KR20130022308A

KR20130022308A - Waste tire pyrolysis oil extraction equipment

Info

Publication number: KR20130022308A
Application number: KR1020110085548A
Authority: KR
Inventors: 최정열
Original assignee: 최정열
Priority date: 2011-08-26
Filing date: 2011-08-26
Publication date: 2013-03-06

Abstract

The present invention is a safer manufacturing apparatus through pyrolysis of waste tires and a device for making regenerated oil through heat reactor in the absence of oxygen. The waste tires are shredded to a suitable size. The heat of combustion is set to 450 ° -500 ° in the heat reactor. At this time, the reaction by heat starts (melting), and in the process, oil vapor is formed. 3. It passes through the oil condenser and is converted into regeneration oil. This oil, stored and stored, is transferred to the 6. refining tank and 1. regenerated oil is refined through the refining tank using this heat from the furnace. This refined oil is stored as 8.OIL TANK after 7. cooling process.
The steam generated during the pyrolysis process is condensed through the condensation cooling system, and the remaining waste gas is discharged through the waste gas separator, 1.burning and removing dioxin and harmful substances through the combustion furnace, and 2.passing through the thermal reactor. Through the blower, through the blower, and through the cleaning tower to filter dust and solids and release them into the atmosphere.
10. It is a cooling device that makes the thermal reactor from high temperature to low temperature after the thermal reaction is finished. It is an oil extraction equipment that is recycled through industrial waste.

Description

Waste Tire Pyrolysis Oil Extraction Unit {omitted}

The present invention relates to an apparatus for extracting regenerated oil from waste tires and to an apparatus for extracting regenerated oil which can be thermally decomposed and recycled as fuel.

Waste tires can be treated in an environmentally friendly manner without additional pollutant emissions to prevent environmental pollution.

The present invention is an apparatus for producing oil by pyrolyzing waste tires. Environmental waste (tire, synthetic resin) is a major cause of serious environmental pollution while providing convenience of use.

Ozone depletion due to rapid industrial development, ecological destruction due to global warming, global oil prices are on high march and no drop of oil This technology will be used to recycle waste tires that will protect the environment, reduce economic burden and be a new force. It is a recycling business

The present invention is an apparatus for regenerating oil by pyrolyzing environmental wastes, but various environmental pollutions caused by the use of tires, synthetic resins, and vinyl are generated. Waste tires and waste synthetic resin products are increasing in number, and only some of them are recycled and others are disposed of by incineration, landfilling, or other methods.

As there are many existing businesses that extract oil components because they are thermally decomposed with industrial waste (waste tires, waste synthetic resins), the initial investment costs are high and the technology is successful, but the productivity is low. A large amount of waste tires cannot be processed at one time, and the processing time is too long, which is an uneconomical problem.

When the high temperature pyrolysis in vacuum for pyrolysis (melting) of the waste tire, there are various problems such as cooling the high temperature with the risk of explosion.

Many companies have seen examples of technology success through the mass media, but after a while they are almost fading.

The pyrolysis method that can treat industrial wastes (waste tires and synthetic resins) that are pouring out even now is eco-friendly and can generate high heat, high efficiency fuels, bulk processing and renewable energy fuels. Can

The present invention has been developed to solve the above problems of the prior art, a method of inputting the waste tire and the flow to the heat of the heat reactor and the alternating operation of the two heat reactors using the waste tire heat is heat reactor In solving the explosion hazard and the high temperature cooling of the thermal reactor.

The present invention aims at maximizing throughput and maximizing throughput by crushing tires in pyrolysis of waste tires and putting them in a drawer-type container in a thermal reactor.

The heat entering the thermal reactor has conventionally been directed from bottom to top, but the invention is characterized by a shortening of time in making the best use of more deviating heat as the heat is directed from top to bottom. On the other hand, the technology is naturally designed to enable ring blow operation behind the thermal reactor, so it is designed to be safer without pressure on the thermal reactor.

According to the present invention as described above through waste pyrolysis

1.Effective in shortening time 2.Effective in continuous production

3. Increases oil extraction

The present invention minimizes environmental pollution, while maximizing renewable energy fuel extraction by pyrolyzing high carbonaceous materials contained in industrial waste tires.

1 is a front view of a waste tire pyrolysis apparatus according to the present invention.
Figure 2 is a front view of the thermal reactor of the waste tire of the present invention
Figure 3 is a cross-sectional view of the thermal reactor of the present invention
Figure 4 is a side view of the thermal reactor of the present invention.
(Symbol explanation)
1.combustion furnace 2.heat reactor
3.cooling device 4.waste gas separator
5.Oil Storage Tank 6.Refining Tank
7.chiller 8.heat exchanger
9. Air pollution prevention measures 10. Nitrogen cooling system
11.Oil Storage Tank 12.Ring Blower
13.Oil transfer pump 14.Blower
15.Water Pump 16.Ring Blower
4-1. Waste tire container 4-2. Castable-fireproof material
4-3.Cooler 4-4.Ceramic Fiber Gasket
2-1.2-2.2-3.2-4,2-5.2-6,2-7 Actuation Valve and Piping Flow Diagram

Hereinafter, the configuration according to the present invention in detail by the drawings as follows.

1 is a schematic diagram of pyrolysis of a tire. 2. Put waste tire into heat reactor. 12. Start ring blower. 14. Start blower.

1.In the combustion furnace, if the temperature is increased through the primary auxiliary burner, the thermal reaction (melting) starts in the thermal reactor, and the oil vapor generated by the vapor is formed through the cooling condenser. The waste gas condensed once more is returned to the furnace to become waste gas fuel.

In the furnace, dioxin, harmful substances, etc. are completely burned at 1000 degrees in the waste gas and recycled.

2. The process of getting heat into the heat reactor is divided into 2-1 upper part 2-2 middle part lower part. 12. Ring blower and 14. Blower ratio of air volume is 7: 3. % 9. The heat exiting the washing tower should preferably have a specific gravity of 30%.

The oil which has undergone the pyrolysis process is 13. Through the pump 6. The oil transferred to the refining tank 2. Through the first distillation using the heat from the heat reactor 1. The fuel in the combustion furnace and the remaining oil is Purification is done by a manufacturer-refined device

6.Refined heat from the refining tank 8.Cools the heat through the heat cooler 9.Paints the remaining dust and harmful substances through the air treatment facility (cleaning tower) and releases it to the atmosphere

In this way, when the waste tire pyrolysis operation is performed and operating oil vapor is reduced, the temperature of the combustion furnace is automatically dropped.

At this time, after one of the same two thermal reactors is finished, operate the valve in the combustion furnace to transfer the heat to the non-operating thermal reactor.

Once the thermal reactor is in operation, the incoming and outgoing heat flow is completely blocked. 2.The thermal reactor is cooled by 10. Nitrogen cooling system.

16. Nitrogen gas flows very finely and is recycled through the ring blower to make the thermal reactor as soon as possible.

At this time, if the temperature of the thermal reactor is less than 100 degrees, safety work is possible even if the door is opened.

The process proceeded in detail is described in Figure 2. The front and side views of the heat reactor is described, and the heat in the furnace is shown in Figure 1. The flow structure of the heat reactor piping is 2-1.2-2.2-3.2-4.2-5.2-6.2 It consists of -7 and 2-1.2-2.2-3 transfers heat to the heat reactor.

2-4.2-5 is a cooling device through liquefied nitrogen used to cool down the thermal reactor after operation, and when the thermal reaction (melting) starts in the thermal reactor, the flow path through which the vapor escapes to the bottom of the thermal reactor through 2-7.

Fig. 2.2The heat reactor is made of two doors, so the 4-1 waste tire container can be easily moved by using a forklift during the process of adding waste tires. Is conveniently configured to

3-1.11 locks and 4-1. The container is made to hold 8 waste tires and is made to improve efficiency.

Figure 3 is an internal front view. 4-2 is configured to increase thermal efficiency by thermally blocking the inner part of the thermal reactor, which is a fireproofing castable 25 mm. Also, the entire surface of the thermal reactor is made of castable fireproofing.

The purpose of 4-3 is to make a heat cooler form through a pipe, to heat the inside and outside, and to raise the internal temperature rapidly.

4-5 door seal through ceramic fiber gasket and tighten through 3-1

Figure 4.4-1 is a container for waste tires and the bottom is made of metalless net.

State that eight to ten petty container containers are also available.

The flow to the heat reactor temperature is gradually progressed from the top to the bottom, so 4-3 is configured with a heat cooler device to maximize the heat reactor temperature.

After passing through the thermal reaction (melting) process in this thermal reactor, the oil vapor moves naturally to the oil condensation and cooling system by the operation of the ring blower.

12. Located in the ring blower Located in the rear of the thermal reactor, the pressure of the thermal reactor. It is a safer tire oil extraction device because expansion is not formed and the risk of explosion disappears.

In addition, the present invention as described above is an advantage that can reduce the risk and obtain fuel at high efficiency compared to the prior art because it thermally decomposes waste resources.

Claims

Steam extraction from pyrolysis in the extraction of waste oil from waste tires 1.In the combustion furnace 2.Operation of two thermal reactors alternately Purification Method by Flow and Self Heat

The device of claim 1, which maximizes the heat transferred to the thermal reactor.
Pyrolysis device that transfers heat transfer from top to bottom

The method of claim 1 wherein the post-operation thermal reactor chiller