipe (58) is in order to connect heat pump (44) and air-water heat exchanger (43), what described heat exchanger (46) was arranged at the air-water heat exchanger is oppositely arranged the Sewage outlet the other end, this heat exchanger upper and lower ends is provided with circulating water outlet (59), the upper end is provided with circulating water inlet (60), and this end links to each other with the wind cabinet by being provided with circulating hot water pipe (61) simultaneously.

10. waste or used plastics as claimed in claim 1, tire, equipment is produced in the renewable energy resources comprehensive utilization of used oil, it is characterized in that: described environment-friendly and high-energy low sulphur coal system is with plastic waste, damaged tire, in the oil refining process the promptly thick black carbon of the recrement that can not gasify utilize again, include thick carbon black is carried out aged preaging device (47), handle through heat steam treater (48) again, the coarse carbon black that to handle is as major ingredient again, add the compatibility material therein, the compatibility material is a raw coal, ferrocene, six methynes, four ammoniums, sodium hydroxide, unslaked lime and cakingagent, form coal-based material, wherein major ingredient shared weight percent in coal-based material is 45%-60%; Then coal-based material is made readymade coal.

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