KR200208460Y1 - an automatic product system of a carbide &a manutacturing process - Google Patents

Abstract

The present invention utilizes various organic and inorganic materials as well as general and industrial wastes, which are the main culprit of environmental pollution, and performs excellent functions such as environmental purification, crop growth promotion, deodorization, and antibacterial deodorization. Materials that produce carbides (charcoal) and at the same time that carbides are not produced are those devices that can be disposed of without causing any harm to the environment, such as pollution.

That is, the drying section 10a and the pyrolysis section 10b, the cooling section and the moving section 11c are separated, and the outer surface portion is surrounded by the screw right wall 11, the screw right 10 in a sealed state is the power unit In the raw material to be introduced while rotating at a constant speed by the power received in (1), while drying the introduced raw material to the screw right 10, and dried through the primary drying section (10a), the second 800 ~ 850 ℃ The pyrolysis may proceed in the pyrolysis section 10b for 1 hour and 30 minutes in a high temperature and anoxic or low oxygen atmosphere, and the pyrolyzed carbides may be moved at the same time as the third cooling to recover the carbides.

Description

An automatic product system of a carbide & a manutacturing process

The present invention relates to an automatic carbide manufacturing apparatus, and more specifically, it is excellent in promoting environmental purification, crop growth, deodorization, and antibacterial deodorization by using general and industrial wastes, which are the main causes of environmental pollution, along with various organic and inorganic materials. The present invention relates to a device that performs a function, and in particular, produces a carbide (charcoal) used for various heat sources, and at the same time, a material in which carbide is not produced, without causing any harm to the environment such as pollution.

In general, carbides are heated to a high temperature (800 ~ 850 ℃) in an oxygen-free or low oxygen to produce a flammable gas, such as hydrocarbon methane, such as hydrogen methane, and the organic compounds such as liquid vinegar, acetone methanol Tar powder or oil content is generated, and chemical decomposition occurs into three groups of pure carbon, glass, metal, and earth and char. The combustible gas and liquid tar powder and oil content are generated. Except for the charcoal is made of high carbon (C) carbide of 70% to 80% of carbon, which includes non-burning glass, metal materials, earth and sand, etc., depending on the type of organic matter.

The above-mentioned carbide (charcoal) benefits to us because of too much known relationship will be omitted a detailed description.

On the other hand, waste is largely divided into general waste discharged from the home, industrial waste discharged from the industry, and specific waste containing specific components in a specific field, most of which are very expensive in incineration, reprocessing, landfilling, and the like. You will hear.

Therefore, in order to reduce these costs, some illegal activities such as illegal incineration and landfilling are prevalent, and it is very problematic for the disposal of medical wastes that may enter urban areas and infectious wastes. The method which is emerging as the most preferable method is studied in each layer by suggesting a method for producing carbide using pyrolysis.

Accordingly, the present invention is capable of producing carbides (charcoal) at the same time as appropriately solving various problems such as wastes that worsen the existing environment as described above, and proper temperature setting and oxygen-free or low oxygen (vacuum) required for carbide production. The condition must be maintained, and the flammable gas generated in the carbonization process, the tar and oil in the liquid phase must be properly treated, and the carbonization process can meet the conditions most suitable for its characteristics such as time and temperature according to the components of the organic material. With the main focus on doing, the technical task was completed.

1 is a schematic cross-sectional view showing a preferred embodiment of the present invention

Figure 2 is a side view showing a power unit provided by the present invention

3 is a cross-sectional view taken along the line A-A 'of FIG.

Figure 4 is a side cross-sectional view of the thermal chamber provided by the present invention

5 is a cross-sectional view taken along the line B-B 'of FIG.

Figure 6 is an enlarged cross-sectional view of the gas combustion device provided in the present invention

7 is a cross-sectional view showing another embodiment of the thermal chamber rear end of the present invention

□ Explanation of symbols for main parts of drawing □

1: power unit 2: reduction motor

2a, 3a, 3b, 4,4a, 5: sprockets 2b, 3b, 4b: chain

3: Reducer 10: screw

10a: dry section 10b: pyrolysis section

10c: cooling and moving section 11: screw wall

11a: Passing groove 12a: Cover plate

20: thermal chamber 21: combustion chamber

22: non-combustion chamber 23: partition

23a: Movement Route 24: Burner

25: refractory brick 30: guide

31: exhaust pipe 32: outflow pipe

40: gas combustion device 41: air jet

42: common barrel 43: gas injection hole

44: oil pipe 50: cooling water container

60: Communication 100: Loading container

100a: entrance 110: collecting container

120: opening and shutting 150: oxidation chamber

151: burner 152: outlet

153: inlet 154: carbide outlet

Figure 1 is a schematic cross-sectional view showing a preferred embodiment of the present invention, Figure 2 is a side view showing a power unit provided by the present invention, Figure 3 is a cross-sectional view taken along line AA 'of Figure 1, Figure 4 is the present invention Fig. 5 is a sectional view taken along line B-B 'of Fig. 4, Fig. 6 is an enlarged cross-sectional view of a gas combustion device provided by the present invention, and Fig. 7 is a fire chamber of the present invention. As a cross-sectional view showing another embodiment at the rear end, it will be described in detail the configuration and operation of the automatic carbide production apparatus and method provided by the present invention in this way.

Carbide formation is the solid carbide (charcoal) obtained after the organic or inorganic material is pyrolyzed in an oxygen-free or low-oxygen, ie vacuum atmosphere, after appropriate treatment of gaseous flammable gases, liquid tars, and oils. Contact with air (particularly oxygen) will oxidize completely, making it impossible to obtain carbides.

Therefore, the present invention seeks flammability, a gas generated during pyrolysis, during which the raw materials introduced in consideration of the characteristics of such carbide are moved for a predetermined time in an atmosphere of high oxygen-free or low oxygen (vacuum) state at 800 to 850 ° C. The gas is bypassed again and re-introduced into the gas combustion device 40 of the thermal chamber 20 to complete combustion, and at the same time, tar and oil are discharged and stored through the outlet 32 on one side, and then processed. After the pyrolysis process, only carbides (charcoal) are finally obtained through the recovery port 110a.

That is, the power unit 1 composed of a reduction ratio motor 2, a reduction gear 3, a sprocket 2a, 3a, 3b, 4, 4a, 5, a chain 2b, 3c, 4b, and the like on one side of the front side. The heat treatment chamber 20 is heat-treated with a refractory brick 25 in the inner surface at the inlet (100a) of the front upper end is provided with a pair of two driven by the power unit (1) And the penetrating through the cooling water tank 50 is installed to extend long to the upper portion of the recovery container 110 of the rear bottom, when the raw material is introduced from the inlet (100a) of the loading container 100 is divided into two stages of the screw ( 10) This is dried in the transfer process, the pyrolysis proceeds through the thermal chamber 20, is cooled while passing through the cooling water tank 50 is the final carbide is placed in the recovery tank 110. .

In the rough configuration as described above will be described in detail for each detailed configuration as follows.

The screw 10 is divided into two stages and the length is configured to extend from the raw material inlet 100 in the front to the recovery container 110 in the rear so that the two pairs side by side, the outer periphery of the screw 10 In order to completely block the screw right wall 11 of the metal body in the same shape as the outer shape of the screw 10 in the inside is kept completely sealed in a state holding only a constant GAP (?? 設) .

As described above, if the screw 10 is a raw material containing moisture, it is necessary to dry the drying section 10a necessary for drying and the pyrolysis section 10b, which is substantially thermally decomposed, and the cooling and moving section 10c. It is divided into three sections according to the density of screw blade pitch. That is, the drying section 10a has a slightly larger pitch for rapid progress, and the pyrolysis section 10b proceeds at a very slow speed (1 m in an atmosphere of 800 to 850 ° C. to allow complete pyrolysis to proceed, about 1 hour). The pitch is very dense as the material must proceed at very slow speeds, which can take up to 30 minutes.

In order to proceed at the speed as described above, the role of the power unit 1 is very important because the power to be transmitted while the appropriate reduction ratio is applied to the rotational power transmitted to the screw 10.

The power unit 1 is to set the reduction ratio so that the rotational speed of the screw 10 can be properly adjusted according to the length and outer diameter, pitch and length of the pyrolysis section of the screw right (10). These conditions are intended to allow carbides to stay for 1 hour to 2 hours per meter in the pyrolysis section 10b.

The thermal chamber 20 has a front wall formed of a refractory brick 25 having excellent heat resistance therein, and a combustion chamber 21 in which substantial thermal decomposition proceeds while the temperature is maintained at 800 to 850 ° C. by the combustion flame of the burner 24. ) And the non-combustion chamber 22 which can simultaneously serve as a moving mirror when discharged from the moisture and combustion gas generated by the drying of the material to the atmosphere at 200-300 ° C. at a somewhat lower temperature than the combustion chamber 21. ) Is separated from the combustion chamber 21 by the partition 23 having a constant moving path 23a in the refractory brick dual structure.

As shown in FIG. 4, a considerable combustible gas may be generated when raw material introduced in the screw right wall 11 in which the screw 10 is installed is thermally decomposed, which may be polluted. As shown in FIG. 3, a pair of contacting portions, ie, screwwoos, which are positioned when installed in the combustion chamber 21 and the non-combustion chamber 22 so as to be moved to the common cylinder 42 configured to be re-burned (complete combustion) When the round part of the wall 11 is formed, a plurality of passage grooves 11a are formed at one side of the concave edge drying section 10a and one side of the pyrolysis section 10b which are in contact with each other, and the combustion chamber is disposed above the passage groove 11a. (21) The guide part 30 is configured to allow the combustible gas generated by blocking the cover plate 12a from a predetermined portion to a predetermined section outside the front fire chamber 20 to be moved to the exhaust pipe 31.

The through groove 11a serves as a jet port of water generated when dried in the drying section 10a and a gas generated in the pyrolysis section 10b.

An exhaust pipe 31 is connected between the end of the guide part 30 and the gas combustion device 40 to reburn the gas. The gas combustion device 40 has a cylindrical shape and a fan (not shown) at the edge thereof. An air jet port 41 for injecting the air generated by the, is formed in the lower end of the common cylinder 42, the common cylinder 42 is a plurality of gas injection holes 43 around the vicinity of the jet port 41 ) Is formed toward the air jet port 41.

In addition, an oil pipe 44 is configured to allow combustion oil to be injected at one side of the jet port, and an exhaust pipe 31 connected to the guide part 30 is configured at one side of the lower end of the common cylinder 42.

Meanwhile, liquid tar and oil or one side of the exhaust pipe 31 connecting the guide part 30 and the common barrel 42 are collected when the liquid is tar or oil or the raw material is wood. The tube 32 is formed.

Gas combustion device 40 of the combustible gas is configured as described above is the gas generated in the process of pyrolysis proceeds to the exhaust pipe 31 through the guide portion 30 while the raw material is moved by the screw right (10). At this time, when the liquid tar and oil or the raw materials to be introduced are wood, wood vinegar is first filtered and only the gas enters the common barrel 42 to re-burn by injecting gas into the air injection port 41. By supplementing the role as a combustion raw material, it is also possible to obtain the effect of reducing the oil input during combustion.

In addition, since the burner 24 is provided in the direction of the air ejection opening 41 at the side of the thermal chamber 20, it can be easily ignited at the first ignition.

On the other hand, the cooling water tank 50 is installed between the thermal chamber 20 and the recovery tank 110 serves to cool the high-temperature carbide that the raw material is pyrolyzed in the combustion chamber 21 of the thermal chamber 20. If it is not cooled, the carbide gathered in the recovery container 110 at the bottom of the recovery port 110a continuously emits high heat for a considerable time, so that it is not possible to obtain high quality carbides, and the operator is close to the high temperature when recovering carbides. You will not have the problem.

Between the recovery port 110a and the recovery container 110 is provided with an opening and closing piece 120 to be selectively opened and closed by manual operation before and after, if necessary, which is continuously open during operation It will be closed when the carbide is recovered and then the carbide is recovered. This is because the operator opens the door of the recovery container 110 to allow the outside air to enter the inside of the screw right wall 11 to maintain the vacuum state by blocking it.

In the above configuration, if the user does not have the need for carbides, the cooling process and the carbide recovery process are not necessary, and the generated carbides must be completely burned and treated.

Therefore, the cooling water container 50 and the recovery container 110 formed at the rear of the thermal chamber 20 should be eliminated and have a different configuration. That is, the refractory brick is formed on the inner wall, the burner 151 is provided at one side, the outlet 152 for discharging the burned material on one side and the heat generated in the process of oxidizing the carbide is the thermal chamber 20 The inlet 153 is provided with an oxidation chamber 150 each configured at one side portion so as to be introduced into the combustion chamber 21 of the screw chamber. Carbide outlet 154 of a predetermined size is formed at the bottom of the wall (11).

When the pyrolysis-complete carbide in the combustion chamber 20 is moved to the oxidation chamber 150 and falls to the bottom of the oxidation chamber 150 through the carbide discharge port 154, it is completely burned using the burner 151 and then the ash discharge port ( Through 152).

The configuration of the oxidation chamber 150 as described above may be applied only when necessary as a selective function according to the use purpose of the user.

The automatic carbide manufacturing apparatus of the present invention, which can be configured as described above, easily handles various wastes (organic and inorganic), which are the main culprit of environmental pollution, and at the same time, additionally carbides (charcoal), which are recognized for their many uses in each field. It can be produced as a product so that not only waste disposal but also a certain profit can be provided.

In addition, carbides are formed evenly from the beginning to the end by silent operation, and carbides of high carbon can be obtained because there is no air inflow from charging to discharge. It is easy to burn and has high combustion efficiency, and by using exhaust gas as an auxiliary heat source, it saves a lot of fuel to burner, and it can handle aerobic substances from sludge, sludge, and other household wastes with high water content. Compared with the existing waste treatment, it is a very innovative design that can achieve double and triple effects.

As environmental problems caused by various wastes become more and more social problems, it is expected to contribute significantly to environmental cleanup.

Claims (3)

A power unit 1 composed of a reduction motor 2, a reduction gear 3, and sprockets 2a, 3a, 4, 4a, and 5 on one side; It is divided into a drying section 10a, a pyrolysis section 10b, a cooling section and a moving section 10c. The outer surface is surrounded by a screw right wall 11 in a sealed state, and the sprocket 4, 4a, 5) and the screw (10) is composed of two pairs to be connected to the power transmission; The wall is formed by the refractory brick 25 in the interior of the screw right wall 11 having the built-in screw right 10 is separated by the partition 23 into the combustion chamber 21 and the non-combustion chamber 22. A combustion chamber 20 having a gas combustion device 40 and a burner 24 at one side of the exhaust communication 26 and a bottom of the upper side; Several gas passage grooves 11a are formed at an upper end of the screw right wall body 11 positioned in the combustion chamber 21 and the non-combustion chamber 22 of the thermal chamber 20, and a cover plate is formed on the passage grooves 11a. The guide part 30 is formed by the structure of 12a, and the exhaust pipe 31 is provided between the guide part 30 and the common cylinder 42 comprised in the lower end of the combustion apparatus 40 of the bottom face of the said combustion chamber 21. To configure the connection: It is provided with a cooling water container (50) outside the screw right wall (11) of the rear end of the thermal chamber (20); Raw material loading container 100 and the inlet opening (100a) at the top of the front of the screw wall (11), recovery port (110a) at the bottom of the rear to configure the recovery container 110, respectively, the inlet (100a) and recovery port ( Automated carbide production apparatus characterized in that each provided with an opening and closing piece (120) in (110a). The method of claim 1, A burner 151 is provided at one side of the rear of the thermal chamber 200, and an oxidation chamber 150 is provided at each of the lower ends thereof with an outlet 152 and an inlet 153 connected to the combustion chamber 21. Automatic carbide production apparatus, characterized in that the carbide outlet (154) formed on the lower end of the screw right wall (11) penetrating the oxidation chamber 150. The method of claim 1; The gas combustion device 40 is cylindrical, and an air jet port 41 and a shared cylinder 42 are formed at the bottom thereof, and the shared cylinder 42 has a plurality of gas jet holes 43 at the side ends of the jet port 41. At the same time the automatic pipe manufacturing apparatus, characterized in that each of the exhaust pipe 31 and the exhaust pipe 31 is connected to the guide portion 30 on one side of the oil pipe (44) and the lower side of the common barrel (42).