KR102038966B1 - Manufacturing system for fuel using livestock excrements - Google Patents

Abstract

The present invention is a vehicle having a mobility; A drying apparatus connected to the vehicle and including a stirring unit to crush and stir the injected axial fraction; A hot air supply device connected to the drying device and supplying hot air; And an exhaust device connected to the drying device and discharging the air inside the drying device to the outside, wherein the drying device may be separated from the vehicle or may be integrally formed. to provide.

Description

Manufacturing system for fuel using livestock excrements

The present invention relates to a condensed fuel production system.

Livestock refers to the manure produced by farms. The livestock from farms has long been used as fertilizer for farms.

In recent years, as the size of livestock farms has increased, the amount of livestock has increased, and as it has become difficult to process the farm itself, surplus stocks have increased.

Surplus stock is not only a problem in storage and utilization, but also becomes a habitat for pests such as flies and mosquitoes.

In this respect, various methods such as incineration, mill composting and milling fuel processing have been sought for processing.

Among them, the method for processing condensed fuel is to produce solid fuel by processing the condensed powder, which is known as an environmentally friendly method.

A common method for processing condensed fuel is to first collect the condensate from a farm and then transport it to a place with a treatment facility. Thereafter, the conveyed livestock is processed into dehydrated fuel, which is subjected to processing such as dehydration, stirring and drying in the livestock treatment plant.

However, for the installation of the above-described waste treatment plant, a lot of site and enormous equipment costs are incurred. In addition, even if the installation of the facility, there is a problem that the installation and management costs a lot.

In addition, the livestock processing facilities have a problem that it is difficult to secure a site, such as the installation of these facilities is refused by residents in the residential area due to the harmful substances generated during the processing of the livestock powder.

In addition, in the process of transporting the collected shaft powder to the vehicle, there is a problem that the pollution water generated from the shaft powder causes environmental pollution due to falling water or odor problems in the distance.

In addition, these facilities have a problem that causes odor generated in the process of storing and processing the collected livestock for a long time, causing environmental pollution in the area where the facilities are installed.

Korean Patent Registration No. 10-1285400 (Notification date, 2013.07.11)

The technical problem to be achieved by the present invention is to produce livestock fuel, which can process livestock powders regardless of the place, there is little problem of environmental pollution when processing livestock feedstocks, and help increase farm household income by processing livestock feedstocks. We want to provide a system.

In order to solve this problem, the axial fuel production system according to an embodiment of the present invention includes a vehicle having mobility; A drying apparatus connected to the vehicle and including a stirring unit to crush and stir the injected axial fraction; A hot air supply device connected to the drying device and supplying hot air; And an exhaust device which is connected to the drying device and discharges the air inside the drying device to the outside, wherein the drying device may be separated from the vehicle or may be integrally formed.

In addition, the drying apparatus may be operated by the power of the vehicle or a power unit connected thereto.

In addition, the stirring unit includes a forward and reverse stirrer in which the rotation direction is reversed at regular intervals, the forward and reverse stirrer includes a stirring blade formed at right angles on the axis of the forward and reverse stirrer, the stirring blade is generated during stirring It can be formed of a hollow steel pipe that resists torsional stress to form a turbulent flow in accordance with the rotation of the static stirrer.

In addition, the stirring blade may include a plurality of stirring auxiliary blades formed in a plate shape at one end of the stirring blade in the longitudinal direction of the stationary stirrer.

In addition, the exhaust device may include a dust collector for removing contaminants in the discharged air.

In addition, the dust collector includes a first dust collector, the first dust collector, the first reaction unit for removing the harmful substances contained in the air by reacting the absorbed liquid with the air introduced into the exhaust device; Located at the bottom of the reaction portion, the absorbent liquid storage unit for receiving the absorbent liquid; A partition part including an absorbent liquid pipe and a through hole separating the reaction part and the absorbent liquid storage part and communicating with the reaction part and the absorbent liquid storage part; An injection unit connected to the through hole to inject air introduced into the exhaust device to the first reaction unit; And a first inlet connected to the absorbent liquid storage part and introducing air into the first dust collecting part.

The dust collector may further include a second dust collector, and the second dust collector may include: a second inlet that introduces air into the second dust collector; A second reaction part connected to the second inlet part and provided with a spray part for spraying a reaction solution on the inflowed air; A plurality of blocking wall portions that partition the inside of the second reaction portion at predetermined intervals; And it may be formed to pass through the air introduced into the blocking wall portion, it is disposed alternately with each other.

In addition, it is connected to the drying device, and may further include a axial fuel feed device for transporting the dried constituents in a predetermined direction.

The apparatus may further include a packaging device for packaging the axial powder transferred from the axial fuel feeder in a predetermined weight unit.

In addition to the technical task of the present invention mentioned above, other features and advantages of the present invention will be described below, or from such description and description will be clearly understood by those skilled in the art.

According to the present invention as described above has the following effects.

The present invention is moved by a vehicle having a mobility and because the processing of the shaft portion immediately in the field, there is no need for a separate site and can be transported directly to the buyer who needs processed milled fuel can save the logistics cost.

Since the present invention can process the shaft powder during movement, it is possible to shorten the time required for transportation and processing of the shaft powder.

The present invention includes two different dust collectors in the exhaust device, thereby removing harmful substances and odors in the exhausted air, thereby minimizing air pollution generated during the processing of the shaft powder.

The present invention can help to increase the income of farmers through the sale of the livestock fuel by regenerating the livestock powder to the livestock fuel.

In addition, other features and advantages of the present invention may be newly understood through the embodiments of the present invention.

1 is a right side perspective view schematically showing a condensed fuel production system according to an embodiment of the present invention.
Figure 2 is a left side perspective view schematically showing a condensed fuel production system according to an embodiment of the present invention.
Figure 3 is a perspective view schematically showing a stirring portion of the condensed fuel production system according to an embodiment of the present invention.
4 is a cross-sectional view schematically showing a first dust collecting part of the axial fuel production system according to an embodiment of the present invention.
5 is a schematic cross-sectional view of a second dust collecting part of a condensed fuel production system according to an embodiment of the present invention.

In the present specification, in adding reference numerals to components of each drawing, it should be noted that the same components have the same reference numerals as much as possible even if they are displayed on different drawings.

On the other hand, the meaning of the terms described herein will be understood as follows.

A singular expression should be understood to include a plurality of expressions unless the context clearly indicates otherwise. The terms "first", "second", and the like are intended to distinguish one component from another. However, the scope of the rights shall not be limited by these terms.

It is to be understood that the term "comprises" or "having" does not preclude the existence or addition of one or more other features or numbers, steps, operations, components, parts or combinations thereof.

The term " on " means to include not only when a configuration is formed directly on top of another configuration but also when a third configuration is interposed between these configurations.

Hereinafter, with reference to the accompanying drawings will be described in detail preferred embodiments of the present invention designed to solve the above problems.

In the following description of the present invention, in order to clearly describe the present invention, parts irrelevant to the description are omitted, and detailed descriptions of related well-known technologies or configurations are omitted in order not to obscure the gist of the present invention.

1 is a right side perspective view schematically showing a condensed fuel production system according to an embodiment of the present invention, Figure 2 is a left side perspective view schematically showing a condensed fuel production system according to an embodiment of the present invention.

1 to 2, the axial fuel production system 1 according to an embodiment of the present invention is a vehicle 100, a frame 900, a power unit, a drying device 300, a hot air supply device having a mobility 500, a fire protection device 70, an exhaust device 700, a condensed fuel feed device 10, a packing device, a storage device, a control device 50, and a walking path 90.

The vehicle 100 moves the axle fuel production system 1 and is generally referred to as a tractor or trailer truck.

The frame 900 may mount various facilities of the axial fuel production system 1.

In more detail, the frame 900 may be equipped with a drying apparatus 300, the frame 900 may be separated or connected to the vehicle 100.

For example, the frame 900 is connected to the rear of the vehicle 100, the front portion, if separated, can be balanced so as not to fall by standing up the support. In this case, the frame 900 may be a trailer, a semi-trailer is preferably secured a lot of mounting space. In addition, it may be a low height trailer with a low height so as to facilitate the worker's work on the crushing.

The power unit provides power to each device of the side fuel production system, and may be a power unit provided in the vehicle 100 or a power unit independently mounted in the frame 900.

In this case, since the vehicle 100 may process the collected shafts by itself after collecting the shafts, the transportation cost of moving the vehicle 100 to a separate place where the treatment facility is located for the treatment of the collected shafts is conventionally used. Can be saved.

In addition, since the processing of the collected livestock proceeds while the vehicle 100 moves to the next farmhouse, a separate time for processing the livestock is not required, and more farmhouses can be visited and processed. .

In addition, the power plant may be provided from the outside. In one embodiment, the condensed fuel production system 1 may receive a power unit from a farmhouse where the condensate is collected, and process the condensate.

That is, it is possible to move the condensed fuel production system 1 to the place where the condensate occurs, and to immediately proceed with the work at that position.

For example, in the case of a farmhouse in which a large amount of generated nutrients is required to take several days to process, the nutrient-fuel manufacturing system 1 is moved to the farmhouse and installed separately from the vehicle 100 to provide power from the farmhouse. Receiving can be carried out during the required period.

The drying apparatus 300 may include a stirring unit 310 for crushing and stirring the collected crushed powder.

Axles generated in a farm can be hardened due to agglomeration or a low moisture content in the agglomerated state according to a storage environment and a storage period, and the stirring unit 310 may perform a work of crushing them.

In addition, the shaft powder is processed by the incoming hot air to be made of condensed fuel, at which time the shaft powder may be crushed or stirred with hot air to increase the efficiency of the hot air.

In addition, in making condensed fuel, it may be agitated, such as wood pulverized, coffee foil, slug excretion, etc. that is added to lower the amount of moisture contained in the condensate or to remove the smell of the condensate.

The drying apparatus 300 may include a chamber 350, an inlet 370, and an outlet.

The chamber unit 350 may provide a space in which the processing of the shaft powder injected into the drying apparatus 300 is performed.

The inlet 370 is formed at one side of the chamber unit 350, and the shaft portion is introduced into the chamber unit 350 through the inlet 370. At this time, the inlet 370 may include a guide vane so that the axial portion that is collectively introduced into the fork-lane or the like smoothly flows.

The discharge port discharges the condensed fuel produced by the processing of the shaft powder to the outside of the chamber unit 350. Preferably, the outlet is formed in plural, and may be driven by an actuator in a sliding manner or a sliding manner.

In addition, the lower end of the discharge port may be formed with a axial fuel feed device 10 for transferring the axial fuel discharged to the desired position.

Condensed fuel production system 1 may include a storage device for storing condensed fuel.

More specifically, the storage device may be directly connected to the drying apparatus 300 to store the shaft powder or may be connected to the shaft fuel feed device 10 to store the shaft powder.

In this case, the storage device may be installed in the frame 900 or in a separate trailer.

Drying apparatus 300 may include an exhaust manifold for adjusting the weak vacuum inside the chamber portion (350).

3 is a perspective view schematically showing the stirring unit 310 of the condensed fuel production system 1 according to an embodiment of the present invention. Referring to FIG. 3, the stirring unit 310 includes a forward and reverse stirrer 330.

The stationary stirrer 330 is freely rotatable inside the chamber 350.

The stationary stirrer 330 may be formed in the form of a hollow steel pipe so as to resist the torsional stress generated when the shaft is stirred.

The stationary stirrer 330 reverses the rotation at a predetermined time interval in the rotational direction thereof to prevent the shaft portion introduced into the chamber 350 from being biased or compacted to one side, or prevents the rotational resistance between the shaft portion and other materials to be stirred. It is desirable to make it shrink.

For example, reverse rotation of the forward and reverse stirrer 330 in the forward and reverse directions at intervals of 5 minutes may prevent the shaft portion introduced into the chamber 350 from being compacted to one side.

In addition, the stationary stirrer 330 may be driven by a drive sprocket and a power source connected to the sprocket 335 formed at one end of the chain.

The stationary stirrer 330 may include a stirring blade 331 formed at regular intervals on an outer surface along the longitudinal direction of the stationary stirrer 330.

In this case, the internal shaft powder is distributed evenly by the interaction of the plurality of stirring blades 331, and it is possible to solve the pulling phenomenon and the aggregation phenomenon of the shaft powder.

At this time, each stirring blade 331 is preferably formed at a predetermined interval. In one embodiment, each of the intervals corresponding to the three lengths of the shaft diameter of the forward and reverse stirrer 330 may be arranged at a right angle to each other.

In addition, the stirring blades 331 may further include a plurality of stirring auxiliary blades 333 formed in a plate shape at one end.

In this case, the helical motion smoothly occurs in the shaft portion in which the plate-shaped stirring auxiliary wing 333 is stirred, thereby increasing the efficiency of stirring.

The stirring auxiliary vane 333 may be formed in an appropriate size so as not to get caught in the foreign matter contained in the shaft powder.

In addition, the cross section of the stirring blades 331 may be formed in a streamlined shape, and the stirring blades 331 adjacent to each other may face different directions.

More specifically, if the stirring blade 331 closest to the sprocket 335 based on the stationary stirrer 330 is oriented in the angular direction of 315 degrees based on the sprocket 335, the stirring blade 331 closest to the sprocket 335 is 45 degrees. Can be oriented in the angular direction of the figure.

In this case, while the stationary stirrer 330 is driven, the adjacent stirring blade 331 and the other stirring blade 331 adjacent to the stirring blade can be induced to smoothly flow in the axial component introduced in different directions.

In this way, the shaft powder is guided in various directions to prevent the shaft from being pulled out, and the stirring blade 331 is formed in a streamlined shape to minimize the resistance of the shaft powder during agitation, so that it is efficient with little power. Agitation is possible.

The hot air supply device 500 is connected to one side of the chamber unit 350 of the drying apparatus 300 to supply hot air to the inside of the chamber unit 350.

In more detail, the hot air supply device 500 may include a burner 510, a hot air chamber 530, and a booster blower 550.

The burner 510 burns the outside air flowing into the hot air chamber 530 to create hot air.

The hot air chamber 530 may mix the produced hot air with outside air and maintain the hot air at an optimum temperature.

The booster blower 550 applies an appropriate pressure to the created hot air and flows it into the drying apparatus 300.

In addition, the hot air supply device 500 may further include an exhaust recirculation unit.

The exhaust recirculation unit may allow the hot air introduced into the chamber unit 350 of the drying apparatus 300 to be introduced back into the hot air chamber 530.

More specifically, the exhaust recirculation unit may include a recirculation tube, a flow control valve, and an inlet fan.

The recirculation tube is a hollow tube formed in one side is in communication with the chamber unit 350, the other side is in communication with the hot air chamber (530).

The flow control valve is formed in the recirculation pipe, and the inlet fan is located between the flow control valve and the hot air chamber 530 inside the recirculation pipe.

At this time, it is possible to control the flow rate flowing into the recirculation pipe by adjusting the flow control valve and the inlet fan.

In more detail, the hot air recirculation system made through the exhaust recirculation unit will be described.

First, the burner 510 burns outside air at about 1850 degrees Celsius, and outflows of hot air at 900 degrees Celsius to the hot air chamber 530.

The hot air chamber 530 lowers the temperature by 150 degrees Celsius by mixing hot air introduced through the burner 510 and external air introduced by itself, and then flows out to the chamber 350 through the booster blower 550.

Drying the shaft portion processed in the chamber 350, the hot air is lowered to 50 degrees Celsius is discharged to the outside of the 20% through the exhaust device.

The remaining 80% of the hot air is introduced into the hot air chamber 530 through the recirculation pipe.

Thereafter, the hot air of 900 degrees Celsius and the hot air of 50 degrees Celsius introduced through the recirculation tube are stirred in the hot air chamber 530, and the outside air is agitated, and the chamber unit 350 is readjusted by the hot air of 150 degrees Celsius. Repeat cycles entering the process.

As such, by reusing the hot air through the exhaust recirculation unit, the amount of air exhausted can be absolutely reduced, and the waste heat can be recycled to increase energy efficiency.

In addition, when the waste hot air is stirred in the hot air chamber 530, the harmful substances contained in the waste hot air are burned, thereby significantly reducing the pollution of exhaust air, thereby minimizing air pollution.

Heat source tank 30 is a heat source to be used to create a hot air is accommodated, it may use a petroleum fuel such as diesel, kerosene, LPG.

The heat source tank 30 is preferably located at the end opposite to the position of the hot air supply device 500 in the longitudinal direction in the frame 900, in order to reduce the risk of fire.

The fire protection device 70 is a device that fires when a fire occurs due to high temperature hot wind when the drying device 300 processes the shaft powder.

The exhaust device 700 discharges air generated in the process of drying the shaft powder to the outside.

In more detail, during the drying process, pollutants and odors such as ammonia, hydrogen sulfide, methyl sulfide, methyl disulfide, trimethylamine, acetaldehyde, styrene, etc. are generated. Can cause.

Therefore, it is preferable to include a dust collector 710 for removing contaminants in the air discharged to the exhaust device 700, and the dust collector 710 may use various methods.

4 is a cross-sectional view schematically showing a first dust collecting part of the axial fuel production system according to an embodiment of the present invention.

Referring to FIG. 4, the dust collector 710 may include a first dust collector 730.

The first dust collecting unit 730 is configured to increase the number of contact and the likelihood of contact between the incoming air and the absorbent liquid to increase the absorption rate of harmful substances in the air.

The first dust collecting part 730 includes a first inlet part 731, a first reaction part 733, a plate part 735 including the absorbent liquid pipe 737 and a through hole 739, an injection part 741, and an absorbent liquid. The storage part 743, the first pumping member 745, the nozzle 747, the porous reaction plate 749, and the first discharge part 751 may be included.

In more detail, the first reaction unit 733, the first reaction unit 733, and the first inlet unit 731 which react the air introduced into the exhaust apparatus 700 and the absorbent liquid to remove harmful substances contained in the air It may be connected to the liver, and may include an injection unit 741 for injecting air introduced into the first reaction unit (733).

Absorbent liquid can remove harmful substances, and there is no limit to the type of liquid that can be sprayed.

Preferably, the absorbent liquid may be water or dissolved ozone. In this case, after the removal of harmful substances, it is possible to recycle from farms to farm water, thereby minimizing water pollution.

A predetermined space is formed inside the first reaction unit 733, and the nozzle 747 may be disposed at a predetermined height in the corresponding space.

The porous reaction plate 749 may be disposed under the nozzle 747 in the first reaction part 733, and in the nozzle 747 and air moving upward from the lower part of the first reaction part 733. It may include a plurality of through-holes to increase the contact rate between the absorbing liquid is injected from the top to the bottom to improve the absorption of harmful substances.

A first discharge part 751 may be formed at an upper end of the first reaction part 733 to react with the absorbent liquid and discharge air from which harmful substances have been removed.

An absorbent liquid storage part 743 is positioned below the first reaction part 733, and the first reaction part 733 and the absorbent liquid storage part 743 are separated by the diaphragm part 735 and at the same time, the absorbent liquid pipe 737. ) And the through hole 739 may be in communication with each other.

That is, the absorbent liquid storage part 743 is positioned below the first reaction part 733, and the absorbent liquid storage part 743 stays with the absorbent liquid for removing the harmful substances contained in the air, and the absorbent liquid storage part 743. The nozzles 747 are connected to each other by the first pumping member 745.

In this case, when the operator drives the first pumping member 745, the absorbent liquid from the absorbent liquid storage part 743 may be supplied to the nozzle 747 and sprayed inside the first reaction part 733.

In addition, the absorbent liquid injected in the first reaction unit 733 may react with air and accumulate in the lower portion of the first reaction unit 733. At this time, since a plurality of absorbent liquid pipes 737 are formed in the diaphragm 735 separating the first reaction part 733 and the absorbent liquid storage part 743, the absorbent liquid existing under the first reaction part 733. The silver may move the absorbent liquid storage part 743 again along the absorbent liquid pipe 737.

The first inlet 731 may be connected to the absorbent liquid storage 743. In this case, air containing harmful substances introduced from the first inlet 731 flows through the upper portion of the absorbent liquid storage 743.

The first reaction part 733 and the absorbent liquid storage part 743 are separated by the diaphragm part 735, the air is discharged from the first reaction part 733, and air is supplied to the upper part of the absorbent liquid storage part 743. As it is introduced, a constant pressure difference may occur between the first reaction unit 733 and the absorbent liquid storage unit 743.

The injection unit 741 is formed on the through hole 739 of the diaphragm 735, and the air introduced into the upper portion of the absorbent liquid storage unit 743 passes through the injection unit 741 and the first reaction unit 733. To be sprayed on.

At this time, the injection unit 741 may be arranged in plural number on the diaphragm 735 at predetermined intervals to prevent the uneven flow of air in the first reaction unit 733. That is, since the air is uniformly sprayed from the lower portion of the first reaction portion 733, the flow of air is uniform in the first reaction portion 733. This may improve the contact possibility of the absorbing liquid injected in the first reaction unit 733 to increase the absorption rate of the harmful substances.

In addition, the injection unit 741 may be disposed in the diaphragm 735 to be deposited in the absorbent liquid accumulated in the lower portion of the first reaction unit 733. This is for the air injected from the injection unit 741 to preferentially react with the absorbent liquid accumulated in the lower portion of the first reaction unit 733.

In this case, the air containing the harmful substance reacts first with the absorbent liquid accumulated in the lower part of the first reaction part 733, and secondly with the absorbent liquid injected from the upper part of the first reaction part 733. By increasing the frequency of contact with the absorbent liquid, it is possible to improve the removal rate of harmful substances.

5 is a schematic cross-sectional view of a second dust collecting part of a condensed fuel production system according to an embodiment of the present invention.

Referring to FIG. 5, the dust collector 710 may include a second dust collector 770.

The second dust collecting part 770 is the second inlet part 771, the second reaction part 773, the blocking wall part 775, the vent part 777, the spray part 779, the porous plate 781, and the second pumping part. The member 783, the second outlet, and the reaction liquid storage part 787 may be included.

The second reaction unit 773 may include a space for removing harmful substances contained in the air by reacting the air including the hazardous substances with the reaction liquid, and may be formed to have a length in a horizontal direction.

Hazardous substances can be removed by the reaction solution, and any kind of liquid that can be sprayed is not limited.

Preferably, the reaction solution may be water or ozone dissolved water. In this case, it is possible to effectively remove the harmful substances, can be used as farm water in the farm after use may not contaminate the water environment.

The second reaction part 773 is connected to a second inlet part 771 in which air containing harmful substances is introduced into one side, and is connected to a second discharge part 785 in which air from which harmful substances are removed is discharged to the other side. .

The interior of the second reaction unit 773 may be partitioned in multiple stages by the plurality of blocking wall portions 775.

In this case, the blocking wall part 775 may divide the inner space of the second reaction part 773 toward the second discharge part 785 from the second inlet part 771 along the direction in which air flows. have.

Each blocking wall portion 775 may include a respective air passage portion 777 through which air passes. Preferably, the openings 777 of each blocking wall portion 775 are alternately formed in the vertical position between the adjacent openings 777, so that the air can flow up and down.

The sprayer 779 may spray the reaction liquid to the air passing through each compartment of the second reaction unit 773 partitioned by the blocking wall 775.

Spray unit 779 may be formed in a plurality. Preferably, each compartment of the second reaction unit 773 is installed to inject the reaction liquid. In this case, the harmful substances are removed by direct contact with the harmful substances in the air, and they become droplets and may contact the blocking wall portion 775 and flow down.

In addition, the sprayer 779 may include an ultrasonic diaphragm to finely spray the reaction solution. In this case, the fine spray liquid can remove the minute harmful substances.

The lower plate of the second reaction unit 773 may be formed with a porous plate 781 for discharging the liquid. In this case, each blocking wall part 775 may be formed between the porous plate 781 and the upper portion of the second reaction part 773.

The porous plate 781 may be sprayed from the spray unit 779 to collect the harmful substances therethrough, and may be passed down to collect in the reaction liquid storage unit 787.

The reaction liquid collected in the reaction liquid storage part 787 may be sent to the injection part 741 by the second pumping member 783. In other words, even a small amount of the reaction liquid can efficiently remove harmful substances in the air.

As such, the air containing the harmful substances may react with the reaction solution step by step, and increase the number of contact with the reaction solution to improve the removal rate of the hazardous substances. In addition, the harmful substances contained in the air can be effectively removed by the sterilization action of ozone dissolved water.

1 and 2, the dust collector 710 may include both the first dust collector 730 and the second dust collector 770.

In this case, the removal rate of harmful substances in the discharged air is increased, thereby minimizing the air pollution problem generated when processing the shaft.

Condensed fuel transfer device 10 may transport the condensed fuel made in the drying apparatus 300, it is preferable to include a belt conveyor at the lower end of the outlet formed on the lower side of the drying apparatus (300).

Condensed fuel transported through the condensed fuel feeder 10 may be stored in a storage device or transported in a packaging device and packaged.

When the condensed fuel passes through the packaging device, the packaging is completed, and the condensed fuel can be immediately provided where it is needed. In this case, it is possible to directly supply to farms or factories using condensed fuel, thereby reducing costs such as logistics costs and storage costs.

The control device 50 may control the axial fuel production system 1 as a whole and may be managed by an operator by installing a separate controller unit.

The pedestrian path 90 may provide space in managing the operator's work of the axial fuel production system 1, thereby increasing the safety of the worker.

Next, a process of manufacturing the condensed fuel using the condensed fuel production system 1 according to an embodiment of the present invention will be described.

First, the condensed fuel production system 1 moves to a farmhouse which requires the treatment of the condensed powder.

Next, the axial component flows into the chamber 350 through the inlet 370 of the drying apparatus 300.

Next, the condensed fuel production system 1 moves to a farmhouse that requires the processing of the next condensate, or starts moving to a factory to supply condensed fuel.

At this time, the axial fuel production system 1 stops or moves, and manufactures axial fuel.

In more detail, the hot air flowing through the booster blower 550 of the hot air supply device 500 and the forward and reverse stirrer 330 of the stirring unit 310 driven by the power of the vehicle 100 or the power unit connected thereto are The input shaft powder is crushed, stirred with hot air or other input materials, and dried to produce shaft fuel.

Thereafter, the manufactured condensed fuel is discharged to the condensed fuel feeder 10 through the discharge port of the chamber 350 and transported to a storage device or a packaging device by a belt conveyor.

At this time, the contaminated air passes through the stirring unit 310 in the chamber 350 and flows into the exhaust apparatus 700.

The introduced air passes through the first dust collecting part 730 and after the harmful substances contained in the air are removed, passes through the second dust collecting part 770 and once the harmful substances are removed once more, is discharged to the outside through the exhaust port 790. do.

As described above, according to the present invention, in the manufacture of the livestock powder, it is not necessary to have a large site for the facility to carry out the livestock powder treatment, and it is possible to reduce the equipment and the management cost.

In addition, it is possible to reduce the complaints that occurred in the place where a conventional facility is installed, by providing a collection vehicle with a device that can directly process the collected shaft powder.

In addition, the exhaust device includes two different dust collectors, thereby minimizing the problem of air pollution even when the vehicle moves, and can process the axial fuel.

The present invention described above is not limited to the above-described embodiments and the accompanying drawings, and it is possible to substitute, modify, and change variously within the scope without departing from the technical spirit of the present invention. It will be clear to those of ordinary knowledge.

1: Axle Fuel Manufacturing System 100: Vehicle
300: drying apparatus 310: agitator
330: forward and reverse stirrer 331: stirring blade
333: auxiliary stirring wing 335: sprocket
350: chamber 370: inlet
500: hot air supply device 510: burner
530: hot air chamber 550: booster blower
700: exhaust device 710: dust collector
730: first dust collecting unit 731: first inflow unit
733: first reaction unit 735: diaphragm
737: absorbent liquid piping 739: through hole
741: injection unit 743: absorbent liquid storage unit
745: first pumping member 747: nozzle
749: porous reaction plate 751: first outlet
770: second dust collecting portion 771: second inflow portion
773: second reaction unit 775: blocking wall portion
777: vent part 779: spray part
781: porous plate 783: second pumping member
785: second outlet 787: reaction liquid storage unit
790: exhaust port 10: shaft fuel feed device
30: heat source tank 50: control device
70: fire protection device 90: walkway
900: frame

Claims (9)

A vehicle having mobility;
A drying apparatus connected to the vehicle and including a stirring unit to crush and stir the injected axial fraction;
A hot air supply device connected to the drying device and supplying hot air; And
Is connected to the drying device, including an exhaust device for discharging the air inside the drying device to the outside,
The drying apparatus may be separated from the vehicle or may be integrally formed.
The stirring unit includes a forward and reverse stirrer in which the rotation direction is reversed at regular intervals,
The stationary stirrer includes a stirring blade formed at right angles on the axis of the stationary stirrer,
The stirring blade is formed in a streamlined cross section, formed of a hollow steel pipe that resists the torsional stress generated during stirring, forms turbulence according to the rotation of the stationary stirrer, and stirs the stirring in the longitudinal direction of the stationary stirrer. It includes a plurality of stirring auxiliary blades formed in a plate shape at one end of the blade,
The exhaust device includes a dust collector for removing contaminants in the discharged air,
The dust collector includes a first dust collector and a second dust collector,
The first dust collecting unit may include: a first reaction unit for removing harmful substances contained in the air by reacting the absorbed liquid with the air introduced into the exhaust device; Located at the bottom of the reaction portion, the absorbent liquid storage unit for receiving the absorbent liquid; A partition portion including an absorbent liquid pipe and a through hole separating the reaction part and the absorbent liquid storage part and communicating with the reaction part and the absorbent liquid storage part; Disposed in the diaphragm so as to be immersed in the absorbent liquid accumulated in the lower part of the first reaction part, and connected to the through hole to inject the air introduced into the exhaust apparatus from the absorbent liquid accumulated in the lower part of the first reaction part; Injection unit; And a first inlet connected to the absorbent liquid storage part and introducing the air into the first dust collecting part.
The second dust collecting unit may include a second inlet unit for introducing the air into the second dust collecting unit; A second reaction part connected to the second inlet part and provided with a spray part for spraying a reaction liquid on the introduced air; A plurality of blocking wall portions that divide the inside of the second reaction portion at predetermined intervals; And a vent formed to pass through the air introduced into the blocking wall, and arranged alternately with each other. The method of claim 1,
The drying device,
A condensed fuel production system operated by the power of the vehicle or a connected power unit. delete delete delete delete delete The method of claim 2,
Condensed fuel production system is connected to the drying device, further comprising a condensed fuel feed device for conveying the dried constituents in a predetermined direction. The method of claim 8,
Condensed fuel production system further comprises a packaging device for wrapping the axial powder transferred from the axial fuel feeder in a predetermined weight unit.

Images