JP3558358B2 - Horizontal rotation activation device - Google Patents

Description

[0001]
[Industrial applications]
The present invention provides a temperature, atmosphere, and residence time suitable for processing conditions while heating and granulating the powdery carbonaceous material to dry distill and carbonize the powdery carbonaceous material by contacting the powdery carbonaceous material with steam. Activated carbon suitable for long-term stable operation with high thermal efficiency without causing environmental pollution by achieving various processes of drying, carbonizing, activating, and cooling powders continuously and consistently in one unit with high efficiency. The present invention relates to a horizontal rotary activation device for production.
[0002]
[Prior art]
When manufacturing activated carbon from plant raw materials such as coconut shells and sawdust or raw materials such as lignite and coal, and activated carbon from molded pellets, it is necessary to go through four steps of drying, carbonization, activation and cooling. Do it in a separate device.
[0003]
The activation of the carbonaceous powder particles obtained by the carbonization step with water vapor has been conventionally performed in many cases by using any of a separately prepared multi-stage floor furnace, an internally heated rotary furnace and a fluidized bed furnace.
[0004]
The multi-stage furnace has a multi-stage hearth that forms a space in which the granules fall, and the heating gas is raised from below through the space, and the granules falling sequentially are heated in each hearth. It will be activated gradually.
[0005]
The internal heating type rotary furnace transfers powder particles from the upper end to the lower end in a cylindrical furnace that rotates around an axis that is slightly inclined with respect to the horizontal plane, while heating gas is applied to the powder particles from the lower end to the upper end. The powder is heated and activated by countercurrent.
[0006]
Further, the fluidized bed furnace heats the granular material by disposing the granular material on a mesh provided in the vertical cylindrical body, and allowing the heating gas supplied from below to flow through the granular material. Is activated.
[0007]
[Problems to be solved by the invention]
However, in the case of the above-mentioned conventional apparatus, there are the following problems in safely, continuously and economically obtaining the target activated carbon without polluting the environment.
[0008]
{Circle around (1)} In the multi-stage floor furnace, the internally heated rotary furnace, and the fluidized bed furnace in which the carbonaceous powder is activated by steam, the temperature, atmosphere, and residence time suitable for the processing conditions cannot be simultaneously satisfied. In particular, the multi-stage furnace and the internally heated rotary furnace do not have a means for maintaining the steam concentration in the furnace at an optimum value for the activation reaction, so that the activation requires a long time. Further, the fluidized bed furnace cannot be operated continuously to keep the residence time of the carbonaceous powder particles constant.
[0009]
(2) Despite the fact that a large amount of combustible gas is generated per unit mass of product due to the activation reaction, in the furnaces for activation of each of the above types, it is necessary to effectively use most of the energy possessed by the furnace. It cannot be released and is released into the atmosphere as combustion gas.
[0010]
{Circle around (3)} In the case of the above-mentioned conventional apparatus, the construction cost, operation cost, and labor cost of the apparatus are increased because four apparatuses, a drying apparatus, a carbonizing furnace, an activation furnace, and a cooling apparatus are required. In addition, since these furnaces are provided separately, there is an increased chance of leakage during handling of the particulate carbonaceous material between the furnaces, which significantly deteriorates the working environment.
[0011]
The present invention solves the above-mentioned problems of the conventional apparatus, and enables the continuous production of activated carbon, which requires four steps of drying, carbonization, activation and cooling, in a single apparatus consistently and continuously. It is an object of the present invention to provide a horizontal rotation activation device that enables a large amount of combustible gas generated per unit mass of a product to be used as a by-product in a dense state and that can continuously remove low-temperature products.
[0012]
[Means for Solving the Problems]
According to the present invention, the object is to provide a rotatable cylindrical body whose rotation axis is substantially horizontal, has an opening at one end in the axial direction, and has the other end closed. An inner cylinder having an axial line shared or parallel to the cylindrical body and open at both ends, and an opening side where an annular space between the cylindrical body and the inner cylinder is divided at an intermediate portion in the axial direction. and substantially parallel partition walls in the axial line divided into a plurality of axial space extending two regions of a region and the innermost side region in the axial direction, are arranged at intervals in the axial direction have a tilt angle with respect to the axis A plurality of guide plates attached to at least both sides of the partition wall in the opening side region so that the inclination angle of the guide plate is such that each surface of the partition wall faces upward when each surface of the partition wall faces upward. Guide plates in opposite directions, and each of a plurality of guide plates arranged in the axial direction Edges plurality of axial space between which is divided by at least partially form a gap above the partition wall between the inner surface of the tubular body, in the axial direction, the opening position, an intermediate portion position and the rear portion The axial space is communicated with each other at a position, and the axial space is provided with a blow hole for receiving supply of steam from the outside and injecting the steam toward the axial space in the back side region. Achieved.
[0013]
[Action]
The raw material in powder form generally contains moisture, and the raw material is supplied to an annular space between the cylindrical body and the inner cylinder from an inlet provided at an opening at one end of the cylindrical body. The cylindrical body rotates around a substantially horizontal axis, and due to the action of the partition wall and the guide plate installed in the opening side area in the annular space, the powder and granules are partitioned according to the rotation of the cylindrical body. A circulating flow is formed between the two ends of the wall, part of which enters the next deeper area.
[0014]
Since the rotating cylindrical body is heated, the raw material powder containing water is dried at a substantially constant temperature in the opening side region. For a raw material containing no water, the step in the opening side region can be omitted.
[0015]
The dried raw material particles sequentially proceed to the back side region in the annular space between the cylindrical body and the inner cylinder. In the rear region, the raw material particles are sequentially supplied to the opening-side region even if a means for positively transferring the particles is not provided. A part of the granules to be introduced enters the inner region, which pushes the granules in the inner region to the inner part to be transferred. At that time, since the rotating cylindrical body is heated, the raw material powder is heated at a substantially constant temperature, and a part or all of the carbonization reaction is released by releasing combustible gas in the front part of the back side area. To achieve.
[0016]
When the carbonized powder reaches the rear part of the back side area, steam is injected from the fuze holes provided in the area, and the temperature rises to the temperature necessary for the activation reaction in a state where the steam is contained, and the activation is performed. Is performed.
[0017]
The activated carbon at a high temperature after the activation reaction changes its direction from the back of the back side region, flows into the inner cylinder, and flows toward the raw material inlet opening through the inner cylinder as the cylindrical body rotates. And flows out of the device through the opening. At that time, since the low-temperature raw material particles exist in the annular space between the cylindrical body and the inner cylinder, the activated carbon as a product is cooled by the heat energy exchange through the inner cylinder with the low-temperature raw material. It is taken out in a state.
[0018]
The combustible gas generated by thermal decomposition of water vapor and raw materials generated in the cylindrical body, the combustible gas generated by activation of carbonaceous particles, and unreacted water vapor are located near the opening on the supply side of the raw material particles and the product. Although discharged from the apparatus from both or one of the outlet openings (one end of the inner cylinder), these are not mixed with the combustion gas, so that a large amount of combustible gas can be obtained as a by-product without being diluted.
[0019]
The cylindrical body rotating around a substantially horizontal axis can increase the volume filling ratio of the granular material with respect to the internal space volume to about 35 to 45%, and by the introduction of water vapor from the blowing holes. The time required for the activation reaction is greatly reduced, and the equipment is much smaller than in the prior art.
[0020]
【Example】
Hereinafter, embodiments of the present invention will be described with reference to the accompanying drawings.
[0021]
<First embodiment>
In FIG. 1, an axis 1 is substantially horizontal, and a cylindrical body 2 which is driven to rotate around the axis 1 is rotatably supported by a bearing (not shown). The cylindrical body 2 can rotate relative to the raw material side hood 3 and the product side hood 4 fixed in the space at the opening side of the cylindrical body 2 while maintaining airtightness. The method of sealing for hermetic rotation is optional. The raw material side hood 3 is provided with a raw material feed pipe 8 and an exhaust pipe 14, and the product side hood 4 is provided with a product discharge pipe 13 and an exhaust pipe 15, respectively.
[0022]
An inner cylinder 5 having substantially the same axis is provided integrally with the cylindrical body 2 inside the cylindrical body 2, and as a preferred embodiment, an inclined guide is provided inside the inner cylinder 5. A partition wall 7 having plates 6, 6 'is mounted. The partition wall 7 is disposed on a plane including the axis 1 or a parallel plane, and divides the internal space of the inner cylinder 5 into two spaces extending in the axial direction. The guide plates 6 and 6 ′ are provided on both sides of the partition wall 7, and when the respective surfaces of the partition wall 7 rotate downward from a position where the partition wall 7 faces upward, the powder and granules are separated from the guide plates 6 and 6 ′. 'And slide down to go to the left in Fig. 1. It should be noted that a known spiral plate may be used instead of the partition wall 7 having the guide plates 6 and 6 ′.
[0023]
The annular space between the inner cylinder 5 and the tubular body 2 is divided into an opening-side region and a back-side region at an intermediate portion in the axial direction, and a surface including the axis 1 in each region or It is divided into a plurality of axial spaces by partition walls 9, 11 arranged on parallel surfaces. In the case of the illustrated example, as shown in FIG. 2A, in the opening-side region, the partition wall 9 on one surface forms two axial spaces, and in the back-side region, FIG. As can be seen, it is divided into four axial spaces by a partition wall 11 on two sides forming a cross. The plurality of axial spaces separated by the partition walls 9 and 11 communicate with each other at an opening P, an intermediate portion Q, and a depth R of the tubular body 2.
[0024]
Guide plates 10 and 10 ′ that are inclined are provided on the partition wall 9 on both sides of the partition wall 9. These guide plates 10, 10 'are mounted in opposite directions to each other when each of the two surfaces of the partition wall 9 faces upward. 2A, the edges of the guide plates 10, 10 'are partially cut off linearly to have a clearance between the guide plate 10, 10' and the inner surface of the cylindrical body 2, so that the guide plates 10 and 10 ' Spaces formed between adjacent guide plates communicate with each other at the inner surface position of the tubular body 2. Therefore, granular material on one surface along the inner surface of the cylindrical body 2 while sliding the guide plate when said surface is rotated to face downward from above proceeds to the right in FIG. 1, to On the other hand, the granular material on the other surface advances to the left.
[0025]
The partition wall 11 that divides the inner space into four axial spaces has a large number of blowholes 12 formed in the inner wall (right portion) (see also FIG. 2C). In the case of the example shown in the figure, the fumaroles 12 are more densely distributed toward the inner part, and are supplied with water vapor from the outside and blow it out into the axial space.
[0026]
In the apparatus of this embodiment, the production of activated carbon is performed in the following manner.
[0027]
The carbonaceous raw material powder as a raw material for the production of activated carbon is fed from a raw material feed pipe 8 into an annular space (opening side region) between the cylindrical body and the inner cylinder, and then into the cylindrical body 2 and the inner cylinder 5. Rolls at the bottom of the annular space with the rotation of. As described above, in the opening-side region, the powder and granules travel in the opposite directions due to the action of the guide plates 10 and 10 ′ during rotation in the two axial spaces separated by the partition wall 9. A circulating flow is created in the two axial spaces via P and the intermediate section Q.
[0028]
The cylindrical body 5 is externally heated by means (not shown), and the raw material particles forming the circulating flow are heated to a substantially uniform temperature and sufficiently dried.
[0029]
In the axial direction, a circulating flow of the granular material formed in the area of the partition wall 9 is formed. Here, since the granular material is sequentially supplied from the raw material feed pipe 8, it is pushed by this. Thus, a part of the circulating flow enters the next deeper side area. The inner region is divided into four axial spaces by a partition wall 11 and does not particularly have a means for transferring the granular material. The granular material is pushed by the granular material from the opening side region, and the granular material further moves to the back.
[0030]
The granular material is also heated to a uniform temperature via the tubular body 2 in the deep region where the partition wall 11 exists. Then, along with the transition, the dry distillation and carbonization of the granular material proceed at the front of the region.
[0031]
When the carbonized powder reaches the rear part of the back side region, it receives the injection of water vapor from the fumarole 12 and comes into contact with sufficient water vapor, and is activated by heating here to generate activated carbon. At this time, since the temperature of the powder increases as it moves to the right in FIG. 1, the distribution density of the blast holes 12 is correspondingly increased so that the steam injection amount increases toward the right in response to this. .
[0032]
At a predetermined temperature, activated carbon activated at a predetermined temperature and in a steam atmosphere flows from the bottom of the cylindrical body 1 to a predetermined height, and flows into the right end of the inner cylinder 5 from near one end of the partition wall 11 in FIG. With the rotation of the tubular body 2, it moves in the inner cylinder 5 to the left, that is, in the direction of the product side hood 4 at a substantially constant speed by the action of the guide plates 6 and 6 ′, and discharges the product side hood 4. It is discharged out of the device via the pipe 13. At this time, the high-temperature activated carbon moving in the inner cylinder 5 exchanges thermal energy via the inner cylinder 5 with the low-temperature raw material powder rolling in the annular space between the cylindrical body 2 and the inner cylinder 5. Then, the temperature is lowered to reach the product discharge pipe 13.
[0033]
The pyrolysis gas, combustible gas by activation and unreacted steam are taken out from the exhaust pipes 14 and 15, and one or both of them can be used at the same time depending on the conditions required for the pyrolysis and activation.
[0034]
<Second embodiment>
FIG. 3 shows a second embodiment of the apparatus according to the present invention, which is suitable for activating a raw material powder containing more moisture than the target raw material. In FIG. 3, reference numeral 16 denotes a range of the steam blowing holes 12 provided on the partition wall 11 in the same manner as in the previous embodiment.
[0035]
The present embodiment is characterized in that the partition wall in the opening side region of the previous embodiment is opened at an intermediate portion in the axial direction, and a circulating flow is generated at a front portion and a rear portion of the region. There is. In the example specifically shown in FIG. 3, another partition wall 17 and guide plates 18 and 18 'having the same structure as the opening side area are additionally provided at the front stage of the apparatus of the previous embodiment.
[0036]
In this embodiment, the raw material granules containing a large amount of water fall into the annular space between the cylindrical body 2 and the inner cylinder 5 after being fed and roll at the bottom thereof, and The circulation flow is formed between both ends of the partition wall 17 by the action of the additional partition wall 17 and the guide plates 18 and 18 ′ provided thereon. The raw material particles circulating between the two sides of the partition wall 17 evaporate moisture by heating from the outside of the cylindrical body 2, and enter a region of the partition wall 9 with a small amount of moisture.
[0037]
The behavior of the raw material particles that have advanced to the region of the partition wall 9 in the annular space between the cylindrical body 2 and the inner cylinder 5 is the same as in the first embodiment.
[0038]
In the first and second embodiments, the section taken along the line YY 'in FIGS. 1 and 3 is not limited to the one shown in FIG. 2B, but may be a partition wall in an annular space between the cylindrical body and the inner cylinder. May be two or three as shown in FIGS. 4 (A) and 4 (B), and may be shown in FIGS. 4 (C) and 4 (D) in all or a part of the axial range of the partition wall. May be provided with such guide plates 19, 19 '. At that time, the angle of the partition wall 7 installed in the inner cylinder is not necessarily limited to the angle shown in FIG. 1, and may be any angle such as, for example, 45 degrees, and includes a known spiral plate. There may be. Further, guide plates 19, 19 ', 19 ", 19"' may be provided in the annular space between the cylindrical body 2 and the inner cylinder as shown in FIGS.
[0039]
<Third embodiment>
FIG. 5 shows a third embodiment in which guide plates 19 and 19 ′ are installed on a partition wall 11 in a range of the rightmost end of a deep side region in an annular space between the cylindrical body 2 and the inner cylinder 5 (FIG. 4). This is an example in the case of the structure shown in C). According to the present embodiment, the rightward transfer of the granular material in the inner region is promoted.
[0040]
<Fourth embodiment>
FIG. 6 shows a fourth embodiment in which guide plates 19, 19 ′, 19 ″, 19 ′ ″ are provided on a partition wall 11 in the rightmost end region of the back side region in the annular space between the cylindrical body 2 and the inner cylinder 5. This is an example in the case of the structure shown in FIG.
[0041]
<Fifth embodiment>
In this embodiment, as shown in FIG. 7, the cylindrical body 2 is covered with an outer cylinder 20 made of a heat-resistant and heat-insulating material, and electric resistance heating elements 21, 21 ′, 21 ″ are provided on the inner surface of the outer cylinder 20 as a heating device. Thus, the cylindrical body 2 of each of the above-described embodiments is heated by the electric resistance heating elements 21, 21 ', 21 ". At that time, the type, shape, arrangement and number of the electric resistance heating elements are arbitrary. The outer cylinder 20 may be fixed in a space with respect to the cylindrical body 2 rotating around the substantially horizontal axis 1, or may rotate together with the cylindrical body 2.
[0042]
<Sixth embodiment>
FIG. 8 shows that the cylindrical body 2 is heated by flowing a high-temperature combustion gas through the annular space between the cylindrical body 2 and the outer cylinder 20 without using the electric resistance heating element as in the fifth embodiment. This is a sixth embodiment showing the case. In FIG. 8, reference numeral 22 denotes a fuel inlet pipe, which feeds air at normal temperature or preheated from the inlet pipe 22 to burn fuel inside the combustion chamber 24. Here, reference numeral 25 denotes a refractory material wall for protecting one end surface of the cylindrical body 2, but may be omitted if unnecessary. The high-temperature combustion gas generated inside the combustion chamber 24 is provided with a material feed pipe 8 of the cylindrical body 2 through a flow path 26 formed in an annular space between the cylindrical body 2 and the outer cylinder 20. The tubular body 2 is heated while flowing toward the end portion, and is discharged outside the apparatus through one or more combustion gas discharge ports 27 provided near the end portion of the outer tube 20. At that time, the combustion gas can be discharged using the combustion gas discharge hood 28. One or more air inlets 29 may be provided at an intermediate position of the outer cylinder 20, and air may be sent in through the conduit 30 and the valve 31 to adjust the temperature. At this time, the shape, size, number and arrangement of the air inlets 29 are arbitrary, and the type and operation method of the valve 31 are also arbitrary.
[0043]
FIG. 8 shows an example in which the cylindrical body 2 and the outer cylinder 20 are integrally rotated around an axis. The cylindrical body 2 has a flow path for combustion gas, and is provided at an appropriate position in the axial direction. Since the cylindrical body 2 is supported by the outer cylinder 20 by the portion 32, even if the strength of the cylindrical body 2 is reduced at a high temperature, a large stress based on the deformation does not act on the cylindrical body 2; There is no fear that 2 will break. Even when operating at a high temperature close to the softening point of the cylindrical body 2 at high temperatures, the cross section of the cylindrical body is kept substantially circular because it rotates around the horizontal axis and can be supported all around.
[0044]
The support portion shown in FIG. 8 is an example in which the same material as the heat-resistant and heat-insulating material constituting the outer cylinder 20 is used. The shape, size, and material are arbitrary, and for example, as shown in FIG. The support 33 may be made of a heat-resistant metal, and its shape, dimensions, number, and arrangement method are arbitrary.
[0045]
In order to facilitate the transfer of thermal energy from the combustion gas flowing through the annular space between the tubular body 2 and the outer barrel 20 to the tubular body 2, the outer surface of the tubular body 2 extends over a substantially half circumference as shown in FIG. The baffle plate 34 can be installed at a plurality of positions in the axial direction while alternately changing its circumferential position. At this time, the shape, size, number, and arrangement method of the baffle plates 34 are arbitrary.
[0046]
Also, instead of installing the baffle plate 34 shown in FIG. 9 on the outer surface of the cylindrical body 2, the cross-sectional area of the inner surface of the outer cylinder 20 is changed at an arbitrary position as shown in FIGS. It can also be configured.
[0047]
Instead of burning the fuel inside the combustion chamber 24 in FIG. 8, high-temperature combustion gas generated in a combustor (not shown) fixed to the space is supplied to the outer cylinder 20 as shown in FIG. 9. Combustion gas can be sent from one end and passed through the combustion gas distribution section 35 to flow through the cylindrical body 2 and the annular space 26 in the outer cylinder 20. At this time, the sealing method between the rotating outer cylinder 20 and the combustion gas inlet pipe 36 is arbitrary.
[0048]
FIGS. 8, 9 and 10 show an embodiment in which the cylindrical body 2 and the outer cylinder 20 are simultaneously rotated around the axis 1. However, the method of heating the cylindrical body 2 by the combustion gas is not necessarily described above. The configuration is not limited thereto, and a configuration in which the cylindrical body 2 rotates around the axis 1 in the outer cylinder 20 fixed to the space may be used.
[0049]
【The invention's effect】
As described above, in the present invention, the inner cylinder is provided in the rotating cylindrical body, and the raw material powder containing water is supplied from the opening at one end of the cylindrical body to the cylindrical body and the inner cylinder. The circular flow of the raw material particles is formed by the action of the partition wall with the guide plate accompanying the rotation of the tubular body in the opening side region, so that the range of the opening side region is At least, the powder is sufficiently dried by heating from the outside of the cylindrical body.
[0050]
The dried raw material particles continue to advance to the front part of the next inner region, and carbonization proceeds at a temperature suitable for the carbonization reaction by heating from the outside of the cylindrical body, thereby increasing the strength. The carbonized granular material proceeds to the rear part of the back side region, is gradually heated while proceeding, receives the supply of steam, and the activation reaction proceeds, and becomes high-temperature activated carbon. Since a series of steps from the drying to the activation are continuously performed, the size of the apparatus can be reduced and the thermal efficiency can be improved.
[0051]
The high-temperature activated carbon enters the inner cylinder with the rotation of the cylindrical body, changes its direction and moves in the inner cylinder in the direction of the raw material feeding end, so that the size of the apparatus can be reduced, and at that time, the wall surface of the inner cylinder The heat energy is transferred to the low-temperature carbonaceous powder and the raw material powder during drying in the annular space between the cylindrical body and the inner cylinder through, and the temperature is low when discharged from the inner cylinder, Thermal efficiency can be improved.
[0052]
Furthermore, the combustible gas and steam generated can be taken out as a by-product without being diluted, which not only significantly reduces the construction and labor costs of an activated carbon production plant, but also effectively uses energy and purifies the environment. Can be promoted.
[Brief description of the drawings]
FIG. 1 is a cross-sectional view of an apparatus according to a first embodiment of the present invention in a plane including an axis.
FIG. 2 is a sectional view perpendicular to the axis of the apparatus of FIG. 1;
FIG. 3 is a cross-sectional view of a device including a second embodiment of the present invention in a plane including an axis.
FIG. 4 is a cross-sectional view perpendicular to the axis of the apparatus of FIGS. 1 and 2;
FIG. 5 is a cross-sectional view of a device including a third embodiment of the present invention in a plane including an axis.
FIG. 6 is a cross-sectional view of a device including a fourth embodiment of the present invention in a plane including an axis.
FIG. 7 is a sectional view of a device including a fifth embodiment of the present invention in a plane including an axis.
FIG. 8 is a sectional view of a device including a sixth embodiment of the present invention in a plane including an axis.
FIG. 9 is a cross-sectional view taken along a plane including an axis, showing another configuration of the device according to the sixth embodiment of the present invention.
FIG. 10 is a cross-sectional view perpendicular to an axis, showing another configuration of the device according to the sixth embodiment of the present invention.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Axis 2 Cylindrical body 5 Inner cylinder 9 Partition wall 10, 10 'Guide plate 21, 21', 21 "Electric resistance heating element

Claims (6)

A rotatable cylindrical body whose rotation axis is substantially horizontal and has an opening at one end in the axial direction and the other end of which is closed, and which is disposed inside the cylindrical body and substantially has the axis defined by the cylindrical body. An inner cylinder that is shared or parallel and has both ends opened, and an annular space between the cylindrical body and the inner cylinder, an opening-side area and an inner-side area that are separated at an intermediate portion in the axial direction. and substantially parallel partition walls in the axial line divided into a plurality of axial space extending regions axially, at least the opening side region so as to be arranged at intervals in the axial direction have a tilt angle with respect to the axis It has a plurality of guide plates attached to both sides of the partition wall, and the inclination angle of the guide plates is such that when the respective surfaces of the partition wall face upward, the guide plates on the respective surfaces of the partition wall face in opposite directions. None, each edge of a plurality of guide plates arranged in the axial direction is between the inner surface of the cylindrical body At least partially forming a gap plurality of axial space between which is partitioned by the partition wall, in the axial direction, the opening position, are mutually communicated at an intermediate portion position and the rear portion position, said axis A horizontal rotation activation device in which the directional space is provided with a blowing hole for receiving a supply of steam from the outside in the back side region and injecting the steam toward the axial space. The horizontal rotation activation device according to claim 1, wherein the tubular body is provided with a heating device. The horizontal rotation activation device according to claim 2 , wherein the heating device is an electric resistance heating element that receives power supply from outside. The horizontal rotation activation device according to claim 1, wherein the cylindrical body is heated by a combustion gas from the outside. The cylindrical body is housed in the outer cylinder, and the space between the cylindrical body and the outer cylinder forms a heating space through which high-temperature gas flows from the back side region toward the opening side region. Item 5. The horizontal rotation activation device according to Item 4 . 6. The horizontal rotation activation device according to claim 5 , wherein an air inlet for supplying air for cooling from outside to the space between the cylindrical body and the outer cylinder is provided in the outer cylinder.

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