JP2007091889A - Manufacturing system of biomass fuel - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a manufacturing system of a lignous biomass fuel that can efficiently carbonize and grind lignous biomass and can feed it as a fuel to power generation equipment or the like. <P>SOLUTION: The manufacturing system comprises a carbonizing furnace for carbonizing ligneous biomass by utilizing waste heat from a refuse incinerator and a grinding machine for grinding the ligneous biomass after carbonized, and feeds a dry-distilled gas generated when the ligneous biomass is carbonized in the carbonizing furnace as a part of fuels from the carbonizing furnace to the refuse incinerator. In this system, carbonization of the ligneous biomass is carried out utilizing waste heat from refuse incineration sites while the dry-distilled gas generated on carbonization is fed as a fuel to a boiler of the refuse incinerator and therefore the biomass fuel is efficiently manufactured. As there are many refuse incineration sites in the country, utilization of waste heat therefrom permits reduction in energy cost for carbonizing ligneous biomass. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

The present invention mainly targets woody biomass (hereinafter sometimes referred to as woody biomass) represented by forestry (sawmill waste, thinned wood, firewood, etc.) waste wood and construction waste wood. As described above, the woody biomass is efficiently carbonized and pulverized to effectively utilize the biomass as a fuel.

In response to the amendment of the “Special Measures Law for Promotion of New Energy Use” in 2002, biomass energy has been recognized as new energy. It was obliged to use more than the standard amount of new energy.

“Biomass”, recognized as new energy, is a collective term for biomass, such as agriculture (wheat straw, sugarcane, rice bran, vegetation, etc.), forestry (waste wood, thinned wood, wood firewood, etc.), livestock ( Livestock waste), fisheries (fishery processing residue), waste (garbage, construction waste), etc. One of the aforementioned legal purposes is to protect these biomass for environmental protection. Is to be used as new energy. At present, in order to search for an effective utilization method of biomass, many schemes have been tried, and methods such as chipping and burning biomass or gasifying it are already known.

As one of the biomass utilization methods described above, in thermal power generation facilities and the like, there is an expectation for a method of co-firing woody biomass with coal and the like as a fuel, and electric companies are also actively investigating.
In addition, when co-firing the woody biomass described above with a coal-fired power generation facility, it is efficient to make fine powder having a predetermined particle size or less in a carbonized state of the woody biomass. Are listed.

JP 2005-114261 A

However, the method disclosed in Patent Document 1 described above requires thermal energy for carbonizing the woody biomass, unlike the case where the woody biomass is directly fed as fuel into a boiler or the like. The problem is whether it can be made more efficient.

  In addition, generally, woody biomass before carbonization is bulky, so that the amount that can be transported at one time by transportation means such as a truck is limited, and transportation efficiency is poor. Therefore, when woody biomass is directly brought into a power generation facility or the like and carbonized and pulverized there to obtain a fuel, there arises a problem that transportation efficiency is poor.

  Since woody biomass is reduced in weight and volume by carbonization and pulverization, the transport of biomass after carbonization and pulverization is more efficient than the transport of biomass before carbonization, and the transport distance of biomass before carbonization is reduced. There was a need for a woody biomass production system that could be shortened as much as possible.

An object of the present invention is to provide a production system of woody biomass fuel that can efficiently carbonize and pulverize woody biomass and supply it as a fuel to a power generation facility.

In order to achieve the above object, the present invention provides:
(1) A biomass fuel production system comprising: a carbonization furnace that carbonizes woody biomass using waste heat from a waste incinerator; and a pulverizer that carbonizes the woody biomass and then pulverizes the woody biomass, It is set as the structure provided with the piping which supplies the carbonization gas produced when carbonizing wood type biomass with a carbonization furnace from this carbonization furnace to this garbage incinerator as a part of fuel.

(2) In the method for producing biomass fuel according to (1), the carbonized woody biomass after the carbonization is pulverized by a vertical pulverizer.

According to the present invention, the waste biomass of the waste incineration plant is used to carbonize the woody biomass, and the dry distillation gas generated during the carbonization is supplied to the boiler of the waste incinerator for fuel. Biomass fuel can be produced efficiently.
In addition, many waste incinerators are installed in the country, and waste heat can be used, so energy costs for carbonizing woody biomass can be saved.
Since woody biomass before carbonization is bulky, there is a problem that the amount that can be conveyed at one time is limited and the conveyance efficiency is poor, and the woody biomass is brought directly into power generation facilities etc. In the case of fuel, transportation costs are inevitably high. However, in the case of the present invention, by using a waste incineration plant that is installed in large numbers in Japan, it is possible to carbonize and pulverize in a place close to the place where the biomass is generated, and the power generation equipment is in a reduced or reduced volume state. Can be transported to etc.

Preferred embodiments of the present invention will be described below with reference to the drawings.
1 to 6 are diagrams for explaining an embodiment of the present invention. FIG. 1 is a conceptual diagram of a woody biomass fuel production system used in the embodiment. FIG. 2 is a vertical crusher used in the embodiment. It is principal part sectional drawing for demonstrating this structure.
FIG. 3 is a perspective view for explaining the primary crusher, and FIG. 5 is a perspective view for explaining the granulator. 4 and 6 are conceptual diagrams for explaining the carbonization furnace structure.

A preferred example of a biomass fuel production system used in the embodiment of the present invention will be described with reference to FIG.
The biomass fuel manufacturing system used in the present embodiment is a primary system that cuts woody biomass such as sawmill waste and thinned wood into a carbonization furnace 50 adjacent to the waste incineration plant 100 installed in various places in Japan. Crusher 40, carbonization furnace 50 that uses waste heat from the waste incineration plant, cooling device 60 that cools the charcoal of woody biomass discharged from the carbonization furnace 50, preliminary that preliminarily pulverizes (coarsely pulverizes) the cooled carbide A pulverizer 70, a centrifuge 80 for removing foreign substances from the pre-ground carbide, a vertical pulverizer 1 for pulverizing (finely pulverizing) the carbonized raw material into a size suitable for combustion, and granulating the pulverized raw material A pelletizer 90 for pelletizing is provided, and a boiler facility (such as a power plant) that uses biomass fuel is provided with a crusher 150 for crushing the pelletized biomass fuel.

Further, in the present embodiment, the dry distillation gas is supplied as a part of fuel from the carbonization furnace 50 to the waste incinerator of the waste incineration plant 100 from the carbonization furnace 50 to carbonize the woody biomass in the carbonization furnace 50. A supply pipe L is provided.
Here, since the woody biomass before carbonization is bulky, the amount that can be transported at one time is limited, the transport efficiency is poor, and the cost is high because it is transported as fuel.
In order to solve this problem, it is preferable to carbonize the place where the woody biomass is generated as close as possible, reduce the volume or reduce the volume, and then transport to a power generation facility or the like. The inventors of the present application can easily collect woody biomass with the waste incineration plant 100 widely installed in various places in Japan, and can use waste heat for carbonization. Focusing on the fact that the dry distillation gas generated in the waste incinerator can be used as fuel for the incinerator, the waste heat from the exhaust gas from the waste incineration plant 100 is used, and the boiler fuel for the incinerator equipped with the dry distillation gas in the waste incineration plant 100 Carbonize woody biomass while using as
Therefore, in the present embodiment, the dry distillation gas generated when carbonizing the woody biomass in the carbonization furnace 50 is supplied to the boiler of the waste incinerator and used as the fuel, so that the biomass fuel can be efficiently manufactured.

Hereinafter, the process flow in the biomass fuel production system will be briefly described. Woody biomass such as waste wood that has been transported and collected to the waste incineration plant 100 is input to the primary crusher 40 and is then supplied to the carbonization furnace 50. Cut to the size that can be inserted.
The crushed woody biomass is charged into the carbonization furnace 50 and carbonized (sometimes referred to as dry distillation), then cooled by the cooling device 60, and then charged into the preliminary pulverizer 70 and coarsely pulverized. The

The woody biomass taken out from the preliminary pulverizer 70 is put into the centrifugal separator 80 to remove foreign matter, and then put into the vertical pulverizer 1 and pulverized to a particle size suitable for combustion. become. The woody biomass in the form of fine powder is taken out from the vertical crusher 1 and then put into the granulator 90 where it is pelletized and then conveyed.

The pellet-like woody biomass is transported to a boiler-holding facility such as a power plant, and then finely pulverized again by the crusher 150 provided therein, and used as fuel in that state.

  Here, the carbonization furnace 50 used in the embodiment described in FIG. 1 is a two-layered rotary kiln type carbonization furnace, as shown conceptually in FIG. 4 and FIG. Waste heat from waste incineration facilities is used as a heat source. FIG. 4 conceptually shows the flow of raw material and the flow of gas, but passes wood furnace biomass 44 from the raw material charging port 43 of the carbonization furnace 50 and passes through the furnace tube 44 of the inner cylinder 42 in which the supply of air is restricted. In addition, the exhaust gas from the waste incinerator installed in the waste incineration plant 100 is caused to flow into the space 45 between the outer cylinder 41 and the inner cylinder 42 disposed on the outside of the inner cylinder 42, and the amount of heat of the exhaust gas The wood biomass was heated and carbonized.

The scope of application according to the present invention is not limited to the above-described embodiment, and a known carbonization method or the like may be performed. For example, the carbonization furnace 50 is a closed type charcoal furnace type, a trolley type, a stirring type, or the like. Alternatively, a screw type or the like such as a continuous rotary type or a repetitive swing type may be used.

  Further, the carbonization conditions used in the carbonization furnace 50 vary depending on the type of the carbonization furnace 50, the type of woody biomass to be treated, and the like. It is common to carbonize in the range of about 700 ° C.

Next, the primary crusher 40 used in the present embodiment will be briefly described with reference to FIG. 3. The raw material charged from the raw material input port 42 of the primary crusher 40 is sandwiched between crushing rollers 43 to a predetermined size. In addition, as another form of the primary crusher, for example, a primary crusher of a type generally called a jaw crusher may be used, and a primary crusher of a type generally called a jaw crusher is Among them, a swing jaw (movable plate) that supports one end is rocked back and forth toward the fixed plate, thereby crushing crushed material between the fixed plate and the swing jaw. In addition, like the carbonization furnace 50 described above, the primary crusher 40 is not limited to the above-described form, and a known crusher or crusher may be used without departing from the technical idea of the present invention. A method may be used.

  Further, although not shown in detail, in the embodiment of the manufacturing system described in FIG. 1, a water-cooled type is used as the cooling device 60. In addition, like the carbonization furnace 50 or the primary crusher 40 described above, the cooling device 60 is of course not limited to the present embodiment, and is well-known within the scope of the technical idea of the present invention. A cooling device may be used.

Next, the preliminary pulverizer 70 used in FIG. 1 will be described.
In the embodiment of the crushing system described in FIG. 1, the crusher of the type shown in FIG. 3 is used as the preliminary crusher 70 as with the primary crusher 40.
For example, when the woody biomass to be treated is construction (architectural) waste wood and metal foreign matter is mixed in it, the metal foreign matter is woody even if it is cut by the primary crusher 40 before carbonization. It is difficult to separate by leaving it in the biomass.
If the primary crusher 40 is crushed finely, the foreign matter is separated. However, if the foreign matter remains finely crushed, the primary crusher 40 may be damaged by the metal foreign matter.

In contrast, since the biomass itself is brittle after carbonization of the woody biomass, it is possible to easily separate foreign substances without pulverizing so finely.
Further, if woody biomass with metal foreign matter remaining is put into the vertical crusher 1, the crushing roller 3 of the vertical crusher 1 or the upper surface 2A of the rotary table may be damaged. In the worst case, In addition, sparks may be generated by rubbing between metals, leading to a serious disaster such as a fire. For the reasons described above, when metal foreign matter is mixed in the woody biomass to be treated, it is effective to use the preliminary pulverizer 70.
The preliminary pulverizer 70 provided for the above-described reason is a case where no metal foreign matter is mixed in the woody biomass to be treated, and the woody biomass taken out from the carbonization furnace 50 is directly input to the vertical pulverizer 1. It can be omitted when the size is such that it can be crushed to a size that can be charged into the vertical crusher 1 by the primary crusher 40.

  Next, the woody biomass pulverized by the preliminary pulverizer 70 is put into the centrifugal separator 80 to remove foreign matters. As for the method for removing foreign matter, the centrifugal separator 80 is a preferable form in that it can remove things such as ceramics, cements, and earths other than metallic foreign matters. Of course, it is not limited, and a known foreign substance removing device (for example, a magnet type metal removing device) may be used without departing from the technical idea of the present invention.

Hereinafter, the vertical crusher 1 used in this embodiment will be described. The vertical crusher 1 used in the present embodiment includes a rotary table 2 driven by an electric motor 2M via a speed reducer 2B installed at the lower part of the vertical crusher 1, as shown in FIG. And a plurality of conical crushing rollers 3 disposed at positions that equally divide the outer peripheral portion of the upper surface (sometimes referred to as the rotary table upper surface 2A) in the circumferential direction. The crushing roller 3 is pressed in the direction of the rotary table upper surface 2A and rotates by being driven by the raw material through the rotary table upper surface 2A.

  The vertical pulverizer 1 shown in FIG. 2 is a so-called inner partial type air sweep type in which a rotary separator 14 having a classification function is provided inside the vertical pulverizer 1. During operation, this type of vertical crusher 1 introduces gas into the machine to generate a gas stream that passes from the lower side of the rotary table through the separator 14 to the upper outlet 39.

  The raw material charged from the raw material charging chute 13 is caught by the rotary table upper surface 2A and the pulverizing roller 3 and crushed. 30) and is transported by the gas to the separator 14 where the raw material having a predetermined particle size or less is taken out from the upper outlet 39 as a pulverized product together with the gas.

  Note that the type of vertical crusher 1 that can be used in the present invention is not limited to the above-described inner partial class of air sweep, and may be, for example, a fixed type separator 14 according to the required particle size of the product. An external circulation type vertical crusher that does not include a separator may be used. Needless to say, the grinding roller 3 may be a spherical type tire crusher 1 having a spherical shape.

  Further, in the embodiment shown in FIG. 1, the woody biomass that has been pulverized by the vertical pulverizer 1 into a fine powder is put into a granulator 90 to be pelletized. FIG. 5 shows a perspective view of the granulator 90. In this embodiment, a roll type pellet apparatus having a simple structure is used as the granulator 90. The reason for pelletizing woody biomass is for the purpose of improving storage efficiency and transportation efficiency. Usually, woody biomass that has been finely pulverized from woody biomass fuel in pellet form is used. Since it is easier to burn, in this production system, after pelletization, after transporting to a power plant, the pellet is crushed and re-combusted again into a fine powder that is easy to burn. Therefore, in this production system, it is preferable not to use a strong molding aid or the like when pelletizing, and it is possible to obtain a pellet in a state that can be crushed immediately if necessary with an appropriate amount of hydrogenation or the like. preferable.

  The woody biomass that has been crushed and finely ground again burns in a boiler or the like as woody biomass fuel.

Hereinafter, one example of a preferred embodiment will be briefly described below regarding the operating state of the woody biomass production system according to the present invention using the system of FIG.

Wood biomass such as construction waste timber and thinned wood that have been collected up to the garbage incineration plant 100 by means of transportation such as trucks is put into the primary crusher 40 to a size that can be put into the carbonization furnace 50. Crush.
In the present embodiment, the thinned wood is crushed to a size of about 30 cm square so that it can be easily fed from the charging port of the carbonization furnace 50. (If the collected woody biomass has a shape and dimensions that can be charged into the carbonization furnace 50 without primary crushing, the primary crushing step may be omitted.)

As the next step, the crushed biomass is put into a carbonization furnace 50 and carbonized.
The carbonization conditions of the carbonization furnace 50 used at this time are not particularly limited depending on the type of woody biomass to be processed by the carbonization furnace 50, but are generally carbonized in the range of about 500 ° C to 600 ° C. In this case, dry distillation gas is generated in the furnace tube 44 of the carbonization furnace 50 by heating the woody biomass. The dry distillation gas flows through the dry distillation gas supply pipe L, and is a boiler of the incinerator. It is used as fuel.

  After the carbonization, the woody biomass is taken out from the carbonization furnace 50 and then charged into the cooling device 60 and cooled to 100 ° C. or lower. The cooling temperature at this time may be a temperature at which the carbonized woody biomass can be charged into the preliminary pulverizer 70 without being oxidized even if it is put into the atmosphere.

The cooled woody biomass is put into the preliminary pulverizer 70 and pulverized to about 1 cm square. Then, the woody biomass pulverized by the preliminary pulverizer 70 is put into the centrifugal separator 80 to remove foreign substances such as metals. Here, the woody biomass after carbonization is very fragile and easily broken unlike the woody biomass before carbonization. Therefore, crushing and crushing are easy, and the metal foreign matter and the like that have been fixed can be easily separated in this step.

The woody biomass from which foreign matter has been removed is put into the vertical crusher 1 and crushed to a particle size suitable for combustion as a woody biomass fuel.
The particle size can be adjusted by changing the flow rate of the gas flowing to the vertical crusher 1, the pressing force of the crushing roller 3, the rotation speed of the rotary table 2, and the like.

In the next step, the finely ground woody biomass is put into a granulator 90 and transported to a power plant or the like in a pelletized state. In addition, the woody biomass is easy to be transported by reducing the volume or reducing the volume at the time of carbonization and pulverization, and an effect of improving transport efficiency can be expected.
In the present embodiment, by further pelletizing it, the risk of dust explosion and the like is reduced to facilitate handling.

The pellet-like woody biomass transported to a power plant or the like is crushed by a crusher 150 installed in the power plant and is charged as fuel into a power generation boiler.
Here, since the woody biomass pulverized by the vertical pulverizer 1 is only granulated and aggregated, it can be easily pulverized by the pulverizer 150.

As described above, the woody biomass before carbonization is bulky, so the amount that can be carried at one time is limited, and transportation is not easy. Therefore, it is preferable to carbonize at a place as close as possible from the place where the biomass is generated, reduce the amount of the woody biomass by carbonization and reduce the volume, and then deliver to a power generation facility or the like.
In this embodiment, the woody biomass is carbonized using a waste incinerator widely installed in various places in Japan to save thermal energy during carbonization, and further, carbonization with poor transport efficiency. The transport distance of the previous woody biomass can be shortened and efficiently transported in a reduced volume, and the dry distillation gas generated during carbonization is sent to the waste incinerator boiler to produce fuel. Therefore, biomass fuel can be produced efficiently.

BRIEF DESCRIPTION OF THE DRAWINGS It is a conceptual diagram for demonstrating the structure of the manufacturing system of woody biomass fuel concerning embodiment of this invention. It is principal part sectional drawing for demonstrating the structure of the vertical crusher concerning embodiment of this invention. It is a perspective view for explaining a primary crusher concerning an embodiment of the present invention. 1 is a perspective view for explaining a carbonization furnace according to an embodiment of the present invention. It is a perspective view for explaining a granulator concerning an embodiment of the present invention. It is a side view for demonstrating the carbonization furnace structure in connection with embodiment of this invention.

Explanation of symbols

DESCRIPTION OF SYMBOLS 1 Vertical crusher 2 Table 3 Crushing roller 13 Chute 14 Separator 15 Dam ring 33 Gas inlet 35 Raw material inlet 39 Upper outlet 40 Primary crusher 50 Carbonization furnace 60 Cooling device 70 Preliminary crusher 80 Centrifuge (centrifugation) apparatus)
90 Granulator 100 Garbage incinerator 150 Crusher

Claims (2)

A biomass fuel production system comprising: a carbonization furnace that carbonizes wood biomass using waste heat from a waste incinerator; and a pulverizer that carbonizes the wood biomass and then pulverizes the wood biomass,
A biomass fuel production system comprising a pipe for feeding dry distillation gas generated when carbonizing woody biomass in the carbonization furnace from the carbonization furnace to the waste incinerator as a part of fuel.   The biomass fuel production system according to claim 1, wherein the carbonized woody biomass is pulverized by a vertical pulverizer.

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