KR101762898B1 - The manufacturing apparatus of half carbide using biomass mixture - Google Patents

Abstract

The present invention relates to an apparatus for producing a semi-carbide using mixed biomass.
The present invention comprises a first feedstock in which the plant biomass is stored, a second feedstock in which the animal biomass is stored, and a third feedstock in which the organic biomass is stored, wherein each of the biomass is individually dried and crushed A raw material processing section; A raw material mixing unit connected to the raw material processing unit to mix dried and crushed biomass with an additional binder to produce a mixed fuel constituting a semi-carbide; a mixture storage unit for storing the mixed fuel mixed through the raw material mixing unit; A mixture treatment section including a mixture supply section for supplying the mixed fuel to the semi-carbonization treatment section; A semi-carbonization treatment unit for mixing the mixed fuel and the barrel and carbonizing the mixture by removing oxygen to produce a semi-carbide; A semi-carbide treatment unit for supplying the semi-carbide manufactured by the semi-carbide treatment unit and selectively molding the semi-carbide according to a user's request; And a control unit for controlling the driving of the raw material treatment unit, the mixture treatment unit, the semi-carbonization treatment unit and the half-carbide treatment unit.

Description

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a half-carbide production apparatus using mixed biomass,

The present invention relates to an apparatus for producing a semi-carbide using mixed biomass. More particularly, the present invention relates to a biomass containing biomass including waste wood, sludge, wood, bovine, rice hull, rice straw, and the like, Carbide production apparatus using a mixed biomass capable of selectively producing and controlling the quality of a calorific value according to a purpose of use.

Recently, biomass, which has been attracting attention as an alternative energy for fossil energy such as petroleum, has a disadvantage because it has a very high internal porosity in a raw state and is bulky and has a low energy density per unit weight.

In order to solve these drawbacks, recently, the biomass material is semi-carbonized to increase the energy density per unit weight (Kcal / kg), while the semi-carbonized biomass material is produced in the form of pellets, Technologies and devices are being developed continuously.

Here, the semi-carbonization treatment is to heat-treat the biomass material in a high-temperature anaerobic state to lower the weight. At this time, the calorific value of the biomass is also slightly reduced. However, as a result, the calorific value per unit weight, that is, the energy density (Kcal / kg) can be improved.

For example, Korean Patent Registration No. 10-1344860 discloses a biomass carbonization apparatus comprising: a supply unit for supplying a biomass material; A porous screen provided at a lower portion of the semi-carbonization space, and a biocomposite space provided at a lower portion of the biocarbonization space, A semi-carbonizing treatment unit having an agitator for causing the agitator to agitate; A heater provided in a lower region of the porous screen, and a heat exchanger having a heat exchanger provided adjacent to a lower portion of the heater; And an air blowing unit for blowing air into the semi-carbonizing space via the heating unit.

However, according to the above-mentioned prior art documents, when the raw material of such biomass is solidified (molded) into a solid fuel, the process has a merit merely. However, since the absorption rate is low, There is a difficulty in. In addition, it is possible to increase the specific gravity through molding rather than the biomass itself, but it still has a problem that the distribution cost is increased in transportation and storage due to its low weight

In addition, in the conventional method for producing biomass fuel, moisture is evaporated in the (semi) carbonization process of biomass to produce pores, and the strength and the apparent density of the biomass fuel are weakened by the generated pores. Accordingly, there is a problem that dust due to breakage during storage and transportation of the biomass fuel is generated and the commerciality of the biomass pulverized fuel is deteriorated.

Korean Patent No. 10-1344860

In order to solve such problems, the present invention has been made in view of the above-mentioned background art, and it is an object of the present invention to provide a biomass containing biomass including waste wood, sludge, wood, bovine rice, rice hull, rice straw, And an organic biomass to provide a semi-carbide producing apparatus using a mixed biomass that maintains a calorific value of 3,000 to 6,000 kcal / kg.

The present invention also provides an apparatus for producing a semi-carbide using a mixed biomass that can selectively produce quality of a heating value required by users by using a mixed raw material in which a plant, an animal, and organic biomass are mixed It has its purpose.

Another object of the present invention is to provide an apparatus for producing a semi-carbide using a mixed biomass capable of freely shaping and providing various shapes, sizes and shapes of a semi-carbide having a constant calorific value according to a demand of a customer .

According to an aspect of the present invention, there is provided a method of producing a biomass comprising: a first feeding part for storing vegetable biomass; a second feeding part for storing animal biomass; and a third feeding part for storing organic biomass A raw material treatment unit for individually drying and crushing the biomass; A raw material mixing unit connected to the raw material processing unit to mix dried and crushed biomass with an additional binder to produce a mixed fuel constituting a semi-carbide; a mixture storage unit for storing the mixed fuel mixed through the raw material mixing unit; A mixture treatment section including a mixture supply section for supplying the mixed fuel to the semi-carbonization treatment section; A semi-carbonization treatment unit for mixing the mixed fuel and the binder, carbonizing the mixture by removing oxygen to produce a semi-carbide; A semi-carbide treatment unit for supplying the semi-carbide manufactured by the semi-carbide treatment unit and selectively molding the semi-carbide according to a user's request; And a control unit for controlling the driving of the raw material treatment unit, the mixture treatment unit, the semi-carbonization treatment unit and the half-carbide treatment unit.

According to an embodiment of the present invention, the first to third supply units include first to third raw material storing units in which respective biomass are individually stored, and biomass from the first to third storing units, Further comprising first to third raw material supply units for supplying the biomass transferred and transferred to the raw material mixer under the control of the control unit, wherein the first to third raw material storage units and the first to third raw materials And the first to third drying units for drying the respective biomass stored and configured between the supply units are selectively constructed.

According to an embodiment of the present invention, the first to third raw material storage units may include a charging unit into which vegetable, animal, or organic biomass is charged, and biomass stored individually through the charging unit, A storage chamber in which the same group of biomass is separately stored by dividing a space, a moisture removing device for removing moisture contained in the biomass, and a controller for controlling the vegetable, animal, or mixed biomass And a supply member for supplying the raw material to the mixing portion of the mixing portion.

In addition, according to an embodiment of the present invention, the charging unit may include a rotating plate configured to rotate on the charging unit, which is formed on the storage chamber, a driving motor for rotating the rotating plate, And a sealing plate that is hermetically sealed by the sealing plate.

In addition, according to an embodiment of the present invention, the first to third drying units include inner tubes for transporting and drying the biomass; An outer tube which is formed on an outer periphery of the inner tube and circulates a predetermined hot air to dry the biomass; A transfer screw configured to transfer the biomass to the inner periphery of the inner cylinder; And a hot air supply unit provided on one side of the outer cylinder and providing a predetermined amount of hot air under the control of the control unit.

According to an embodiment of the present invention, the first to third raw material supplying units may include a crusher connected to the first to third drying units and crushing the dried biomass to a predetermined size under the control of the controller, And a quantitative feeder for quantitatively feeding the pulverized products of the pulverized biomass to the raw material mixing portion.

According to an embodiment of the present invention, the raw material mixing unit may further include an agitator constituted by an impeller for mixing the vegetable, animal and organic biomass, and a crushing blade configured to crush the biomass in the impeller .

According to an embodiment of the present invention, the mixture storage unit is configured with a temperature and humidity sensor interlocked with the control unit so that the internal temperature and humidity can be maintained constant at all times.

According to an embodiment of the present invention, the mixing portion further includes a mixture drying portion connected to the raw material mixing portion to dry the biomass.

According to an embodiment of the present invention, the semi-carbonization treatment unit includes a semi-carbonization unit for semi-carbonizing the mixture; A heat source supply unit for supplying a heat source to the semi-carbonized part side; And a refining unit for refining the refuse by sucking noxious gas generated during carbonization of the mixture.

According to an embodiment of the present invention, the half-carbide treatment unit includes a semi-carbonization discharge unit for receiving the semi-carbonized semi-carbonized material through the semi-carbonated treatment unit and cooling the semi-carbonized material, and discharging the cooled semi-carbonized material; A semi-carbide storage part for storing the semi-carbide discharged from the semi-carbonated discharge part; A semi-carbide forming unit for receiving a predetermined amount of semi-carbide from the semi-carbide storage unit and processing the same to produce a semi-carbide having a calorific value of 3,000 to 6,000 Kcal / kg; And a semi-carbonization non-molding section for supplying a predetermined amount of semi-carbide from the semi-carbide storage section and producing a semi-carbide having a predetermined amount of heat while maintaining the shape of the semi-carbide.

According to an embodiment of the present invention, the control unit may include: a data management unit for storing data on moisture and calorific value of the biomass; A raw material detecting unit which receives data on the moisture and calorific value of the biomass stored in the first to third raw material storing units and compares and analyzes the data with the data recorded in the data managing unit to control the driving of the raw material treating unit and the mixture treating unit; A reaction regulator for controlling the reaction temperature and the reaction time of the semi-carbonization treatment unit so as to control the oxygen present in the semi-carbonization treatment unit to be removed and perform semi-carbonization of the mixed raw material; And a supply amount adjusting unit for controlling the supply amount of each type of the biomass by controlling each of the first to third raw material supplying units individually.

According to the embodiment of the present invention, a semi-carbide composed of plant, animal, and organic biomass mixed with biomass including waste wood, sludge, wood, bovine, rice hull, rice straw and the like is minimized and moisture content is minimized , It is possible to provide an energy saving effect by providing a high-quality semi-carbide which can be used by mixing a certain amount of biomass semi-carbide fuel together with coal fuel in a power plant by maintaining a high calorific value at a calorific value of 3,000-6,000 kcal / kg.

In addition, according to the embodiment of the present invention, it is possible to selectively control the quality of the calorific value required by the users by using the mixed raw material in which the plant system, the animal system, and the organic biomass are mixed, .

According to the embodiment of the present invention, the shape of the semi-carbide maintaining a constant calorific value can be freely formed and provided in various shapes, sizes and shapes according to the demand of the customer.

FIG. 1 is a schematic view of a half-carbide production apparatus according to an embodiment of the present invention. FIG.
FIG. 2 is a schematic view illustrating a raw material treatment unit of a half-carbide production apparatus according to an embodiment of the present invention;
FIG. 3 is a schematic view showing a mixture treatment unit of a half-carbide production apparatus according to an embodiment of the present invention;
FIG. 4 is a schematic view illustrating a semi-carbonization treatment unit of a half-carbide production apparatus according to an embodiment of the present invention;
FIG. 5 is a schematic view of a half-carbide treatment unit of a half-carbide manufacturing apparatus according to an embodiment of the present invention;
FIGS. 6 to 9 are schematic views of the respective parts of the apparatus for producing a semi-carbide according to an embodiment of the present invention.

Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings. In the drawings, the same reference numerals are used to designate the same or similar components throughout the drawings. In the following description of the present invention, a detailed description of known functions and configurations incorporated herein will be omitted when it may make the subject matter of the present invention rather unclear.

In describing the components of the present invention, terms such as first, second, A, B, (a), and (b) may be used. These terms are intended to distinguish the constituent elements from other constituent elements, and the terms do not limit the nature, order or order of the constituent elements. When a component is described as being "connected", "coupled", or "connected" to another component, the component may be directly connected to or connected to the other component, It should be understood that an element may be "connected," "coupled," or "connected."

FIG. 1 is a schematic view of a half-carbide production apparatus according to an embodiment of the present invention. FIG. 2 is a schematic view of a raw material treatment section of a half- FIG. 4 is a schematic view of a semi-carbonization treatment section of a half-carbide production apparatus according to an embodiment of the present invention. FIG. 5 FIG. 6 is a schematic view illustrating a half-carbide treatment unit of a half-carbide manufacturing apparatus according to an embodiment of the present invention, and FIGS. 6 to 9 are views schematically showing various parts of a half- .

As shown, the apparatus for producing a semi-carbide using the mixed biomass of the present invention includes plant biomass such as waste wood, wood, rice husk, rice straw, organic biomass such as animal biomass and sewage sludge, A mixture treatment unit 200 for mixing the types of biomass transferred from the raw material treatment unit 100, and a mixture of biomass for each type conveyed from the mixture treatment unit 200, Carbonized processing unit 300 for producing a semi-carbonized product by semi-carbonizing and molding the semi-carbonated product 300 to form a semi-carbonized product, The mixture treatment section 200, the half-burning treatment section 300, and the half-carbide treatment section 400 are driven so as to drive the half-carbide treatment section 400 and the raw material treatment section 100, And a control unit 600 for controlling the control unit 600.

The raw material processing unit 100 is divided into first to third supply units 110, 120 and 130 so as to be individually stored according to the type of the biomass.

The first supply part 110 includes a first raw material storage part 112 for storing vegetable biomass and a first raw material drying part for drying the plant biomass stored in the first raw material storage part 112 And a first raw material supply unit 116 for crushing and pulverizing the dried plant biomass and supplying the pulverized pulverized material to the mixture processing unit 200 side.

The second feeder 120 includes a second feedstock storage unit 122 for storing the animal biomass and a second feedstock drying unit 122 for drying the animal biomass stored in the second feedstock storage unit 112 And a second raw material supply unit 126 for crushing and pulverizing the dried animal biomass and supplying the pulverized pulverized material to the mixture processing unit 200 side.

The third supply part 120 includes a third raw material storage part 132 storing the organic biomass and a third raw material drying part 134 drying the organic biomass stored in the third raw material storage part 132. [ And a third raw material supply unit 136 for supplying the dried organic biomass to the mixture processing unit 200 side.

As shown in FIG. 6, the first to third raw material storage parts 112, 122, and 132 are formed with an injection part 512 in which vegetable, animal, and organic biomass are respectively introduced into the upper surface, A storage chamber 514 in which the biomass introduced through the input unit 512 is separated and stored for each type, a water storage tank 514 for removing water contained in the stored biomass under the control of the controller 600, A device 516 is further configured, and in particular a partition plate 518 may be configured to divide the storage chamber 514 such that the stored biomass can be separated and stored independently.

At this time, the charging unit 512 is configured to be rotatable at the upper portion of the storage chamber 514 so that different types of biomass can be introduced into the storage chamber 514 divided by the partition plate 518 .

That is, the charging unit 512 is coupled to the rotating plate 512a through which the rotating motor 512c is rotated by the driving motor 512c. The charging unit 512 is connected to the charging hole formed in the upper portion of the storage chamber 514 under the control of the controller 600, The biomass is introduced, and the injection hole of the other storage chamber 514 divided by the partition plate 518 is configured to be sealed by the sealing plate 512b.

The first to third raw material storage units 112, 122 and 132 are provided with a supply member 515 for supplying the biomass stored in the storage chamber 514 to the first to third raw material drying units 114, The supply member 515 is configured to be supplied through a screw conveying system or a conveyor system.

The first to third raw material drying units 114, 124, and 134 may be selectively configured in the raw material processing unit 100.

As shown in FIG. 6, the first to third drying units 114, 124, and 134 of the present invention include an outer cylinder 522 and an outer cylinder 522, And the inner tube 524.

The inner barrel 524 is supplied with biomass that is respectively transported from the first to third raw material storage parts 112, 122 and 132, and the supplied biomass is supplied to the transporting screw 526 formed in the inner periphery of the inner barrel 524 .

The outer tube 522 includes a hot air supply device 528 for heating the inner tube 524 to supply the hot air to the inner circumferential surface of the inner tube 524 in order to dry the biomass.

At this time, the hot air flowing through the hot air supply device 528 heats the outer circumferential surface of the inner cylinder 524 while circulating the inner circumferential surface of the outer cylinder 522, and the circulated hot air flows into the hot air supply device 528 again, .

The first to third drying units 114, 124, and 134 discharge dust and moisture generated during the drying of the biomass, and dust is separately separated and discarded by means such as a cyclone. In the case of moisture, To condense it and dispose of it.

The moisture removal device 140 removes water contained in the biomass stored in the storage chambers 514 under the control of the control unit 600 and controls the temperature of the storage chamber 514 The control unit 600 transmits a signal indicating whether the moisture removal unit 140 is driven according to the temperature and humidity of the current storage chamber 514 to determine the temperature and humidity of the storage chamber 514, Is always kept constant.

8, the first and second raw material supplying units 116 and 126 are connected to the screw 526 of the inner tube 524 to receive the dried biomass, The pulverized product of the pulverized biomass is introduced into the lower part of the pulverizer 532 into the raw material mixing part 210 of the mixture processing part 200 ) Side by a predetermined amount.

Between the inner cylinder 524 and the crusher 532 is formed a conveying means 536 for conveying the dried biomass to the crusher 532 side and the conveying means 536 can be constituted by a conventional conveyor system .

In addition, the third raw material supply unit 136 supplies organic biomass, and it is not necessary to perform a separate crushing process due to the characteristics of the organic biomass, but it is also possible to selectively supply the raw materials to the first and second raw material supply units 116 and 126 A separate grinder 532 and a quantitative feeder 534 may be constructed.

The mixture treatment unit 200 mixes the raw materials supplied from the first to third raw material supplying units 116, 126 and 136, respectively, and mixes various types of biomass with the binder to produce a mixture of the forming fuel A raw material mixing portion 210 is constituted.

At this time, the raw material mixing unit 210 may be configured to mix the different kinds of biomass while mixing them. The impeller of the mixer is divided into the biomass which is pulverized through the crusher 532, The pulverizing blade is further constructed so that pulverization is carried out by the pulverizer, so that the impeller of the pulverizer is configured to perform mixing and pulverizing while the pulverizing operation is performed.

Here, the raw material mixing unit 210 is stored in the first to third raw material storage units 112, 114, and 116, and the biomass having different heating values is mixed and mixed with the fossil raw material used in the power plant, To produce a mixed raw material comprising semi-carbide having a calorific value of 3,000 to 6,000 kcal / kg, and more preferably to produce a mixed raw material having a semi-carbide of 3,000 to 4,500 kcal / kg.

That is, in the raw material mixing unit 210 of the present invention, vegetable biomass such as waste wood and wood usually has a high calorific value, so that the calorific value is lower than the existing calorific value by mixing a certain amount of animal or organic biomass It can be used in accordance with the fuel standards used in power plants or incineration facilities by mixing them with fossil raw materials within a range where the input amount does not exceed 10 wt% Thereby producing a mixed raw material constituting a semi-carbide.

In addition, the mixture processing unit 200 includes a mixture storage unit 220 through which a mixture mixture is stored through the raw material mixing unit 210.

The mixture storage unit 220 may include a temperature and humidity sensor interlocked with the control unit 600 so that the temperature and humidity inside the mixture storage unit can be constantly maintained. A supply member 515 is configured to transfer the stored mixture to the mixture drying unit 230 side.

The mixture drying unit 230 is divided into an outer cylinder 522 and an inner cylinder 524 in the same manner as the material drying units 114, 124 and 126 and constitutes a transfer screw 526 in the inner cylinder 524, The drying and conveying of the paper is carried out.

The mixture supplying part 240 is a constituent element for conveying the mixture in a dried state in the mixture drying part 230 to the semi-carbonizing part 310 of the semi-carbonizing part 300, and is preferably constituted by a conveyor system, It is not.

The semi-carbonization treatment section 300 includes a semi-carbonization section 310 for carbonizing the mixture to make it a semi-carbide, a heat source supply section 320 for providing a high-temperature gas to the carbonization furnace side, and a noxious gas generated during carbonization of the mixture And a refining unit 330 for refining.

The semi-carbonizing unit 310 includes a carbonization furnace having the same structure as that of the first to third drying units 114, 124, and 134 so that the mixture supplied from the mixture supply unit 240 is received and carbonized, And a heat source supply unit 320 for supplying a high-temperature gas to the furnace side.

The semi-carbonizing unit 310 may further include a binder supplying unit for supplying a binder of 3 to 5% by weight based on the weight of the carbide to the semi-carbonizing process, have.

Here, it is preferable that the heat source supply unit 320 is integrally formed on one side of the carbon furnace so that the heat source is supplied to the inside of the outer cylinder 522 of the carbon furnace in which the rotation operation is performed, but the present invention is not limited thereto.

The semi-carbonizing unit 310 may further include a refiner 330 for refining the harmful gas generated during carbonization of the mixture.

In this case, the refiner 330 separates the harmful gas into a harmful component and a pure high-temperature gas. The harmful components are stored in a separate storage tank for disposal. The pure high-temperature gas is supplied to the heat source supply part 320, Can be achieved.

The semi-carbonization treatment unit 300 of the present invention may further comprise a storage unit in which the semi-carbonized raw materials are stored and stored. However, the present invention is not limited thereto.

The semi-carbide treatment unit 400 is a component that is supplied with raw materials that have been semi-carbonized through the semi-carbonizing unit 300, stores the supplied raw materials, and forms the semi-carbonized raw material.

The semi-carbide treatment unit 400 includes a semi-carbide discharge unit 410 connected to the semi-carburetor 310 to discharge the semi-carbide formed by the semi-carbide discharge unit 410, A half-carbide storage part 420 is constituted.

The semi-carbonized discharge unit 410 is a component that receives the semi-carbonized semi-carbonized material through the semi-carbonated part 310 to cool it, and discharges the semi-carbonated material to the semi-carbonized material storage unit 420 when the cooling is completed.

The semi-carbonized discharging unit 320 includes an outer cylinder 522 and an inner cylinder 524 like the first to third drying units 114, 124 and 134. The semi-carbide is received and transported to the inner cylinder 524 , So that the refrigerant circulates to the inner periphery of the outer cylinder 522 to cool the half-carbide of the inner cylinder 524.

At this time, the cooler for supplying the coolant may be separately formed on one side of the outer cylinder 522, but the present invention is not limited thereto.

The semi-carbide storage part 420 stores a semi-carbide and a quantitative feeder is formed on one surface of the semi-carbide storage part 420. The semi-carbide storage part 420 has a semi-carbide forming part 440, .

Here, the half-carbide unformed portion 430 is a component that receives the half-carbide stored in the half-carbide storage portion 420 and carries out the carbonization while maintaining the shape of the half-carbide.

The semi-carbide forming unit 440 receives a predetermined amount of semi-carbide from the semi-carbide storage unit 420 and processes the semi-carbide to produce a carbon-forming fuel having a calorific value of 3,000 to 6,000 Kcal / kg. Accordingly, it is needless to say that the shape, size and shape of the semi-carbide can be freely formed in various forms.

When the semi-carbide forming unit 440 is supplied with the semi-carbide material, the semi-carbide forming unit 440 compresses the semi-carbide material into the shape of a molding fuel while pressing the material to the side of the discharge port. By-products generated during molding are recovered and transferred to the half- The molded fuel after the molding is stored in a separate fuel storage unit, and nitrogen gas, which is an inert gas, is periodically injected through the control of the controller 600 to prevent combustion due to the surrounding environment.

The control unit 600 controls the driving of the raw material treatment unit 100, the mixture treatment unit 200 and the semi-carburetion treatment unit 300 and the half-carbide treatment unit 400. The first to third raw material storage units 112, 122, 132 are controlled so that the first raw materials supplied into the storage chamber 514 are not mixed with each other.

This is to control the moisture removal device 140 constituted in the storage chamber 512 according to the specific characteristic of each plant biomass so as to finely control the temperature and humidity to maintain the optimal state of the plant biomass .

The control unit 600 controls the driving of the first to third drying units 114, 124 and 134 and controls the supply amount of the hot air supplied from the hot air supply unit 528 and the amount of the hot air supplied from the hot air supply unit 528, The first to third raw material supply units 116, 126, and 136 may be controlled to adjust the supply amounts of the masses.

In addition, the control unit 600 of the present invention controls the supply amounts of the vegetable or animal biomass supplied through the raw material mixing unit 210 to be mixed at a predetermined ratio, The temperature and humidity sensor can be controlled so that the temperature and humidity of the air conditioner can be maintained constant.

In addition, the controller 600 controls the binder supply unit to adjust the supply amount and supply amount of the binder supplied to the half-charger 310, and controls the binder supply unit to remove the build- It is preferable to control the temperature and the supply amount of the heat source to control the high-quality semi-carbonization.

The control unit 600 of the present invention includes a data management unit 630 that stores data on the moisture and calorific value of the biomass that is input to the first to third raw material storage units 112, 114, and 116, respectively And data on moisture and calorific value of the stored biomass transmitted from the moisture removal device 140 and the temperature and humidity sensor are transmitted to the data management unit 630, A raw material detecting unit 610 for controlling the driving of the raw material treating unit 100 and the mixture treating unit 200 is constructed so that water and drying are performed.

When the mixed raw material is semi-carbonized in the semi-carbonization processing unit 300, the control unit 600 controls the oxygen contained in the carbonized furnace to be removed, so that the mixed raw material is carbonized at a temperature of 250 to 300 ° C A reaction regulating unit 620 for controlling the reaction temperature and reaction time (residence time of the mixed raw material) of the semi-carbonization treatment unit 300 is configured.

In addition, the control unit 600 of the present invention includes a supply amount adjusting unit 640 for controlling the supply amounts of the first to third raw material supplying units 116, 126 and 136, respectively, by the respective types of the biomass.

For example, in order to produce a semi-carbide having a calorific value of 4,000 Kcal / kg, the supply amount regulating unit 640 controls the feed amount of the plant biomass to 10% by weight based on the weight of the mixed raw material through the first raw material supplying unit 116 And the second raw material supply unit 126 controls the amount of the animal biomass to be supplied in an amount of 30% by weight based on the weight of the mixed raw material. In the case of the third raw material supply unit 126, It is possible to control the supply to the mixture processing unit 200 side.

Here, it is a matter of course that the mixing ratio may be varied according to the amount of heat required by the user, for example.

The present invention thus configured can maximize the strength and density in the semi-carbonization process of the biomass feedstock to improve the combustion efficiency of the semi-carbonized fuel by improving the calorific value of the semi-carbonized fuel to 3,000 ~ 6,000 Kcal / kg, Carbonized fuel made of vegetable, animal and organic biomass that is mixed with biomass including wood, wood, bovine, rice husk, rice straw and sludge and minimized moisture content, It is an invention that can be received.

While the present invention has been described in connection with what is presently considered to be the most practical and preferred embodiments, it is to be understood that the invention is not limited to the disclosed embodiments. That is, within the scope of the present invention, all of the components may be selectively coupled to one or more of them.

It is also to be understood that the terms such as " comprises, "" comprising," or "having ", as used herein, mean that a component can be implanted unless specifically stated to the contrary. And all terms including technical and scientific terms are to be construed in a manner generally known to one of ordinary skill in the art to which this invention belongs, It has the same meaning as understood.

The foregoing description is merely illustrative of the technical idea of the present invention, and various changes and modifications may be made by those skilled in the art without departing from the essential characteristics of the present invention. Therefore, the embodiments disclosed in the present invention are intended to illustrate rather than limit the scope of the present invention, and the scope of the technical idea of the present invention is not limited by these embodiments. The scope of protection of the present invention should be construed according to the following claims, and all technical ideas within the scope of equivalents should be construed as falling within the scope of the present invention.

100: raw material processing unit 110:
120: second supply part 130: third supply part
140: Water removal device 200: Mixture processor
210: raw material mixing part 220: mixture storage part
230: Mixture drying section 240: Mixture supply section
300: half-carbonization processing unit 310: half-
320: heat source supply unit 330: refining unit
400: Half-carbide treatment unit 410: Semi-
420: Half-carbide storage part 430: Half-carbide non-
440: Half-carbide forming section

Claims (12)

A raw material treatment unit for separately drying and crushing the biomass, the first supply unit storing vegetable biomass, the second supply unit storing the animal biomass, and the third supply unit storing the organic biomass, respectively;
A raw material mixing unit connected to the raw material processing unit and mixing the dried and ground biomass with the binder in accordance with a user's request to produce a mixed fuel constituting a half carbohydrate; A mixture treatment section including a storage section and a mixture supply section for supplying the mixed fuel to the semi-carbonization treatment section;
A semi-carbonization treatment unit for removing oxygen from the mixed fuel to carbonize the fuel to produce a semi-carbide;
A semi-carbide treatment unit for supplying the semi-carbide manufactured by the semi-carbide treatment unit and selectively performing non-molding or molding of the semi-carbide according to a user's request; And
And a control unit for controlling the driving of the raw material treatment unit, the mixture treatment unit, the semi-carbonization treatment unit and the half-carbide treatment unit,
The first to third supply units include first to third raw material storing units in which respective biomass are individually stored, and biomass is transferred from the first to third storing units, and the transferred biomass to the control unit Further comprising first to third raw material supplying units for supplying the raw material to the raw material mixing unit under the control of the control unit,
Wherein the first to third raw material storage units are provided with an input unit into which vegetable, animal, or organic biomass is input, and biomass storage units through which the biomass is divided, A moisture removal device for removing moisture contained in the biomass, and a supply member for supplying the vegetable, animal, or mixed biomass to the raw material mixing unit under the control of the control unit Including,
And a sealing plate disposed on the upper portion of the storage chamber for rotating the loading unit, a driving motor for rotating the rotating plate, and a sealing plate for selectively sealing the charging holes of the storage chamber. Carbide production system using mixed biomass.
The method according to claim 1,
Characterized in that the first to third drying units for drying the respective biomass constituted and stored between the first to third raw material storing units and the first to third raw material supplying units are selectively constituted. The apparatus for producing a semi - carbide.
delete delete 3. The method of claim 2,
The first to third drying units
An inner cylinder for transporting and drying the biomass;
An outer tube which is formed on an outer periphery of the inner tube and circulates a predetermined hot air to dry the biomass;
A transfer screw configured to transfer the biomass to the inner periphery of the inner cylinder;
And a hot air supply unit provided on one side of the outer cylinder for providing a predetermined amount of hot air under the control of the control unit,
The apparatus for producing a semi-carbide using mixed biomass according to claim 1,
3. The method of claim 2,
The first to third raw material supplying units
A crusher connected to the first to third drying units for crushing the dried biomass to a predetermined size under the control of the control unit,
A quantitative feeder for quantitatively feeding the pulverized products of the pulverized biomass to the raw material mixing portion side,
The apparatus for producing a semi-carbide using mixed biomass according to claim 1,
The method according to claim 1,
The raw material mixing portion
An agitator composed of an impeller for mixing the vegetable, animal and organic biomass,
A crushing blade configured to crush the biomass in the impeller;
Further comprising a biomass-containing material.
The method according to claim 1,
Wherein the mixture storage unit is constituted by a temperature and humidity sensor interlocked with the control unit so that the temperature and the humidity inside can be always kept constant.
The method according to claim 1,
Wherein the mixture treatment unit further includes a mixture drying unit connected to the raw material mixing unit to dry the biomass.
The method according to claim 1,
The semi-
A semi-carbonated portion for semi-carbonizing the mixture;
A heat source supply unit for supplying a heat source to the semi-carbonized part side; And
A refining unit for refining the harmful gas generated during carbonization of the mixture by inhalation;
The apparatus for producing a semi-carbide using mixed biomass according to claim 1,
The method according to claim 1,
The half-carbide treatment section
A semi-carbonization discharge unit for receiving the semi-carbonized semi-carbonized material through the semi-carbonated processing unit to cool the semi-carbonized material and discharging the cooled semi-carbonized material;
A semi-carbide storage part for storing the semi-carbide discharged from the semi-carbonated discharge part;
A semi-carbide forming unit for receiving a predetermined amount of semi-carbide from the semi-carbide storage unit and processing the same to produce a semi-carbide having a calorific value of 3,000 to 6,000 Kcal / kg;
A predetermined amount of semi-carbide is supplied from the semi-carbide storage portion, and a half-carbide non-forming portion having a predetermined amount of heat generated while maintaining the shape of the half-
The apparatus for producing a semi-carbide using mixed biomass according to claim 1,
The method according to claim 1,
The control unit
A data management unit for storing data on moisture and calorific value of the biomass;
A raw material detecting unit which receives data on the moisture and calorific value of the biomass stored in the first to third raw material storing units and compares and analyzes the data with the data recorded in the data managing unit to control the driving of the raw material treating unit and the mixture treating unit;
A reaction regulator for controlling the reaction temperature and the reaction time of the semi-carbonization treatment unit so as to control the oxygen present in the semi-carbonization treatment unit to be removed and perform semi-carbonization of the mixed raw material;
A supply amount regulating unit for controlling the supply amount of each type of biomass by individually controlling each of the first to third raw material supplying units,
The apparatus for producing a semi-carbide using mixed biomass according to claim 1,

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