JP2024040246A - Gasification device - Google Patents

Abstract

To provide a gasification device which can efficiently gasify a semi-carbonization-treated wood chip.SOLUTION: A gasification system 1 is composed of: a conveying device 20 which feeds a semi-carbonized wood chip S; and a reaction tower 11 which gasifies the semi-carbonized wood chip S. The conveying device 20 has a vertical direction conveying path 50 through which the semi-carbonized wood chip S is conveyed in a vertical direction from a bottom of the reaction tower 11 to an inside. The reaction tower 11 is provided on an upper part with a release pipe 12 through which a gas generated from gasification of the semi-carbonized wood chip S is released. The vertical direction conveying path 50 is configured to be a tubular shape along the vertical direction. A vertical direction screw blade 52 formed in a spiral shape along the vertical direction and rotatable around an axis along the vertical direction as a rotational axis is provided in the pipe. An upper end part of the vertical direction screw blade 52 is exposed above the bottom of the reaction tower 11.SELECTED DRAWING: Figure 1

Description

The present invention relates to a gasifier for gasifying wood chips.

In recent years, environmental issues have become a hot topic, and instead of power generation using fossil fuels such as oil and coal, for example, combustion materials generated from biomass fuels such as naturally derived wood chips and torrefied wood chips are being used. Research is progressing on power generation equipment, etc.

As an example of a gasification device that generates such combustion substances from biomass fuel, a gasification agent such as air or steam is supplied from a gasification agent supply port provided at the bottom of the reaction tower, while a gasification agent is supplied to the top of the reaction tower. Patent Document 1 discloses a gasification apparatus that inputs biomass fuel from a provided input port, heats it, and gasifies the biomass fuel.

This gasifier is a so-called updraft type gasifier, in which a discharge port is installed at the upper side of the reaction tower to release generated gas generated from biomass fuel, and the gasifier at the bottom is not gasified. It is equipped with an ash discharge section to remove biomass ash.

According to the gasifier disclosed in Patent Document 1, the biomass fuel introduced from the top is gasified inside the reaction tower, and the biomass fuel (combustion residue) that has fallen without being completely gasified is stabilized. It is said that it can be eliminated by

However, the size of the biomass input into the reaction tower varies, and combustion residue that has not been sufficiently gasified and falls is removed. For this reason, there has been a problem that these combustion residues cannot be effectively utilized, and the efficiency of gasifying biomass is reduced.

Japanese Patent Application Publication No. 2008-101215

SUMMARY OF THE INVENTION In view of the above-mentioned problems, an object of the present invention is to provide a gasifier that can efficiently gasify torrefied wood chips.

The present invention provides a gasification apparatus for gasifying wood chips, which comprises an input mechanism for inputting torrefied wood chips, and a reaction tower for gasifying the wood chips, wherein the input mechanism is provided with a tubular longitudinal conveying path along the vertical direction for conveying the wood chips from the bottom of the reaction column into the interior thereof, and the reaction column has an outlet for discharging gasified gas from the wood chips. A pipe is provided above, and the vertical conveyance path is formed in the pipe in a spiral shape along the vertical direction, and is provided with a vertical screw blade rotatable about an axis along the vertical direction as a rotation axis. , the upper end portion of the vertical screw blade is exposed above the bottom of the reaction tower.

The above-mentioned torrefaction treatment is a process to generate carbide by heating at a predetermined temperature (approximately 200 to 350 degrees) while limiting or cutting off the amount of oxygen supplied to turn wood chips into a material with a high carbon content. As expected. Thereby, solid fuel with high energy density can be obtained.
The longitudinal conveyance path does not necessarily have to completely coincide with the vertical direction, and may be any direction that intersects the vertical direction at an angle of less than 45 degrees, for example.

According to this invention, torrefied wood chips can be efficiently gasified.
To be more specific, the wood chips that have been torrefied can be transported from below to the top of the high temperature layer in the reaction tower, and the wood chips that have fallen without being gasified in the high temperature layer can be transported at the upper end of the vertical screw blade. It can be transported again to the high temperature layer in the reaction tower together with the wood chips newly introduced into the reaction tower.

Thereby, wood chips that have not been sufficiently gasified can be gasified together with new wood chips. That is, wood chips that have not been gasified inside the reaction tower can be circulated and reused, and wood chips with high energy density can be efficiently gasified.

In addition, since the wood chips that have fallen to the bottom can be transported upward again by the vertical screw blades, the wood chips that have fallen from above and are piled up can be broken down. This allows the stacked wood chips to collapse and eliminates the bridges formed by the wood chips. Therefore, wood chips can be stably gasified in the high temperature layer.

As an aspect of the present invention, the input mechanism is provided with an input port into which the wood chips are input on one end side, and a tubular upstream side connected in a cross direction intersecting with the longitudinal conveyance path on the other end side. A side conveyance path may be provided, and the upstream conveyance path may be formed in a spiral shape within the pipe, and may include an upstream screw blade that conveys the wood chips toward the longitudinal conveyance path by rotation. good.

According to this invention, the wood chips can be divided into small pieces when the wood chips are transported from the upstream transport path to the vertical transport path. Thereby, the wood chips finely divided into desired sizes can be transported to the reaction tower, so that the wood chips can be efficiently gasified.

To explain in detail, the wood chips carried out from the upstream conveyance path by the upstream screw blades are taken into the vertical conveyance path by the vertical screw blades and conveyed, but the conveyance amount of the upstream screw blades and the vertical screw blade are By adjusting the amount of conveyance of the blades, the wood chips can be compacted and fragmented between the vertical conveyance path and the upstream conveyance path, and can be made into a desired size. In this way, by fragmenting the wood chips into desired sizes, it is possible to prevent the wood chips transported to the reaction tower from forming bridges, and the surface area of the fragmented wood chips is expanded. It can be gasified efficiently.

In addition, by individually adjusting the rotational speed of the upstream screw blade and the vertical screw blade, the subdivision size of the new wood chips to be conveyed can be adjusted, and the amount of new wood chips to be conveyed can be restricted to the bottom of the reaction tower. It is possible to reuse the wood chips accumulated in the factory or increase the amount of new wood chips transported. That is, wood chips can be gasified more efficiently depending on the conditions of the reaction tower.

Further, as an aspect of the present invention, the reaction tower may be provided with an injection part for injecting the gasifying agent.
According to the present invention, the gasification of the wood chips is promoted by the gasifying agent, so that the wood chips subjected to the torrefaction treatment can be more efficiently gasified.

Here, the gasification agent is a promoter that promotes gasification of wood chips, and includes, for example, air, oxygen, water vapor, and the like. Note that the gasifying agent is not limited to the above-mentioned gases, and may be gases other than the above-mentioned gases, powders, liquids, etc. as long as they can promote gasification of the wood chips.

Further, as an aspect of the present invention, a conveyance amount control section may be provided that controls the rotational speed of the vertical screw blade and adjusts the conveyance amount of the wood chips to be conveyed to the reaction tower.

The conveyance amount control unit performs the torrefaction treatment based on, for example, the accumulated amount and density of the wood chips introduced into the reaction tower, the temperature inside the reaction tower, the components of the gas released, or a combination thereof. The amount of transported wood chips may be controlled.

According to the present invention, the amount of torrefied wood chips to be transported can be adjusted according to the internal condition of the reaction tower, and wood chips with high energy density can be gasified more efficiently.
For example, if there are too many torrefied wood chips transported into the reaction tower, the amount of wood chips transported into the reaction tower is reduced, and the wood chips accumulated inside are heated up. It can be adjusted to decompose and gasify. On the other hand, if there are too few torrefied wood chips inside the reaction tower, the amount of torrefied wood chips conveyed to the inside of the reaction tower is increased, and the material for gasification is increased. can be increased and gasification can be promoted.

Further, as an aspect of the present invention, the reaction tower is provided with an accumulation amount detection unit that detects the amount of the wood chips accumulated inside the reaction tower, and the conveyance amount control unit is configured to include an accumulation amount detection unit that detects the amount of the wood chips accumulated inside the reaction tower. The rotation speed of the longitudinal screw blades may be controlled based on the detected amount of the wood chips.

According to the present invention, the amount of torrefied wood chips to be transported can be adjusted based on the detection result of the accumulation amount detection section. That is, depending on the amount of wood chips accumulated inside the reaction tower, the wood chips can be transported to the reaction tower and an appropriate amount of wood chips can be accumulated inside the reaction tower. Thereby, wood chips can be gasified more efficiently.

Further, as an aspect of the present invention, the reaction tower is provided with a temperature detection unit that detects an internal temperature, and the conveyance amount control unit controls the vertical screw blades based on the temperature detected by the temperature detection unit. The rotation speed may be controlled.

According to this invention, the amount of torrefied wood chips to be transported can be adjusted based on the detection result of the temperature detection section. That is, depending on the temperature inside the reaction tower, wood chips can be transported to the reaction tower and an appropriate amount of wood chips can be accumulated inside the reaction tower. Thereby, wood chips can be gasified more efficiently.

For example, if it is detected that the internal temperature of the reaction tower has increased compared to the desired temperature, the rotation speed of the vertical screw blades can be increased to transport more wood chips into the interior of the reaction tower. . On the other hand, if it is detected that the internal temperature of the reaction tower is lower than the desired temperature, the rotation speed of the vertical screw blades is lowered to reduce the amount of wood chips conveyed into the inside of the reaction tower. , the wood chips accumulated inside can be gasified. Therefore, wood chips can be gasified more efficiently.

Further, as an aspect of the present invention, an analysis section for analyzing the components of the gas may be provided, and the conveyance amount control section may control the rotational speed of the vertical screw blade based on the components of the gas.
According to the present invention, the amount of torrefied wood chips to be transported can be adjusted based on the detection results of the analysis section, and the wood chips can be gasified more efficiently.

Specifically, the components of the gas released from the reaction tower vary depending on the internal temperature of the reaction tower, the ratio of the gasifying agent, and the like. Therefore, by adjusting the amount of torrefied wood chips transported based on the components of the gas released, the internal temperature of the reaction tower and the ratio of gasification agent can be adjusted, resulting in a stable gas flow. supply. As a result, the amount of wood chips transported can be adjusted depending on the gasification state inside the reaction tower, allowing an appropriate amount of wood chips to be accumulated inside the reaction tower, and making it possible to gasify wood chips more efficiently. .

Further, as an aspect of the present invention, the discharge tube may be configured such that a negative pressure is applied to the distal end side.
According to the present invention, the gas that has been gasified inside the reaction tower can be sucked into the discharge pipe, so that the gasified gas can be reliably discharged from the discharge pipe.

Further, as an aspect of the present invention, the discharge tube may be provided with a narrow diameter portion whose tip end is narrower in diameter than the proximal end side.
According to this invention, since the distal end side of the discharge tube has a small diameter, the flow rate of generated gas, wood chips, etc. flowing through the narrow diameter portion is faster than at the proximal end side of the discharge tube. As a result, the temperature at the location where the flow rate is increased increases, so that wood chip residues that have not been completely gasified can be gasified within the discharge pipe.

Further, as an aspect of the present invention, an ash discharge section may be provided at the bottom of the reaction tower to discharge the wood chips accumulated at the bottom.
According to the present invention, wood chips and the like that have accumulated at the bottom of the reaction tower and are not transported upward again by the vertical screw blades can be discharged from the bottom.

According to the present invention, it is possible to provide a gasification device that can efficiently gasify wood chips that have been subjected to torrefaction treatment.

Schematic diagram of the gasification system. Schematic diagram of a conveyance device and a gasification reaction device. Gasification flowchart. Schematic diagram of wood chip fragmentation. Schematic diagram of the movement of wood chips inside the reaction tower.

One embodiment of this invention will be described below with reference to the drawings.
FIG. 1 shows a schematic diagram of the gasification system 1, FIG. 2 shows a schematic diagram of the gasification reactor 10 and the conveying device 20, FIG. 3 shows a flowchart of gasification by the gasification system 1, and FIG. 4 shows a surge A schematic diagram showing the transportation of the torrefied wood chips S stored in the tank 30 is shown, and FIG. 5 is a conceptual diagram showing the movement of the torrefied wood chips S inside the reaction tower 11.

The gasification system 1 gasifies wood chips that have been torrefied (hereinafter referred to as "semi-carbonized wood chips S") by thermally decomposing, burning, and reducing them, and collects the generated gas G from above. This is a draft gasification system.

Specifically, the gasification system 1 transports the torrefied wood chips S upward from the bottom of the reaction tower 11, which is a substantially cylindrical vertical container, and then converts the torrefied wood chips S into the torrefied wood chips in the reaction tower 11 whose internal temperature has been raised. Gasify S. The product gas G (carbon monoxide and hydrogen) generated by gasification in this manner is discharged from the discharge pipe 12 provided above the reaction tower 11 and stored in the gas storage section 60.

The structure of the gasification system 1 and the gasification of torrefied wood chips S using the gasification system 1 will be described below.
As shown in FIG. 1, the gasification system 1 includes a gasification reaction device 10 that gasifies torrefied wood chips S, and a transport device that transports the torrefied wood chips S, which are raw materials for gasification, to the gasification reaction device 10. It is composed of a device 20 and a gas storage section 60 that stores the generated gas G generated in the gasification reaction device 10.

The gasification reactor 10 includes a reaction tower 11 that gasifies semi-carbonized wood chips S, a discharge pipe 12 that releases the generated gas G generated in the reaction tower 11, and a gasification agent H that is supplied to the reaction tower 11 from the bottom. It is composed of a gasifying agent supply pipe 13. Further, inside the reaction tower 11, a heater 14 for increasing the internal temperature of the reaction tower 11, a temperature sensor 15 for detecting the internal temperature of the reaction tower 11, and torrefied wood chips stored inside the reaction tower 11 are installed. A storage amount detection sensor 16 that detects the storage amount of S is provided.

The reaction tower 11 is a substantially cylindrical vertical container, and the bottom portion has a conical shape that tapers downward. An insertion hole 11a for connecting to an upstream conveyance pipe 41, which will be described later, is provided at the apex of this cone. Furthermore, an ash discharge section 17 is provided at the bottom of the reaction tower 11 for scraping out the residue left after the semi-carbonized wood chips S have not been completely gasified.

In addition, when gasifying the torrefied wood chips S, inside the reaction tower 11, as shown in FIG. Three layers are formed in this order from the bottom to the top: a combustion zone T2 where carbonized wood chips S are burned, and a reduction zone T3 where generated gas G (carbon monoxide and hydrogen) is generated.

The discharge pipe 12 is a pipe for discharging the generated gas G generated inside the reaction tower 11 to the outside, and is provided at the upper part of the reaction tower 11 . As shown in FIG. 2, the discharge pipe 12 includes a proximal discharge pipe 12a connected to the side wall of the reaction column 11, a reduced diameter part 12b whose inner diameter decreases toward the distal end, and a reduced diameter part 12b. and a distal end discharge pipe 12c connected to the distal end discharge pipe 12c. Note that the distal end discharge tube 12c has a smaller diameter than the proximal discharge tube 12a.

A gas storage section 60 for storing the produced gas G and a suction device 71 for sucking the produced gas G are provided at the distal end of the distal end side discharge pipe 12c. Further, a part of the tip-side discharge pipe 12c is branched, and a gas analyzer 72 for analyzing the components of the generated gas G is attached.

This suction device 71 creates a negative pressure in the discharge pipe 12, and the generated gas G can be guided to the gas storage section 60.

A gas analyzer 72 provided in front of the gas storage section 60 collects the results of component analysis of the product gas G produced in the reaction tower 11 and transmits the analysis results to the rotation control section 73.
The rotation control unit 73 controls the rotation speeds of a rotary valve 33, an upstream screw blade 43, and a vertical screw blade 52, which will be described later, to control the amount of torrefied wood chips S to be transported to the reaction tower 11. There is.

The gasifying agent supply pipe 13 supplies the gasifying agent H (air and steam) supplied from the gasifying agent supply device 18 connected to the base end into the reaction tower 11 . This gasifying agent supply pipe 13 is composed of a first supply pipe 13a connected to the bottom of the reaction tower 11, and a second supply pipe 13b connected to the side of the central portion of the reaction tower 11.

The first supply pipe 13a is provided at the center of the rotating shaft of a vertical screw blade 52 installed in a vertical conveyance pipe 51, which will be described later, and gasifies upward along the longitudinal direction of the vertical conveyance pipe 51. Agent H can be supplied.

Note that the first supply pipe 13a only needs to be able to supply the gasifying agent H upward from the bottom of the reaction tower 11, and its position and number are not limited. For example, it may be arranged along the outer circumferential surface of the vertical conveyance pipe 51, or it may be arranged at another location at the bottom of the reaction tower 11.

The second supply pipe 13b is connected to the side surface of the central portion of the reaction tower 11, and can supply the gasifying agent H into the inside of the reaction tower 11 from the side. More specifically, it is arranged at a position corresponding to the reduction zone T3 of the reaction tower 11.

The heater 14 is a heating device for bringing the inside of the reaction tower 11 into a high temperature state in the initial state of gasifying the semi-carbonized wood chips S. Further, based on the temperature detection result by the temperature sensor 15, it may be used to raise the internal temperature of the reaction tower 11 when producing the product gas G.

Temperature sensor 15 detects the internal temperature of reaction tower 11 . Note that the detection result detected by the temperature sensor 15 is transmitted to the rotation control section 73.

The storage amount detection sensor 16 detects the amount of torrefied wood chips S accumulated inside the reaction tower 11. Specifically, inside the reaction tower 11, it is detected whether the accumulated torrefied wood chips S are lower or higher than a desired height. The temperature detection result detected by this storage amount detection sensor 16 is transmitted to the rotation control section 73. The rotation control unit 73 controls the rotation speeds of the rotary valve 33, the upstream screw blade 43, and the vertical screw blade 52, respectively, based on the transmitted result information.

The conveyance device 20 includes a surge tank 30 that stores torrefied wood chips S to be conveyed to the gasification reaction apparatus 10, and an upstream conveyance path 40 that conveys the torrefied wood chips S from the surge tank 30 to the gasification reaction apparatus 10. , and a vertical conveyance path 50 for conveying torrefied wood chips S to the reaction tower 11, and is equipped with an external screw feeder F having a rotation motor attached to its upper end.

The surge tank 30 is installed between a surge tank main body 31 for storing torrefied wood chips S, a supply pipe 32 connected to the lower end of the surge tank main body 31, and between the surge tank main body 31 and the supply pipe 32. It is composed of a rotary valve 33.

The supply pipe 32 is a tubular conveyance path, and one end thereof is connected to a fuel inlet 31a provided at the lower end of the tapered surge tank main body 31 via a rotary valve 33, and the other end is connected to the upstream conveyance path 40. are doing.
The rotary valve 33 is configured to be freely rotatable by a rotary valve motor 34 and can feed torrefied wood chips S stored in the surge tank main body 31 into the supply pipe 32. Note that the rotary valve motor 34 is controlled by the rotation control section 73 as described above. Furthermore, by providing the external screw feeder F, it is possible to prevent the bridging phenomenon of the torrefied wood chips S within the surge tank main body 31, and it is possible to more reliably supply the torrefied wood chips S to the supply pipe 32. .

The torrefied wood chips S stored in the surge tank main body 31 are carbon-rich wood chips obtained by thermally decomposing wood biomass such as wood chips at high temperatures of 200 to 350 degrees under anoxic conditions. It is a carbide. This torrefied wood chip S has a high energy density per weight and has good crushing performance.

As shown in FIGS. 1 and 2, the upstream conveyance path 40 includes an upstream conveyance pipe 41 configured in a tubular shape, and an intermediate conveyance pipe 42 curved from the lower end of the upstream conveyance pipe 41 toward the gasification reaction apparatus 10 side. , an upstream screw blade 43 installed inside the upstream conveyance pipe 41 , and a rotation motor 44 that rotationally drives the upstream screw blade 43 .

The upstream conveyance pipe 41 is a tubular body that stands upright along the vertical direction, and is provided with an input port 41a on the side to which the tip of the supply pipe 32 is connected. Further, a rotary motor 44 for rotationally driving the upstream screw blade 43 is provided at the upper end of the upstream conveying pipe 41 .

The intermediate conveyance pipe 42 is a tubular body whose orthogonal cross section perpendicular to the central axis has the same shape as the orthogonal cross section of the upstream conveyance pipe 41, and as shown in FIG. ing. Further, the base end of the intermediate conveyance pipe 42 is connected to the upstream conveyance pipe 41, and the distal end thereof is connected to a vertical conveyance pipe 51 forming a vertical conveyance path 50.

The upstream screw blade 43 is a blade used in a so-called spring conveyor, which is formed in a spiral shape and can rotate while bending. It extends from to the tip of the intermediate conveying pipe 42.

The upper end of the upstream screw blade 43 is connected to the rotary motor 44 and can freely rotate inside the upstream conveyance pipe 41 and the intermediate conveyance pipe 42 . Thereby, the torrefied wood chips S inputted from the input port 41a can be conveyed to the tip of the intermediate conveyance pipe 42.
Note that the rotation motor 44 is connected to a rotation control section 73, and the rotation speed of the upstream screw blade 43 is controlled by the rotation control section 73.

The vertical conveyance path 50 is composed of a tubular vertical conveyance pipe 51, a vertical screw blade 52 installed inside the vertical conveyance pipe 51, and a rotation motor 53 that rotationally drives the vertical screw blade 52. .
The vertical conveyance pipe 51 is a tubular body that stands upright along the vertical direction, and is arranged below the reaction tower 11 . The longitudinal conveyance pipe 51 is provided with a connecting portion on the side of the central portion thereof, which is connected perpendicularly to the intermediate conveyance pipe 42 connected from the lower end of the upstream conveyance pipe 41 .

The vertical screw blade 52 installed in the vertical conveyance pipe 51 is a so-called screw feeder, which is formed in a spiral shape along the vertical direction and is rotatable about an axis along the vertical direction as a rotation axis. The lower end of this vertical screw blade 52 is connected to a rotation motor 53 provided at the lower end of the vertical conveyance pipe 51, and can freely rotate inside the vertical conveyance pipe 51.

Further, the vertical screw blade 52 is configured to be longer than the vertical conveying pipe 51. For this reason, an exposed portion 52 a that protrudes from the upper end of the vertical conveyance pipe 51 is formed in the upper portion of the vertical screw blade 52 .
Note that the rotation motor 53 is connected to a rotation control section 73, and the rotation speed of the vertical screw blade 52 is controlled by the rotation control section 73.

The vertical conveyance path 50 configured in this manner is arranged below the reaction tower 11, and the upper end of the vertical conveyance pipe 51 is connected to the insertion hole 11a. Therefore, the exposed portion 52a, which is the upper end portion of the vertical screw blade 52, protrudes above the insertion hole 11a, that is, the bottom of the reaction tower 11.

Next, a method of transporting the torrefied wood chips S to the reaction tower 11 using the transport device 20 and gasification in the reaction tower 11 will be briefly explained based on FIG. 3.
As a step before operating the gasification system 1, torrefied wood chips S serving as a raw material are stored in the surge tank main body 31 (step s0). Since the torrefied wood chips S stored in the surge tank main body 31 have been torrefied, their mass is reduced to about 45 to 68% compared to the mass of the wood chips before being torrefied. ing.

First, in order to transport the torrefied wood chips S to the reaction tower 11, the rotary valve 33, intermediate transport pipe 42, and vertical screw blade 52 are rotated (step s1). As a result, the torrefied wood chips S stored in the surge tank main body 31 are conveyed to the supply pipe 32 while being crushed by the rotary valve 33, and are thrown into the upstream conveyance pipe 41 as they are. Furthermore, the torrefied wood chips S introduced into the upstream conveyance pipe 41 are conveyed downward along the upstream conveyance pipe 41 and the intermediate conveyance pipe 42 by the rotation of the upstream screw blades 43 .

Here, by setting the rotation speed of the vertical screw blade 52 to be slower than the rotation speed of the upstream screw blade 43, the torrefied wood chips S are consolidated in the intermediate conveyance pipe 42. When the torrefied wood chips S consolidated in the intermediate conveyance pipe 42 are fed into the vertical conveyance pipe 51, they are transported in the vertical direction while being finely divided by the vertical screw blades 52 rotating inside the vertical conveyance pipe 51. It will be put into the tube 51.
The semi-carbonized wood chips S thus introduced into the vertical transport pipe 51 are transported into the reaction tower 11 along the vertical transport pipe 51 by the rotation of the vertical screw blades 52 .

The torrefied wood chips S introduced into the reaction tower 11 in this way are subdivided into pieces that are about one-half to one-third the size of the torrefied wood chips S stored in the surge tank main body 31. has been made into Therefore, the torrefied wood chips S are accumulated inside the reaction tower 11 without forming bridges (see FIG. 4).

As shown in FIG. 5, the torrefied wood chips S transported to the reaction tower 11 in this manner rise up in the center by overcoming gravity due to the transport of the torrefied wood chips S by the vertical screw blades 52. On the other hand, since the radially outer portion of the reaction tower 11 is pressed downward by the bulge in the center, the torrefied wood chips S that have moved downward are consolidated by the torrefied wood chips S piled up above. and crushed.

Further, since the bottom of the reaction tower 11 is configured in a conical shape, the semi-carbonized wood chips S pressed downward gather in the center along the conical shape. The torrefied wood chips S gathered in the center in this way are wound around the vertical screw blades 52 and lifted upward again. Therefore, torrefied wood chips S (combustion residues of torrefied wood chips S) that have not been completely gasified can be prevented from accumulating at the bottom of the reaction tower 11.

Further, the reaction tower 11 in which the torrefied wood chips S are accumulated is heated to a temperature suitable for gasifying the torrefied wood chips S by the heater 14 when the gasification system 1 starts to be activated. Then, when gasification (thermal decomposition, combustion, reduction) of the torrefied wood chips S is started, the heater 14 is stopped. Thereafter, the internal temperature of the reaction tower 11 is basically controlled by the gasification combustion of the torrefied wood chips S.

When gasification of the semi-carbonized wood chips S starts, a generated gas G (carbon monoxide/hydrogen) is generated inside the reaction tower 11, and this generated gas G is disposed at the top and discharged with negative pressure on the tip side. drawn into tube 12. Thereby, the generated gas G can be stored in the gas storage section 60.

In addition, since the distal end side of the discharge pipe 12 is under negative pressure, the inside of the reaction column 11 is Gasifying agent H is supplied. In this way, the gasifying agent H supplied to the reaction tower 11 becomes an upward airflow through the discharge pipe 12, so that the gasification of the torrefied wood chips S inside the reaction tower 11 can be promoted, and the It is possible to raise torrefied wood chips S.

Thereby, in accordance with the promotion of gasification of the finely divided torrefied wood chips S, it is possible to further prevent torrefied wood chips S that have not been completely gasified from accumulating at the bottom of the reaction tower 11. Furthermore, it is possible to help draw the combustion residue of the torrefied wood chips S, which has not been completely gasified, into the discharge pipe 12.

Here, in the discharge tube 12, since the proximal discharge tube 12a and the distal discharge tube 12c are connected by the diameter-reduced portion 12b, the flow velocity of the torrefied wood chips S flowing inside the discharge tube 12 is lower than the diameter-reduced portion. 12b and the distal discharge tube 12c. As a result, the temperature of the combustion residue of the torrefied wood chips S that has not been completely gasified increases, so that the combustion residue of the torrefied wood chips S can be completely gasified.
Thereby, it is possible to prevent combustion residues of the torrefied wood chips S from remaining at the bottom of the reaction tower 11.

A temperature sensor 15 is provided inside the reaction tower 11 to detect the internal temperature of the reaction tower 11 (step s2). The temperature detection result detected by this temperature sensor 15 is transmitted to the rotation control section 73, and the rotation control section 73 controls the rotary valve 33, the upstream screw blade 43, the vertical screw The rotational speed of the blades 52 is controlled to adjust the amount of torrefied wood chips S to be conveyed (step s6).

Similarly, the storage amount detection sensor 16 also detects the amount of torrefied wood chips S accumulated inside the reaction tower 11 (step s3), and the detection result is transmitted to the rotation control section 73. Then, the rotation control unit 73 controls the rotational speed of the rotary valve 33, the upstream screw blade 43, and the vertical screw blade 52 based on the transmitted detection result information, and adjusts the conveyance amount of the torrefied wood chips S. (step s6).

Furthermore, the components of the generated gas G generated from the reaction tower 11 are analyzed by the gas analyzer 72 installed before the gas storage section 60 (step s4). This analysis result is also sent to the rotation control unit 73, and the rotation control unit 73 controls the rotational speed of the rotary valve 33, upstream screw blade 43, and vertical screw blade 52 based on the sent analysis result information. , the amount of torrefied wood chips S to be transported is adjusted (step s6).

For example, if the temperature sensor 15 detects that the internal temperature of the reaction tower 11 is lower than the appropriate temperature (step s2: No), the torrefied wood chips S being conveyed to the reaction tower 11 cannot be efficiently gasified. . In this case, the rotation control unit 73 that has received the temperature detection result controls the rotary valve motor 34 to increase the rotation speed of the rotary valve 33 and increase the amount of torrefied wood chips S conveyed to the supply pipe 32. be able to.

In addition, the rotation control unit 73 controls the rotation motor 44 and the rotation motor 53 to adjust the rotation speed of the upstream screw blade 43 and the vertical screw blade 52, thereby controlling the torrefied wood chips S in the intermediate conveying pipe 42. The torrefied wood chips S can be further compacted and subdivided. Specifically, by making the rotation speed of the upstream screw blade 43 faster than the rotation speed of the vertical screw blade 52 (step s6), a large amount of torrefied wood chips S transported from the surge tank 30 are transferred to the intermediate transport pipe. 42, it becomes more clogged and becomes more compacted. Since the torrefied wood chips S compacted in this way are conveyed to the reaction tower 11 by the vertical screw blades 52, the torrefied wood chips S can be further divided into smaller pieces.
Thereby, the torrefied wood chips S transported to the reaction tower 11 are efficiently gasified, and the internal temperature of the reaction tower 11 can be increased.

Similarly, when the amount of torrefied wood chips S inside the reaction tower 11 is decreasing, the storage amount detection sensor 16 detects an increase in torrefied wood chips S (step s3: No), and The information is transmitted to the rotation control section 73. Based on this information, the rotation control unit 73 controls the rotation motor 44 to increase the rotation speed of the upstream screw blade 43, and the rotation control unit 73 controls the rotation motor 53 to rotate the vertical screw blade 52. By increasing the speed (step s6), the amount of torrefied wood chips S transported to the reaction tower 11 can be increased, and gasification of the torrefied wood chips S can be promoted.

Conversely, when the amount of torrefied wood chips S accumulated inside the reaction tower 11 is increasing, the storage amount detection sensor 16 detects the increase in torrefied wood chips S (step s3: No). , transmits the information to the rotation control section 73. Based on this information, the rotation control unit 73 reduces the rotation speed of the vertical screw blades 52 (step s6) to further consolidate the torrefied wood chips S in the intermediate conveyance pipe 42. Thereby, the more finely divided torrefied wood chips S can be transported to the reaction tower 11 by the vertical screw blades 52 .
Therefore, since the torrefied wood chips S can be divided into smaller pieces while reducing the amount of torrefied wood chips S to be transported, the surface area of the torrefied wood chips S can be expanded, and the torrefied wood chips S can be gasified efficiently.

Similarly, if the components of the generated gas G detected by the gas analyzer 72 are not at the desired ratio (step s4: No), the rotation control section 73 controls the rotation of the rotary valve motor 34 based on this information. The motor 44 and rotary motor 53 are controlled to adjust their respective rotational speeds (step s6). As a result, the amount, size, and density of the torrefied wood chips S to be transported to the reaction tower 11 are adjusted, and the components of the generated gas G are adjusted to an appropriate ratio.

In this way, until a predetermined amount of produced gas G is obtained (step s5), the rotational speeds of the rotary valve 33, upstream screw blades 43, and vertical screw blades 52 are adjusted according to the internal situation of the reaction tower 11. The torrefied wood chips S are repeatedly gasified in a desired state. After a predetermined amount of generated gas G is obtained, the rotation of the rotary valve 33, upstream screw blade 43, and vertical screw blade 52 is stopped to complete gasification.

Note that by controlling the gasifying agent supply device 18 with the rotation control unit 73, the amount of gasifying agent H supplied from the first supply pipe 13a and the second supply pipe 13b is controlled, and the inside of the reaction tower 11 is controlled. Gasification can also be adjusted.

The gasification system 1 configured in this way is composed of a conveying device 20 into which torrefied wood chips S are introduced, and a reaction tower 11 which gasifies the torrefied wood chips S. A vertical conveyance path 50 is provided for conveying torrefied wood chips S from the bottom of the column 11 in the vertical direction (up and down direction), and the reaction column 11 is provided with a generated gas gasified from the torrefied wood chips S. A discharge pipe 12 for discharging G is provided above, and a vertical conveyance path 50 is formed in a tubular shape along the vertical direction. A vertical screw blade 52 is provided that is rotatable about a shaft that is a rotation axis, and the upper end portion (exposed portion 52a) of the vertical screw blade 52 is exposed above the bottom of the reaction tower 11.

As a result, the torrefied wood chips S can be transported from below to the high temperature layer in the reaction tower 11, and the torrefied wood chips S that have fallen without being gasified in the reduction zone T3 in the exposed portion 52a can be transported to the reaction tower 11. It can be transported again to the reduction zone T3 in the reaction tower 11 together with the torrefied wood chips S newly introduced into the reactor 11.

Thereby, the torrefied wood chips S that have not been sufficiently gasified can be gasified together with new torrefied wood chips S. That is, the torrefied wood chips S that have not been gasified inside the reaction tower 11 can be circulated and reused, and the torrefied wood chips S with high energy density can be efficiently gasified.

Further, since the torrefied wood chips S that have fallen to the bottom can be transported upward again by the exposed portion 52a, the torrefied wood chips S that have fallen from above and are piled up can be broken up. As a result, the stacked torrefied wood chips S collapse, and the bridge formed by the torrefied wood chips S can be eliminated. Therefore, the torrefied wood chips S can be stably gasified in the high temperature layer.

Further, the conveyance device 20 is provided with an input port 41a into which torrefied wood chips S are input at one end, and a tubular upstream side connected to the vertical conveyance path 50 in a cross direction. A conveyance path 40 is provided, and the upstream conveyance path 40 is formed in a spiral shape in the pipe, and includes an upstream screw blade 43 that conveys the torrefied wood chips S toward the vertical conveyance path 50 by rotation. It is being

Thereby, when the torrefied wood chips S are conveyed from the upstream conveyance path 40 to the longitudinal conveyance path 50, the torrefied wood chips S can be divided into small pieces. Thereby, the torrefied wood chips S of a desired size can be transported to the reaction tower 11, so that the torrefied wood chips S with high energy density can be efficiently gasified.

To explain in detail, the torrefied wood chips S carried out from the upstream conveyance path 40 by the upstream screw blade 43 are taken into the vertical conveyance path 50 by the vertical screw blade 52 and conveyed. By adjusting the conveyance amount of 43 and the conveyance amount of the vertical screw blade 52, the torrefied wood chips S are consolidated and finely divided between the vertical conveyance path 50 and the upstream conveyance path 40, and the torrefied wood chips S are divided into desired sizes. can do. By fragmenting the torrefied wood chips S in this way, it is possible to reliably prevent the torrefied wood chips S conveyed to the reaction tower 11 from forming bridges, and to S has an expanded surface area and can be efficiently gasified.

In addition, by individually adjusting the rotational speed of the upstream screw blade 43 and the vertical screw blade 52, the subdivision size of the new torrefied wood chips S to be conveyed can be adjusted, and the conveyance amount of the new torrefied wood chips S can be adjusted. It is possible to reuse the torrefied wood chips S accumulated at the bottom of the reaction tower 11 by limiting the amount of torrefied wood chips S, or to increase the amount of new torrefied wood chips S transported. That is, it is possible to more efficiently gasify the torrefied wood chips S according to the conditions of the reaction tower 11.

Furthermore, since the reaction tower 11 is provided with the gasifying agent supply pipe 13 for injecting the gasifying agent H, the gasifying agent H promotes the gasification of the torrefied wood chips S, resulting in high energy density. The torrefied wood chips S can be gasified more efficiently.

Furthermore, since a rotation control section 73 is provided that controls the rotation speed of the vertical screw blade 52 and adjusts the amount of torrefied wood chips S to be transported to the reaction tower 11, the internal situation of the reaction tower 11 can be controlled. The amount of torrefied wood chips S to be conveyed can be adjusted accordingly, and the torrefied wood chips S can be gasified more efficiently.

For example, if there are too many torrefied wood chips S transported into the reaction tower 11, the amount of torrefied wood chips S transported into the reaction tower 11 is reduced, and the half-carbonized wood chips S accumulated inside the reaction tower 11 are reduced. The carbonized wood chips S can be adjusted to be thermally decomposed and gasified. On the other hand, if there are too few torrefied wood chips S inside the reaction tower 11, the amount of torrefied wood chips S conveyed into the inside of the reaction tower 11 is increased to increase the material for gasification. gasification can be promoted.

Further, the reaction tower 11 is equipped with a storage amount detection sensor 16 that detects the amount of torrefied wood chips S accumulated inside the reaction tower 11, and the rotation control unit 73 is configured to detect the amount of torrefied wood chips S detected by the storage amount detection sensor 16. By controlling the rotational speed of the vertical screw blade 52 based on the amount of torrefied wood chips S, the amount of torrefied wood chips S to be conveyed can be adjusted based on the detection result of the storage amount detection sensor 16.

That is, depending on the amount of torrefied wood chips S accumulated inside the reaction tower 11, the torrefied wood chips S are transported to the reaction tower 11, and an appropriate amount of torrefied wood chips S is accumulated inside the reaction tower 11. can be done. Therefore, the torrefied wood chips S can be gasified more efficiently.

Further, the reaction tower 11 is equipped with a temperature sensor 15 that detects the internal temperature, and the rotation control unit 73 controls the rotation speed of the vertical screw blade 52 based on the temperature detected by the temperature sensor 15. Accordingly, the amount of torrefied wood chips S to be conveyed can be adjusted based on the detection result of the temperature sensor 15.

That is, depending on the temperature inside the reaction tower 11, the torrefied wood chips S can be transported to the reaction tower 11, and an appropriate amount of torrefied wood chips S can be accumulated inside the reaction tower 11. Therefore, the torrefied wood chips S can be gasified more efficiently.

For example, if it is detected that the internal temperature of the reaction tower 11 has increased compared to the desired temperature, the rotation speed of the vertical screw blade 52 is increased to increase the number of torrefied wood chips S inside the reaction tower 11. can be transported to lower the internal temperature of the reaction tower 11. On the other hand, if it is detected that the internal temperature of the reaction tower 11 is lower than the desired temperature, the rotation speed of the vertical screw blade 52 is lowered, and the torrefied wood chips transported into the reaction tower 11 are lowered. By reducing the amount of S, the reaction efficiency of the torrefied wood chips S accumulated inside can be increased, and the torrefied wood chips S can be gasified more efficiently.

Furthermore, a gas analyzer 72 for analyzing gas components is provided, and the rotation control unit 73 controls the rotation speed of the vertical screw blade 52 based on the gas components. Based on the detection result, the amount of torrefied wood chips S to be transported can be adjusted, and the torrefied wood chips S can be gasified more efficiently.

Specifically, the components of the gas released from the reaction tower 11 vary depending on the internal temperature of the reaction tower 11, the ratio of the gasifying agent H, and the like. From this, it is possible to adjust the internal temperature of the reaction tower 11 and the ratio of the gasifying agent H by adjusting the amount of torrefied wood chips S to be transported based on the components of the gas to be released. supply. As a result, the amount of torrefied wood chips S to be transported can be adjusted depending on the gasification state inside the reaction tower 11, and an appropriate amount of torrefied wood chips S can be accumulated inside the reaction tower 11 to more efficiently halve the chips. Carbonized wood chips S can be gasified.

In addition, the discharge pipe 12 is configured to have a negative pressure on the tip side, so that the gas that has been gasified inside the reaction tower 11 can be sucked into the discharge pipe 12. can be reliably released from the release pipe 12.

Furthermore, since the gasifying agent H supplied from the gasifying agent supply pipe 13 can be drawn into the reaction tower 11 to generate an upward air current, the torrefied wood chips S conveyed by the vertical screw blades 52 can be reduced. It becomes easier to lift it upwards where band T3 is formed. Furthermore, torrefied wood chips S that have not been completely gasified can be drawn into the discharge pipe 12.

Furthermore, the discharge tube 12 is provided with the distal discharge tube 12c, which has a smaller diameter at the distal end than the proximal end, so that the distal end of the discharge tube 12 has a smaller diameter. As a result, the flow velocity of the produced gas G, torrefied wood chips S, etc. flowing through the reduced diameter portion 12b and the distal end discharge pipe 12c becomes faster, and the temperature at the location where the flow velocity becomes faster rises, preventing complete gasification. The combustion residue of the torrefied wood chips S can be gasified in the discharge pipe 12.

In addition, an ash discharge section 17 is provided at the bottom of the reaction tower 11 to discharge the torrefied wood chips S accumulated at the bottom. It is possible to discharge torrefied wood chips S and the like accumulated in a position where they cannot be transported upwards from the bottom.

In the correspondence between the configuration of this invention and the above-described embodiments,
The wood chips correspond to torrefied wood chips S, and similarly,
The loading mechanism corresponds to the transport device 20,
The reaction tower corresponds to the reaction tower 11,
The gasifier corresponds to gasification system 1,
The vertical conveyance path corresponds to the vertical conveyance path 50,
The discharge pipe corresponds to the discharge pipe 12,
The vertical screw blade corresponds to the vertical screw blade 52,
The input port corresponds to the input port 41a,
The upstream conveyance path corresponds to the upstream conveyance pipe 41,
The upstream screw blade corresponds to the upstream screw blade 43,
The injection part corresponds to the gasifying agent supply pipe 13,
The conveyance amount control section corresponds to the rotation control section 73,
The storage amount detection section corresponds to the storage amount detection sensor 16,
The temperature detection section corresponds to the temperature sensor 15,
The analysis section corresponds to the gas analyzer 72,
The narrow diameter portion corresponds to the distal end discharge tube 12c,
The ash discharge section corresponds to the ash discharge section 17, but
This invention is not limited only to the configuration of the above-described embodiments, but can be implemented in many other embodiments.

For example, in the present embodiment, the vertical conveyance path 50 is vertically disposed vertically (in the vertical direction) with respect to the reaction tower 11, but it is not necessary to completely coincide with the vertical direction. For example, the vertical conveyance path 50 may be inclined at approximately ±30 degrees with respect to the vertical direction.

Further, in this embodiment, the intermediate conveyance pipe 42 and the vertical conveyance pipe 51 are orthogonal at the connecting portion, but they do not necessarily need to be orthogonal, and the intermediate conveyor pipe 42 and the vertical conveyor pipe 51 are That's fine. Further, the upstream conveyance pipe 41 may be arranged in a direction intersecting the vertical direction, for example, along the horizontal direction, and furthermore, the upstream conveyance pipe 41 and the vertical conveyance pipe 51 may be directly connected.

Further, as long as the vertical screw blades 52 can transport the torrefied wood chips S accumulated below the reaction tower 11 upward, the vertical transport path 50 may have any configuration. For example, in the vertical conveyance path 50, a partial opening is formed in a vertical conveyance pipe 51 extending upward inside the reaction tower 11, and the vertical screw blade 52 is partially exposed from this opening. Good too.

Further, as the gasifying agent, air and water vapor are used in this embodiment, but the gasifying agent is not particularly limited as long as it promotes gasification of the semi-carbonized wood chips S. Therefore, for example, in addition to gas such as oxygen, other gases, powders, liquids, etc. may be used.

Furthermore, the rotation control unit 73 controls the rotation control unit 73 based on, for example, the accumulated amount and density of the torrefied wood chips S introduced into the reaction tower 11, the temperature inside the reaction tower 11, the components of the gas released, or the like. The amount of torrefied wood chips S to be conveyed may be controlled by a combination of these.

Furthermore, the upstream screw blade 43 is configured to extend along the upstream conveying pipe 41 and the intermediate conveying pipe 42 from the upper end of the upstream conveying pipe 41 to the tip of the intermediate conveying pipe 42. However, the configuration is not limited to this, and for example, a so-called screw feeder that is rotatable about an axis along the vertical direction is installed inside the upstream conveyance pipe 41, and a so-called screw feeder is installed inside the curved intermediate conveyance pipe 42. , a so-called spring conveyor blade such as the upstream screw blade 43 that can transmit the rotation of a screw feeder provided inside the upstream conveying pipe 41 may be used.

1 Gasification system 11 Reaction tower 12 Discharge pipe 12c Tip side discharge pipe 13 Gasifying agent supply pipe 15 Temperature sensor 16 Storage amount detection sensor 17 Ash discharge section 20 Conveyance device 40 Upstream conveyance path 41a Input port 43 Upstream screw blade 50 Vertical conveyance path 52 Vertical screw blade 72 Gas analyzer 73 Rotation control section S Semi-carbonized wood chips

The present invention relates to a gasifier for gasifying wood chips.

In recent years, environmental issues have become a hot topic, and instead of power generation using fossil fuels such as oil and coal, for example, combustion materials generated from biomass fuels such as naturally derived wood chips and torrefied wood chips are being used. Research is progressing on power generation equipment, etc.

As an example of a gasification device that generates such combustion substances from biomass fuel, a gasification agent such as air or steam is supplied from a gasification agent supply port provided at the bottom of the reaction tower, while a gasification agent is supplied to the top of the reaction tower. Patent Document 1 discloses a gasification apparatus that inputs biomass fuel from a provided input port, heats it, and gasifies the biomass fuel.

This gasifier is a so-called updraft type gasifier, in which a discharge port is installed at the upper side of the reaction tower to release generated gas generated from biomass fuel, and the gasifier at the bottom is not gasified. It is equipped with an ash discharge section to remove biomass ash.

According to the gasifier disclosed in Patent Document 1, the biomass fuel introduced from the top is gasified inside the reaction tower, and the biomass fuel (combustion residue) that has fallen without being completely gasified is stabilized. It is said that it can be eliminated by

However, the size of the biomass input into the reaction tower varies, and combustion residue that has not been sufficiently gasified and falls is removed. For this reason, there has been a problem that these combustion residues cannot be effectively utilized, and the efficiency of gasifying biomass is reduced.

Japanese Patent Application Publication No. 2008-101215

SUMMARY OF THE INVENTION In view of the above-mentioned problems, an object of the present invention is to provide a gasifier that can efficiently gasify torrefied wood chips.

The present invention provides a gasification apparatus for gasifying wood chips, which comprises an input mechanism for inputting torrefied wood chips, and a reaction tower for gasifying the wood chips, wherein the input mechanism is provided with a tubular longitudinal conveying path along the vertical direction for conveying the wood chips from the bottom of the reaction column into the interior thereof, and the reaction column has an outlet for discharging gasified gas from the wood chips. A pipe is provided above, and an injection part for injecting the gasifying agent into the reaction tower is provided, and the vertical conveyance path is formed in a spiral shape along the vertical direction in the pipe , and A vertical screw blade is provided that is rotatable about an axis along the vertical direction, the vertical screw blade is exposed above the bottom of the reaction tower , and the injection part is configured to be connected to the bottom of the reaction tower. The reactor is characterized in that it includes a first injection section provided at the bottom and a second injection section provided on the side of the central portion of the reaction column .

The above-mentioned torrefaction treatment is a process to generate carbide by heating at a predetermined temperature (approximately 200 to 350 degrees) while limiting or cutting off the amount of oxygen supplied to turn wood chips into a material with a high carbon content. As expected. Thereby, solid fuel with high energy density can be obtained.
The longitudinal conveyance path does not necessarily have to completely coincide with the vertical direction, and may be any direction that intersects the vertical direction at an angle of less than 45 degrees, for example.

According to this invention, torrefied wood chips can be efficiently gasified.
To be more specific, the wood chips that have been torrefied can be transported from below to the top of the high temperature layer in the reaction tower, and the wood chips that have fallen without being gasified in the high temperature layer can be transported at the upper end of the vertical screw blade. It can be transported again to the high temperature layer in the reaction tower together with the wood chips newly introduced into the reaction tower.

Thereby, wood chips that have not been sufficiently gasified can be gasified together with new wood chips. That is, wood chips that have not been gasified inside the reaction tower can be circulated and reused, and wood chips with high energy density can be efficiently gasified.

In addition, since the wood chips that have fallen to the bottom can be transported upward again by the vertical screw blades, the wood chips that have fallen from above and are piled up can be broken down. This allows the stacked wood chips to collapse and eliminates the bridges formed by the wood chips. Therefore, wood chips can be stably gasified in the high temperature layer.

In addition, since the reaction tower is provided with an injection part for injecting a gasification agent, the gasification of the wood chips is promoted by the gasification agent , and wood chips that have been torrefied are more efficiently produced. It can be gasified.

Here, the gasification agent is a promoter that promotes gasification of wood chips, and includes, for example, air, oxygen, water vapor, and the like. Note that the gasifying agent is not limited to the above-mentioned gases, and may be gases other than the above-mentioned gases, powders, liquids, etc. as long as they can promote gasification of the wood chips.

As an aspect of the present invention, the first injection part is provided at a central portion of the rotating shaft of the vertical screw blade installed in the vertical conveyance path, and is arranged upwardly along the longitudinal direction of the vertical conveyance path. The gasifying agent may be supplied.

Further, as an aspect of the present invention, when gasifying the wood chips, the reaction tower includes a pyrolysis zone for thermally decomposing the wood chips, a combustion zone for burning the pyrolyzed wood chips, Three layers of the reduction zone in which the gas is generated are formed in this order from the bottom to the top, and the second injection part is disposed at a position corresponding to the reduction zone on a side surface of the central portion of the reaction tower. Good too.

Further, as an aspect of the present invention, the discharge tube is configured such that the distal end side is under negative pressure, and the negative pressure is applied to the distal end side of the discharge tube, so that the reaction from the first injection part and the second injection part is The gasifying agent may be injected into the interior of the column.
According to the present invention, the gas that has been gasified inside the reaction tower can be sucked into the discharge pipe, so that the gasified gas can be reliably discharged from the discharge pipe.

Further, as an aspect of the present invention, the discharge tube may be provided with a small diameter portion having a smaller diameter at the tip than the proximal end side, and the tip may be provided with an aspirator for sucking the generated gas. good.
According to this invention, since the distal end side of the discharge tube has a small diameter, the flow rate of generated gas, wood chips, etc. flowing through the narrow diameter portion is faster than at the proximal end side of the discharge tube. As a result, the temperature at the location where the flow rate is increased increases, so that wood chip residues that have not been completely gasified can be gasified within the discharge pipe.

Further, as an aspect of the present invention, the vertical conveyance path may include a tubular vertical conveyance pipe that is vertically arranged and connected to an insertion hole provided at the bottom of the reaction tower; and the vertical screw blade installed in the conveying pipe, and the vertical screw blade is configured to circulate the wood chips that have fallen to the bottom of the reaction tower without being gasified. It may protrude upward from the bottom of the reaction column and may be exposed above the bottom of the reaction column.

As an aspect of the present invention, the input mechanism is provided with an input port into which the wood chips are input on one end side, and a tubular upstream side connected in a cross direction intersecting with the longitudinal conveyance path on the other end side. A side conveyance path may be provided, and the upstream conveyance path may be formed in a spiral shape within the pipe, and may include an upstream screw blade that conveys the wood chips toward the longitudinal conveyance path by rotation. good.

According to this invention, the wood chips can be divided into small pieces when the wood chips are transported from the upstream transport path to the vertical transport path. Thereby, the wood chips finely divided into desired sizes can be transported to the reaction tower, so that the wood chips can be efficiently gasified.

To explain in detail, the wood chips carried out from the upstream conveyance path by the upstream screw blades are taken into the vertical conveyance path by the vertical screw blades and conveyed, but the conveyance amount of the upstream screw blades and the vertical screw blade are By adjusting the amount of conveyance of the blades, the wood chips can be compacted and fragmented between the vertical conveyance path and the upstream conveyance path, and can be made into a desired size. In this way, by fragmenting the wood chips into desired sizes, it is possible to prevent the wood chips transported to the reaction tower from forming bridges, and the surface area of the fragmented wood chips is expanded. It can be gasified efficiently.

In addition, by individually adjusting the rotational speed of the upstream screw blade and the vertical screw blade, the subdivision size of the new wood chips to be conveyed can be adjusted, and the amount of new wood chips to be conveyed can be restricted to the bottom of the reaction tower. It is possible to reuse the wood chips accumulated in the factory or increase the amount of new wood chips transported. That is, wood chips can be gasified more efficiently depending on the conditions of the reaction tower.

Further, as an aspect of the present invention, a conveyance amount control section may be provided that controls the rotational speed of the vertical screw blade and adjusts the conveyance amount of the wood chips to be conveyed to the reaction tower.

The conveyance amount control unit performs the torrefaction treatment based on, for example, the accumulated amount and density of the wood chips introduced into the reaction tower, the temperature inside the reaction tower, the components of the gas released, or a combination thereof. The amount of transported wood chips may be controlled.

According to the present invention, the amount of torrefied wood chips to be transported can be adjusted according to the internal condition of the reaction tower, and wood chips with high energy density can be gasified more efficiently.
For example, if there are too many torrefied wood chips transported into the reaction tower, the amount of wood chips transported into the reaction tower is reduced, and the wood chips accumulated inside are heated up. It can be adjusted to decompose and gasify. On the other hand, if there are too few torrefied wood chips inside the reaction tower, the amount of torrefied wood chips conveyed to the inside of the reaction tower is increased, and the material for gasification is increased. can be increased and gasification can be promoted.

Further, as an aspect of the present invention, the reaction tower is provided with an accumulation amount detection unit that detects the amount of the wood chips accumulated inside the reaction tower, and the conveyance amount control unit is configured to include an accumulation amount detection unit that detects the amount of the wood chips accumulated inside the reaction tower. The rotation speed of the longitudinal screw blades may be controlled based on the detected amount of the wood chips.

According to the present invention, the amount of torrefied wood chips to be transported can be adjusted based on the detection result of the accumulation amount detection section. That is, depending on the amount of wood chips accumulated inside the reaction tower, the wood chips can be transported to the reaction tower and an appropriate amount of wood chips can be accumulated inside the reaction tower. Thereby, wood chips can be gasified more efficiently.

Further, as an aspect of the present invention, the reaction tower is provided with a temperature detection unit that detects an internal temperature, and the conveyance amount control unit controls the vertical screw blades based on the temperature detected by the temperature detection unit. The rotation speed may be controlled.

According to this invention, the amount of torrefied wood chips to be transported can be adjusted based on the detection result of the temperature detection section. That is, depending on the temperature inside the reaction tower, wood chips can be transported to the reaction tower and an appropriate amount of wood chips can be accumulated inside the reaction tower. Thereby, wood chips can be gasified more efficiently.

For example, if it is detected that the internal temperature of the reaction tower has increased compared to the desired temperature, the rotation speed of the vertical screw blades can be increased to transport more wood chips into the interior of the reaction tower. . On the other hand, if it is detected that the internal temperature of the reaction tower is lower than the desired temperature, the rotation speed of the vertical screw blades is lowered to reduce the amount of wood chips conveyed into the inside of the reaction tower. , the wood chips accumulated inside can be gasified. Therefore, wood chips can be gasified more efficiently.

Further, as an aspect of the present invention, an analysis section for analyzing the components of the gas may be provided, and the conveyance amount control section may control the rotational speed of the vertical screw blade based on the components of the gas.
According to the present invention, the amount of torrefied wood chips to be transported can be adjusted based on the detection results of the analysis section, and the wood chips can be gasified more efficiently.

Specifically, the components of the gas released from the reaction tower vary depending on the internal temperature of the reaction tower, the ratio of the gasifying agent, and the like. Therefore, by adjusting the amount of torrefied wood chips transported based on the components of the gas released, the internal temperature of the reaction tower and the ratio of gasification agent can be adjusted, resulting in a stable gas flow. supply. As a result, the amount of wood chips transported can be adjusted depending on the gasification state inside the reaction tower, allowing an appropriate amount of wood chips to be accumulated inside the reaction tower, and making it possible to gasify wood chips more efficiently. .

Further, as an aspect of the present invention, an ash discharge section may be provided at the bottom of the reaction tower to discharge the wood chips accumulated at the bottom.
According to the present invention, wood chips and the like that have accumulated at the bottom of the reaction tower and are not transported upward again by the vertical screw blades can be discharged from the bottom.

According to the present invention, it is possible to provide a gasification device that can efficiently gasify wood chips that have been subjected to torrefaction treatment.

Schematic diagram of the gasification system. Schematic diagram of a conveying device and a gasification reactor. Gasification flowchart. Schematic diagram of wood chip fragmentation. Schematic diagram of the movement of wood chips inside the reaction tower.

One embodiment of this invention will be described below with reference to the drawings.
FIG. 1 shows a schematic diagram of the gasification system 1, FIG. 2 shows a schematic diagram of the gasification reactor 10 and the conveying device 20, FIG. 3 shows a flowchart of gasification by the gasification system 1, and FIG. 4 shows a surge A schematic diagram showing the transportation of the torrefied wood chips S stored in the tank 30 is shown, and FIG. 5 is a conceptual diagram showing the movement of the torrefied wood chips S inside the reaction tower 11.

The gasification system 1 gasifies wood chips that have been torrefied (hereinafter referred to as "semi-carbonized wood chips S") by thermally decomposing, burning, and reducing them, and collects the generated gas G from above. This is a draft gasification system.

Specifically, the gasification system 1 transports the torrefied wood chips S upward from the bottom of the reaction tower 11, which is a substantially cylindrical vertical container, and then converts the torrefied wood chips S into the torrefied wood chips in the reaction tower 11 whose internal temperature has been raised. Gasify S. The product gas G (carbon monoxide and hydrogen) generated by gasification in this manner is discharged from the discharge pipe 12 provided above the reaction tower 11 and stored in the gas storage section 60.

The structure of the gasification system 1 and the gasification of torrefied wood chips S using the gasification system 1 will be described below.
As shown in FIG. 1, the gasification system 1 includes a gasification reaction device 10 that gasifies torrefied wood chips S, and a transport device that transports the torrefied wood chips S, which are raw materials for gasification, to the gasification reaction device 10. It is composed of a device 20 and a gas storage section 60 that stores the generated gas G generated in the gasification reaction device 10.

The gasification reactor 10 includes a reaction tower 11 that gasifies semi-carbonized wood chips S, a discharge pipe 12 that releases the generated gas G generated in the reaction tower 11, and a gasification agent H that is supplied to the reaction tower 11 from the bottom. It is composed of a gasifying agent supply pipe 13. Further, inside the reaction tower 11, a heater 14 for increasing the internal temperature of the reaction tower 11, a temperature sensor 15 for detecting the internal temperature of the reaction tower 11, and torrefied wood chips stored inside the reaction tower 11 are installed. A storage amount detection sensor 16 that detects the storage amount of S is provided.

The reaction tower 11 is a substantially cylindrical vertical container, and the bottom portion has a conical shape that tapers downward. An insertion hole is provided at the apex of this cone for connection to a vertical conveyance pipe 51 , which will be described later. Furthermore, an ash discharge section 17 is provided at the bottom of the reaction tower 11 for scraping out the residue left after the semi-carbonized wood chips S have not been completely gasified.

In addition, when gasifying the torrefied wood chips S, inside the reaction tower 11, as shown in FIG. Three layers are formed in this order from the bottom to the top: a combustion zone T2 where carbonized wood chips S are burned, and a reduction zone T3 where generated gas G (carbon monoxide and hydrogen) is generated.

The discharge pipe 12 is a pipe for discharging the generated gas G generated inside the reaction tower 11 to the outside, and is provided at the upper part of the reaction tower 11 . As shown in FIG. 2, the discharge pipe 12 includes a proximal discharge pipe 12a connected to the side wall of the reaction column 11, a reduced diameter part 12b whose inner diameter decreases toward the distal end, and a reduced diameter part 12b. and a distal end discharge pipe 12c connected to the distal end discharge pipe 12c. Note that the distal end discharge tube 12c has a smaller diameter than the proximal discharge tube 12a.

A gas storage section 60 for storing the produced gas G and a suction device 71 for sucking the produced gas G are provided at the distal end of the distal end side discharge pipe 12c. Further, a part of the tip-side discharge pipe 12c is branched, and a gas analyzer 72 for analyzing the components of the generated gas G is attached.

This suction device 71 creates a negative pressure in the discharge pipe 12, and the generated gas G can be guided to the gas storage section 60.

A gas analyzer 72 provided in front of the gas storage section 60 collects the results of component analysis of the product gas G produced in the reaction tower 11 and transmits the analysis results to the rotation control section 73.
The rotation control unit 73 controls the rotation speeds of a rotary valve 33, an upstream screw blade 43, and a vertical screw blade 52, which will be described later, to control the amount of torrefied wood chips S to be transported to the reaction tower 11. There is.

The gasifying agent supply pipe 13 supplies the gasifying agent H (air and steam) supplied from the gasifying agent supply device 18 connected to the base end into the reaction tower 11 . This gasifying agent supply pipe 13 is composed of a first supply pipe 13a connected to the bottom of the reaction tower 11, and a second supply pipe 13b connected to the side of the central portion of the reaction tower 11.

The first supply pipe 13a is provided at the center of the rotating shaft of a vertical screw blade 52 installed in a vertical conveyance pipe 51, which will be described later, and gasifies upward along the longitudinal direction of the vertical conveyance pipe 51. Agent H can be supplied.

Note that the first supply pipe 13a only needs to be able to supply the gasifying agent H upward from the bottom of the reaction tower 11, and its position and number are not limited. For example, it may be arranged along the outer circumferential surface of the vertical conveyance pipe 51, or it may be arranged at another location at the bottom of the reaction tower 11.

The second supply pipe 13b is connected to the side surface of the central portion of the reaction tower 11, and can supply the gasifying agent H into the inside of the reaction tower 11 from the side. More specifically, it is arranged at a position corresponding to the reduction zone T3 of the reaction tower 11.

The heater 14 is a heating device for bringing the inside of the reaction tower 11 into a high temperature state in the initial state of gasifying the semi-carbonized wood chips S. Further, based on the temperature detection result by the temperature sensor 15, it may be used to raise the internal temperature of the reaction tower 11 when producing the product gas G.

Temperature sensor 15 detects the internal temperature of reaction tower 11 . Note that the detection result detected by the temperature sensor 15 is transmitted to the rotation control section 73.

The storage amount detection sensor 16 detects the amount of torrefied wood chips S accumulated inside the reaction tower 11. Specifically, inside the reaction tower 11, it is detected whether the accumulated torrefied wood chips S are lower or higher than a desired height. The temperature detection result detected by this storage amount detection sensor 16 is transmitted to the rotation control section 73. The rotation control unit 73 controls the rotation speeds of the rotary valve 33, the upstream screw blade 43, and the vertical screw blade 52, respectively, based on the transmitted result information.

The conveyance device 20 includes a surge tank 30 that stores torrefied wood chips S to be conveyed to the gasification reaction apparatus 10, and an upstream conveyance path 40 that conveys the torrefied wood chips S from the surge tank 30 to the gasification reaction apparatus 10. , and a vertical conveyance path 50 for conveying torrefied wood chips S to the reaction tower 11, and is equipped with an external screw feeder F having a rotation motor attached to its upper end.

The surge tank 30 is installed between a surge tank main body 31 for storing torrefied wood chips S, a supply pipe 32 connected to the lower end of the surge tank main body 31, and between the surge tank main body 31 and the supply pipe 32. It is composed of a rotary valve 33.

The supply pipe 32 is a tubular conveyance path, and one end thereof is connected to a fuel inlet 31a provided at the lower end of the tapered surge tank main body 31 via a rotary valve 33, and the other end is connected to the upstream conveyance path 40. are doing.
The rotary valve 33 is configured to be freely rotatable by a rotary valve motor 34 and can feed torrefied wood chips S stored in the surge tank main body 31 into the supply pipe 32. Note that the rotary valve motor 34 is controlled by the rotation control section 73 as described above. Furthermore, by providing the external screw feeder F, it is possible to prevent the bridging phenomenon of the torrefied wood chips S within the surge tank main body 31, and it is possible to more reliably supply the torrefied wood chips S to the supply pipe 32. .

The torrefied wood chips S stored in the surge tank main body 31 are carbon-rich wood chips obtained by thermally decomposing wood biomass such as wood chips at high temperatures of 200 to 350 degrees under anoxic conditions. It is a carbide. This torrefied wood chip S has a high energy density per weight and has good crushing performance.

As shown in FIGS. 1 and 2, the upstream conveyance path 40 includes an upstream conveyance pipe 41 configured in a tubular shape, and an intermediate conveyance pipe 42 curved from the lower end of the upstream conveyance pipe 41 toward the gasification reaction apparatus 10 side. , an upstream screw blade 43 installed inside the upstream conveyance pipe 41 , and a rotation motor 44 that rotationally drives the upstream screw blade 43 .

The upstream conveyance pipe 41 is a tubular body that stands upright along the vertical direction, and is provided with an input port on the side to which the tip of the supply pipe 32 is connected. Further, a rotary motor 44 for rotationally driving the upstream screw blade 43 is provided at the upper end of the upstream conveying pipe 41 .

The intermediate conveyance pipe 42 is a tubular body whose orthogonal cross section perpendicular to the central axis has the same shape as the orthogonal cross section of the upstream conveyance pipe 41, and as shown in FIG. ing. Further, the base end of the intermediate conveyance pipe 42 is connected to the upstream conveyance pipe 41, and the distal end thereof is connected to a vertical conveyance pipe 51 forming a vertical conveyance path 50.

The upstream screw blade 43 is a blade used in a so-called spring conveyor, which is formed in a spiral shape and can rotate while bending. It extends from to the tip of the intermediate conveying pipe 42.

The upper end of the upstream screw blade 43 is connected to the rotary motor 44 and can freely rotate inside the upstream conveyance pipe 41 and the intermediate conveyance pipe 42 . Thereby, the torrefied wood chips S input from the input port can be conveyed to the tip of the intermediate conveyance pipe 42.
Note that the rotation motor 44 is connected to a rotation control section 73, and the rotation speed of the upstream screw blade 43 is controlled by the rotation control section 73.

The vertical conveyance path 50 is composed of a tubular vertical conveyance pipe 51, a vertical screw blade 52 installed inside the vertical conveyance pipe 51, and a rotation motor 53 that rotationally drives the vertical screw blade 52. .
The vertical conveyance pipe 51 is a tubular body that stands upright along the vertical direction, and is arranged below the reaction tower 11 . The longitudinal conveyance pipe 51 is provided with a connecting portion on the side of the central portion thereof, which is connected perpendicularly to the intermediate conveyance pipe 42 connected from the lower end of the upstream conveyance pipe 41 .

The vertical screw blade 52 installed in the vertical conveyance pipe 51 is a so-called screw feeder, which is formed in a spiral shape along the vertical direction and is rotatable about an axis along the vertical direction as a rotation axis. The lower end of this vertical screw blade 52 is connected to a rotation motor 53 provided at the lower end of the vertical conveyance pipe 51, and can freely rotate inside the vertical conveyance pipe 51.

Further, the vertical screw blade 52 is configured to be longer than the vertical conveying pipe 51. For this reason, an exposed portion 52 a that protrudes from the upper end of the vertical conveyance pipe 51 is formed in the upper portion of the vertical screw blade 52 .
Note that the rotation motor 53 is connected to a rotation control section 73, and the rotation speed of the vertical screw blade 52 is controlled by the rotation control section 73.

The vertical conveyance path 50 configured in this manner is disposed below the reaction tower 11, and the upper end of the vertical conveyance pipe 51 is connected to the insertion hole . Therefore, the exposed portion 52a, which is the upper end portion of the vertical screw blade 52, protrudes above the insertion hole , that is, the bottom of the reaction tower 11.

Next, a method of transporting the torrefied wood chips S to the reaction tower 11 using the transport device 20 and gasification in the reaction tower 11 will be briefly explained based on FIG. 3.
As a step before operating the gasification system 1, torrefied wood chips S serving as a raw material are stored in the surge tank main body 31 (step s0). Since the torrefied wood chips S stored in the surge tank main body 31 have been torrefied, their mass is reduced to about 45 to 68% compared to the mass of the wood chips before being torrefied. ing.

First, in order to transport the torrefied wood chips S to the reaction tower 11, the rotary valve 33, intermediate transport pipe 42, and vertical screw blade 52 are rotated (step s1). As a result, the torrefied wood chips S stored in the surge tank main body 31 are conveyed to the supply pipe 32 while being crushed by the rotary valve 33, and are thrown into the upstream conveyance pipe 41 as they are. Furthermore, the torrefied wood chips S introduced into the upstream conveyance pipe 41 are conveyed downward along the upstream conveyance pipe 41 and the intermediate conveyance pipe 42 by the rotation of the upstream screw blades 43 .

Here, by setting the rotation speed of the vertical screw blade 52 to be slower than the rotation speed of the upstream screw blade 43, the torrefied wood chips S are consolidated in the intermediate conveyance pipe 42. When the torrefied wood chips S consolidated in the intermediate conveyance pipe 42 are fed into the vertical conveyance pipe 51, they are transported in the vertical direction while being finely divided by the vertical screw blades 52 rotating inside the vertical conveyance pipe 51. It will be put into the tube 51.
The semi-carbonized wood chips S thus introduced into the vertical transport pipe 51 are transported into the reaction tower 11 along the vertical transport pipe 51 by the rotation of the vertical screw blades 52 .

The torrefied wood chips S introduced into the reaction tower 11 in this way are subdivided into pieces that are about one-half to one-third the size of the torrefied wood chips S stored in the surge tank main body 31. has been made into Therefore, the torrefied wood chips S are accumulated inside the reaction tower 11 without forming bridges (see FIG. 4).

As shown in FIG. 5, the torrefied wood chips S transported to the reaction tower 11 in this manner rise up in the center by overcoming gravity due to the transport of the torrefied wood chips S by the vertical screw blades 52. On the other hand, since the radially outer portion of the reaction tower 11 is pressed downward by the bulge in the center, the torrefied wood chips S that have moved downward are consolidated by the torrefied wood chips S piled up above. and crushed.

Further, since the bottom of the reaction tower 11 is configured in a conical shape, the semi-carbonized wood chips S pressed downward gather in the center along the conical shape. The torrefied wood chips S gathered in the center in this way are wound around the vertical screw blades 52 and lifted upward again. Therefore, torrefied wood chips S (combustion residues of torrefied wood chips S) that have not been completely gasified can be prevented from accumulating at the bottom of the reaction tower 11.

Further, the reaction tower 11 in which the torrefied wood chips S are accumulated is heated to a temperature suitable for gasifying the torrefied wood chips S by the heater 14 when the gasification system 1 starts to be activated. Then, when gasification (thermal decomposition, combustion, reduction) of the torrefied wood chips S is started, the heater 14 is stopped. Thereafter, the internal temperature of the reaction tower 11 is basically controlled by the gasification combustion of the torrefied wood chips S.

When gasification of the semi-carbonized wood chips S starts, a generated gas G (carbon monoxide/hydrogen) is generated inside the reaction tower 11, and this generated gas G is disposed at the top and discharged with negative pressure on the tip side. drawn into tube 12. Thereby, the generated gas G can be stored in the gas storage section 60.

In addition, since the distal end side of the discharge pipe 12 is under negative pressure, the inside of the reaction column 11 is Gasifying agent H is supplied. In this way, the gasifying agent H supplied to the reaction tower 11 becomes an upward airflow through the discharge pipe 12, so that the gasification of the torrefied wood chips S inside the reaction tower 11 can be promoted, and the It is possible to raise torrefied wood chips S.

Thereby, in accordance with the promotion of gasification of the finely divided torrefied wood chips S, it is possible to further prevent torrefied wood chips S that have not been completely gasified from accumulating at the bottom of the reaction tower 11. Furthermore, it is possible to help draw the combustion residue of the torrefied wood chips S, which has not been completely gasified, into the discharge pipe 12.

Here, in the discharge tube 12, since the proximal discharge tube 12a and the distal discharge tube 12c are connected by the diameter-reduced portion 12b, the flow velocity of the torrefied wood chips S flowing inside the discharge tube 12 is lower than the diameter-reduced portion. 12b and the distal discharge tube 12c. As a result, the temperature of the combustion residue of the torrefied wood chips S that has not been completely gasified increases, so that the combustion residue of the torrefied wood chips S can be completely gasified.
Thereby, it is possible to prevent combustion residues of the torrefied wood chips S from remaining at the bottom of the reaction tower 11.

A temperature sensor 15 is provided inside the reaction tower 11 to detect the internal temperature of the reaction tower 11 (step s2). The temperature detection result detected by this temperature sensor 15 is transmitted to the rotation control section 73, and the rotation control section 73 controls the rotary valve 33, the upstream screw blade 43, the vertical screw The rotational speed of the blades 52 is controlled to adjust the amount of torrefied wood chips S to be conveyed (step s6).

Similarly, the storage amount detection sensor 16 also detects the amount of torrefied wood chips S accumulated inside the reaction tower 11 (step s3), and the detection result is transmitted to the rotation control section 73. Then, the rotation control unit 73 controls the rotational speed of the rotary valve 33, the upstream screw blade 43, and the vertical screw blade 52 based on the transmitted detection result information, and adjusts the conveyance amount of the torrefied wood chips S. (step s6).

Furthermore, the components of the generated gas G generated from the reaction tower 11 are analyzed by the gas analyzer 72 installed before the gas storage section 60 (step s4). This analysis result is also sent to the rotation control unit 73, and the rotation control unit 73 controls the rotational speed of the rotary valve 33, upstream screw blade 43, and vertical screw blade 52 based on the sent analysis result information. , the amount of torrefied wood chips S to be transported is adjusted (step s6).

For example, if the temperature sensor 15 detects that the internal temperature of the reaction tower 11 is lower than the appropriate temperature (step s2: No), the torrefied wood chips S being conveyed to the reaction tower 11 cannot be efficiently gasified. . In this case, the rotation control unit 73 that has received the temperature detection result controls the rotary valve motor 34 to increase the rotation speed of the rotary valve 33 and increase the amount of torrefied wood chips S conveyed to the supply pipe 32. be able to.

In addition, the rotation control unit 73 controls the rotation motor 44 and the rotation motor 53 to adjust the rotation speed of the upstream screw blade 43 and the vertical screw blade 52, thereby controlling the torrefied wood chips S in the intermediate conveying pipe 42. The torrefied wood chips S can be further compacted and subdivided. Specifically, by making the rotation speed of the upstream screw blade 43 faster than the rotation speed of the vertical screw blade 52 (step s6), a large amount of torrefied wood chips S transported from the surge tank 30 are transferred to the intermediate transport pipe. 42, it becomes more clogged and becomes more compacted. Since the torrefied wood chips S compacted in this way are conveyed to the reaction tower 11 by the vertical screw blades 52, the torrefied wood chips S can be further divided into smaller pieces.
Thereby, the torrefied wood chips S transported to the reaction tower 11 are efficiently gasified, and the internal temperature of the reaction tower 11 can be increased.

Similarly, when the amount of torrefied wood chips S inside the reaction tower 11 is decreasing, the storage amount detection sensor 16 detects the decrease in torrefied wood chips S (step s3: No), and The information is transmitted to the rotation control section 73. Based on this information, the rotation control unit 73 controls the rotation motor 44 to increase the rotation speed of the upstream screw blade 43, and the rotation control unit 73 controls the rotation motor 53 to rotate the vertical screw blade 52. By increasing the speed (step s6), the amount of torrefied wood chips S transported to the reaction tower 11 can be increased, and gasification of the torrefied wood chips S can be promoted.

Conversely, when the amount of torrefied wood chips S accumulated inside the reaction tower 11 is increasing, the storage amount detection sensor 16 detects the increase in torrefied wood chips S (step s3: No). , transmits the information to the rotation control section 73. Based on this information, the rotation control unit 73 reduces the rotation speed of the vertical screw blades 52 (step s6) to further consolidate the torrefied wood chips S in the intermediate conveyance pipe 42. Thereby, the more finely divided torrefied wood chips S can be transported to the reaction tower 11 by the vertical screw blades 52 .
Therefore, since the torrefied wood chips S can be divided into smaller pieces while reducing the amount of torrefied wood chips S to be transported, the surface area of the torrefied wood chips S can be expanded, and the torrefied wood chips S can be gasified efficiently.

Similarly, if the components of the generated gas G detected by the gas analyzer 72 are not at the desired ratio (step s4: No), the rotation control unit 73 controls the rotation of the rotary valve motor 34 based on this information. The motor 44 and rotary motor 53 are controlled to adjust their respective rotational speeds (step s6). As a result, the amount, size, and density of the torrefied wood chips S to be transported to the reaction tower 11 are adjusted, and the components of the generated gas G are adjusted to an appropriate ratio.

In this way, until a predetermined amount of produced gas G is obtained (step s5), the rotational speeds of the rotary valve 33, upstream screw blades 43, and vertical screw blades 52 are adjusted according to the internal situation of the reaction tower 11. The torrefied wood chips S are repeatedly gasified in a desired state. After a predetermined amount of generated gas G is obtained, the rotation of the rotary valve 33, upstream screw blade 43, and vertical screw blade 52 is stopped to complete gasification.

Note that by controlling the gasifying agent supply device 18 with the rotation control unit 73, the amount of gasifying agent H supplied from the first supply pipe 13a and the second supply pipe 13b is controlled, and the inside of the reaction tower 11 is controlled. Gasification can also be adjusted.

The gasification system 1 configured in this way is composed of a conveying device 20 into which torrefied wood chips S are introduced, and a reaction tower 11 which gasifies the torrefied wood chips S. A vertical conveyance path 50 is provided for conveying torrefied wood chips S from the bottom of the column 11 in the vertical direction (up and down direction), and the reaction column 11 is provided with a generated gas gasified from the torrefied wood chips S. A discharge pipe 12 for discharging G is provided above, and a vertical conveyance path 50 is formed in a tubular shape along the vertical direction. A vertical screw blade 52 is provided that is rotatable about a shaft that is a rotation axis, and the upper end portion (exposed portion 52a) of the vertical screw blade 52 is exposed above the bottom of the reaction tower 11.

As a result, the torrefied wood chips S can be transported from below to the high temperature layer in the reaction tower 11, and the torrefied wood chips S that have fallen without being gasified in the reduction zone T3 in the exposed portion 52a can be transported to the reaction tower 11. Together with the torrefied wood chips S newly introduced into the reactor 11, the torrefied wood chips S can be transported again to the reduction zone T3 in the reaction tower 11.

Thereby, the torrefied wood chips S that have not been sufficiently gasified can be gasified together with new torrefied wood chips S. That is, the torrefied wood chips S that have not been gasified inside the reaction tower 11 can be circulated and reused, and the torrefied wood chips S with high energy density can be efficiently gasified.

Further, since the torrefied wood chips S that have fallen to the bottom can be transported upward again by the exposed portion 52a, the torrefied wood chips S that have fallen from above and are piled up can be broken up. As a result, the stacked torrefied wood chips S collapse, and the bridge formed by the torrefied wood chips S can be eliminated. Therefore, the torrefied wood chips S can be stably gasified in the high temperature layer.

Further, the conveyance device 20 is provided with an input port into which torrefied wood chips S are inputted at one end side, and a tubular upstream conveyor connected to the vertical conveyance path 50 in a cross direction at the other end side. The upstream conveyance path 40 is formed in a spiral shape within the pipe, and is provided with an upstream screw blade 43 that conveys the torrefied wood chips S toward the vertical conveyance path 50 by rotation. ing.

Thereby, when the torrefied wood chips S are conveyed from the upstream conveyance path 40 to the longitudinal conveyance path 50, the torrefied wood chips S can be divided into small pieces. Thereby, the torrefied wood chips S of a desired size can be transported to the reaction tower 11, so that the torrefied wood chips S with high energy density can be efficiently gasified.

To explain in detail, the torrefied wood chips S carried out from the upstream conveyance path 40 by the upstream screw blade 43 are taken into the vertical conveyance path 50 by the vertical screw blade 52 and conveyed. By adjusting the conveyance amount of 43 and the conveyance amount of the vertical screw blade 52, the torrefied wood chips S are consolidated and finely divided between the vertical conveyance path 50 and the upstream conveyance path 40, and the torrefied wood chips S are divided into desired sizes. can do. By fragmenting the torrefied wood chips S in this way, it is possible to reliably prevent the torrefied wood chips S conveyed to the reaction tower 11 from forming bridges, and to prevent the torrefied wood chips S from forming a bridge. S has an expanded surface area and can be efficiently gasified.

In addition, by individually adjusting the rotational speed of the upstream screw blade 43 and the vertical screw blade 52, the subdivision size of the new torrefied wood chips S to be conveyed can be adjusted, and the conveyance amount of the new torrefied wood chips S can be adjusted. It is possible to reuse the torrefied wood chips S accumulated at the bottom of the reaction tower 11 by limiting the amount of torrefied wood chips S, or to increase the amount of new torrefied wood chips S transported. That is, it is possible to more efficiently gasify the torrefied wood chips S according to the conditions of the reaction tower 11.

Furthermore, since the reaction tower 11 is provided with the gasifying agent supply pipe 13 for injecting the gasifying agent H, the gasifying agent H promotes the gasification of the torrefied wood chips S, resulting in high energy density. The torrefied wood chips S can be gasified more efficiently.

Furthermore, since a rotation control section 73 is provided that controls the rotation speed of the vertical screw blade 52 and adjusts the amount of torrefied wood chips S to be transported to the reaction tower 11, the internal situation of the reaction tower 11 can be controlled. The amount of torrefied wood chips S to be conveyed can be adjusted accordingly, and the torrefied wood chips S can be gasified more efficiently.

For example, if there are too many torrefied wood chips S transported into the reaction tower 11, the amount of torrefied wood chips S transported into the reaction tower 11 is reduced, and the half-carbonized wood chips S accumulated inside the reaction tower 11 are reduced. The carbonized wood chips S can be adjusted to be thermally decomposed and gasified. On the other hand, if there are too few torrefied wood chips S inside the reaction tower 11, the amount of torrefied wood chips S conveyed into the inside of the reaction tower 11 is increased to increase the material for gasification. gasification can be promoted.

Further, the reaction tower 11 is equipped with a storage amount detection sensor 16 that detects the amount of torrefied wood chips S accumulated inside the reaction tower 11, and the rotation control unit 73 is configured to detect the amount of torrefied wood chips S detected by the storage amount detection sensor 16. By controlling the rotational speed of the vertical screw blade 52 based on the amount of torrefied wood chips S, the amount of torrefied wood chips S to be conveyed can be adjusted based on the detection result of the storage amount detection sensor 16.

That is, depending on the amount of torrefied wood chips S accumulated inside the reaction tower 11, the torrefied wood chips S are transported to the reaction tower 11, and an appropriate amount of torrefied wood chips S is accumulated inside the reaction tower 11. can be done. Therefore, the torrefied wood chips S can be gasified more efficiently.

Further, the reaction tower 11 is equipped with a temperature sensor 15 that detects the internal temperature, and the rotation control unit 73 controls the rotation speed of the vertical screw blade 52 based on the temperature detected by the temperature sensor 15. Accordingly, the amount of torrefied wood chips S to be conveyed can be adjusted based on the detection result of the temperature sensor 15.

That is, depending on the temperature inside the reaction tower 11, the torrefied wood chips S can be transported to the reaction tower 11, and an appropriate amount of torrefied wood chips S can be accumulated inside the reaction tower 11. Therefore, the torrefied wood chips S can be gasified more efficiently.

For example, if it is detected that the internal temperature of the reaction tower 11 has increased compared to the desired temperature, the rotation speed of the vertical screw blade 52 is increased to increase the number of torrefied wood chips S inside the reaction tower 11. can be transported to lower the internal temperature of the reaction tower 11. On the other hand, if it is detected that the internal temperature of the reaction tower 11 is lower than the desired temperature, the rotation speed of the vertical screw blade 52 is lowered, and the torrefied wood chips transported into the reaction tower 11 are lowered. By reducing the amount of S, the reaction efficiency of the torrefied wood chips S accumulated inside can be increased, and the torrefied wood chips S can be gasified more efficiently.

Furthermore, a gas analyzer 72 for analyzing gas components is provided, and the rotation control unit 73 controls the rotation speed of the vertical screw blade 52 based on the gas components. Based on the detection result, the amount of torrefied wood chips S to be transported can be adjusted, and the torrefied wood chips S can be gasified more efficiently.

Specifically, the components of the gas released from the reaction tower 11 vary depending on the internal temperature of the reaction tower 11, the ratio of the gasifying agent H, and the like. From this, it is possible to adjust the internal temperature of the reaction tower 11 and the ratio of the gasifying agent H by adjusting the amount of torrefied wood chips S to be transported based on the components of the gas to be released. supply. As a result, the amount of torrefied wood chips S to be transported can be adjusted depending on the gasification state inside the reaction tower 11, and an appropriate amount of torrefied wood chips S can be accumulated inside the reaction tower 11 to more efficiently halve the chips. Carbonized wood chips S can be gasified.

In addition, the discharge pipe 12 is configured to have a negative pressure on the tip side, so that the gas that has been gasified inside the reaction tower 11 can be sucked into the discharge pipe 12. can be reliably released from the release pipe 12.

Furthermore, since the gasifying agent H supplied from the gasifying agent supply pipe 13 can be drawn into the reaction tower 11 to generate an upward air current, the torrefied wood chips S conveyed by the vertical screw blades 52 can be reduced. It becomes easier to lift it upwards where band T3 is formed. Furthermore, torrefied wood chips S that have not been completely gasified can be drawn into the discharge pipe 12.

Furthermore, the discharge tube 12 is provided with the distal discharge tube 12c, which has a smaller diameter at the distal end than the proximal end, so that the distal end of the discharge tube 12 has a smaller diameter. As a result, the flow velocity of the produced gas G, torrefied wood chips S, etc. flowing through the reduced diameter portion 12b and the distal end discharge pipe 12c becomes faster, and the temperature at the location where the flow velocity becomes faster rises, preventing complete gasification. The combustion residue of the torrefied wood chips S can be gasified in the discharge pipe 12.

In addition, an ash discharge section 17 is provided at the bottom of the reaction tower 11 to discharge the torrefied wood chips S accumulated at the bottom. It is possible to discharge torrefied wood chips S and the like accumulated in a position where they cannot be transported upwards from the bottom.

In the correspondence between the configuration of this invention and the above-described embodiments,
The wood chips correspond to torrefied wood chips S, and similarly,
The loading mechanism corresponds to the transport device 20,
The reaction tower corresponds to the reaction tower 11,
The gasifier corresponds to gasification system 1,
The vertical conveyance path corresponds to the vertical conveyance path 50,
The discharge pipe corresponds to the discharge pipe 12,
The vertical screw blade corresponds to the vertical screw blade 52 ,
The upstream conveyance path corresponds to the upstream conveyance pipe 41,
The upstream screw blade corresponds to the upstream screw blade 43,
The injection part corresponds to the gasifying agent supply pipe 13,
The conveyance amount control section corresponds to the rotation control section 73,
The storage amount detection section corresponds to the storage amount detection sensor 16,
The temperature detection section corresponds to the temperature sensor 15,
The analysis section corresponds to the gas analyzer 72,
The narrow diameter portion corresponds to the distal end discharge tube 12c,
The ash discharge section corresponds to the ash discharge section 17, but
This invention is not limited only to the configuration of the above-described embodiments, but can be implemented in many other embodiments.

For example, in the present embodiment, the vertical conveyance path 50 is vertically disposed vertically (in the vertical direction) with respect to the reaction tower 11, but it is not necessary to completely coincide with the vertical direction. For example, the vertical conveyance path 50 may be inclined at approximately ±30 degrees with respect to the vertical direction.

Further, in this embodiment, the intermediate conveyance pipe 42 and the vertical conveyance pipe 51 are orthogonal at the connecting portion, but they do not necessarily need to be orthogonal, and the intermediate conveyor pipe 42 and the vertical conveyor pipe 51 are That's fine. Further, the upstream conveyance pipe 41 may be arranged in a direction intersecting the vertical direction, for example, along the horizontal direction, and furthermore, the upstream conveyance pipe 41 and the vertical conveyance pipe 51 may be directly connected.

Further, as long as the vertical screw blades 52 can transport the torrefied wood chips S accumulated below the reaction tower 11 upward, the vertical transport path 50 may have any configuration. For example, in the vertical conveyance path 50, a partial opening is formed in a vertical conveyance pipe 51 extending upward inside the reaction tower 11, and the vertical screw blade 52 is partially exposed from this opening. Good too.

Further, as the gasifying agent, air and water vapor are used in this embodiment, but the gasifying agent is not particularly limited as long as it promotes gasification of the semi-carbonized wood chips S. Therefore, for example, in addition to gas such as oxygen, other gases, powders, liquids, etc. may be used.

Furthermore, the rotation control unit 73 controls the rotation control unit 73 based on, for example, the accumulated amount and density of the torrefied wood chips S introduced into the reaction tower 11, the temperature inside the reaction tower 11, the components of the gas released, or the like. The amount of torrefied wood chips S to be conveyed may be controlled by a combination of these.

Furthermore, the upstream screw blade 43 is configured to extend along the upstream conveying pipe 41 and the intermediate conveying pipe 42 from the upper end of the upstream conveying pipe 41 to the tip of the intermediate conveying pipe 42. However, the configuration is not limited to this, and for example, a so-called screw feeder that is rotatable about an axis along the vertical direction is installed inside the upstream conveyance pipe 41, and a so-called screw feeder is installed inside the curved intermediate conveyance pipe 42. , a so-called spring conveyor blade such as the upstream screw blade 43 that can transmit the rotation of a screw feeder provided inside the upstream conveying pipe 41 may be used.

1 Gasification system 11 Reaction tower 12 Discharge pipe 12c Tip side discharge pipe 13 Gasifying agent supply pipe 15 Temperature sensor 16 Storage amount detection sensor 17 Ash discharge section 20 Conveyance device 40 Upstream conveyance path 43 Upstream screw blade 50 Vertical conveyance Channel 52 Vertical screw blade 72 Gas analyzer 73 Rotation control section S Torrefied wood chips

Claims (10)

A gasifier for gasifying the wood chips, comprising an input mechanism for inputting torrefied wood chips, and a reaction tower for gasifying the wood chips,
The input mechanism is
comprising a tubular longitudinal conveyance path along the vertical direction that conveys the wood chips from the bottom of the reaction tower to the inside;
The reaction tower includes
A discharge pipe for discharging gasified gas from the wood chips is provided above;
The longitudinal conveyance path is
A vertical screw blade is provided in the pipe in a spiral shape along the vertical direction and rotatable about an axis along the vertical direction as a rotation axis,
A gasifier in which the longitudinal screw blades are exposed above the bottom of the reaction column. The input mechanism is
An input port into which the wood chips are inputted is provided on one end side, and a tubular upstream conveyance path connected to the vertical conveyance path in a cross direction is provided on the other end side,
The upstream conveyance path is
2. The gasification apparatus according to claim 1, further comprising an upstream screw blade formed in a spiral shape in a pipe and configured to rotate to convey the wood chips toward the longitudinal conveyance path. 3. The gasification apparatus according to claim 1, wherein the reaction tower is provided with an injection part for injecting a gasification agent. 4. The method according to claim 1, further comprising a conveyance amount control section that controls the rotational speed of the vertical screw blade and adjusts the conveyance amount of the wood chips to be conveyed to the reaction tower. Gasifier. The reaction tower is
an accumulation amount detection unit that detects the amount of the wood chips accumulated inside the reaction tower;
The conveyance amount control section includes:
The gasifier according to claim 4, wherein the rotational speed of the vertical screw blade is controlled based on the amount of the wood chips detected by the accumulation amount detection section. The reaction tower is
Equipped with a temperature detection section that detects the internal temperature,
The conveyance amount control section includes:
The gasification apparatus according to claim 4 or 5, wherein the rotational speed of the vertical screw blade is controlled based on the temperature detected by the temperature detection section. an analysis section that analyzes the components of the gas,
The conveyance amount control section is
The gasifier according to any one of claims 4 to 6, wherein the rotational speed of the vertical screw blade is controlled based on the components of the gas. The gasification apparatus according to any one of claims 1 to 7, wherein the discharge pipe is configured such that a distal end thereof is under negative pressure. 9. The gasifier according to any one of claims 1 to 8, wherein the discharge tube is provided with a narrow diameter portion having a smaller diameter at the tip than at the proximal end. 10. The gasification apparatus according to claim 1, wherein the bottom of the reaction tower is provided with an ash discharge section for discharging the wood chips accumulated at the bottom.

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