WO2024252937A1 - Multiple-tube type reaction container - Google Patents
Multiple-tube type reaction container Download PDFInfo
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- WO2024252937A1 WO2024252937A1 PCT/JP2024/018990 JP2024018990W WO2024252937A1 WO 2024252937 A1 WO2024252937 A1 WO 2024252937A1 JP 2024018990 W JP2024018990 W JP 2024018990W WO 2024252937 A1 WO2024252937 A1 WO 2024252937A1
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/06—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds in tube reactors; the solid particles being arranged in tubes
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- Patent Document 1 discloses a method in which a heat transfer tube through which a refrigerant flows is provided in a catalyst packed bed, and cooling is performed from the packed bed.
- the activity of the catalyst gradually decreases due to poisoning from impurities in the raw materials and adhesion of the products to the catalyst surface. For this reason, it is common for the catalyst packed in the reactor to be replaced periodically.
- Patent Document 2 discloses a technique in which the tip of a double pipe is cut open, a vacuum pump hose is inserted to suck out the filler, and the pipe is refilled and then welded shut.
- Patent Document 3 discloses a method in which a fluid is fed into a tube filled with a catalyst to flush the filler.
- the method of Patent Document 1 has a problem in that the cooling efficiency is good in the areas close to the heat transfer tubes in the packed bed, but is poor in areas away from the heat transfer tubes, such as near the wall of the packed container.
- the vacuum pump power is used to suck out the catalyst.
- the catalyst since the catalyst is sucked up, the catalyst may fall due to the effect of gravity, and there is a problem that it is difficult to recover all of it.
- the container in the method of Patent Document 2, the container must be cut open prior to recovery of the catalyst, and the cut portion must be welded shut after filling, which is problematic in terms of labor and cost.
- Patent Document 3 also has the problem that it requires power to transport the fluid. Also, when pushing the filler away, depending on the shape of the container, the filler may be trapped structurally, making it impossible to recover the entire amount.
- the present invention was made to solve these problems, and aims to provide a multi-tube reaction vessel that has excellent cooling efficiency and allows easy replacement of the catalyst that is filled inside.
- a multi-tube reaction vessel comprises a catalyst-filled vessel through which a reaction gas flows and which is filled with a catalyst; an inner cooling pipe which penetrates vertically within the catalyst-filled vessel and is arranged to be movable in the vertical direction and through which a cooling fluid flows to cool the catalyst in the catalyst-filled vessel from the inside; and an outer shell vessel which is provided on the outer periphery of the catalyst-filled vessel and through which a cooling fluid flows to cool the catalyst-filled vessel from the outside, the catalyst filling container has a filling port at an upper end surface for filling the catalyst and a discharge port at a lower end surface for discharging the catalyst;
- the inner cooling pipe functions as a plug for opening and closing the outlet of the catalyst filling vessel.
- the catalyst-filled container is cylindrical and the inner cooling pipe is arranged in the center of the catalyst-filled container.
- a catalyst-filled container through which a reaction gas flows and which is filled with a catalyst
- an inner cooling pipe which passes vertically through the catalyst-filled container and is arranged to be movable in the vertical direction and through which a cooling fluid flows to cool the catalyst in the catalyst-filled container from the inside
- an outer shell container which is provided on the outer periphery of the catalyst-filled container and through which a cooling fluid flows to cool the catalyst-filled container from the outside
- the catalyst filling container has a filling port at its upper end surface for filling with catalyst and a discharge port at its lower end surface for discharging the catalyst
- the inner cooling pipe functions as a plug for opening and closing the discharge port of the catalyst filling container, thereby achieving the following effects.
- the catalyst packed bed can be cooled from both the inside and outside, resulting in excellent cooling efficiency.
- the discharge outlet of the catalyst filling container is opened, and the catalyst can be discharged from the discharge outlet by gravity, making it easy to discharge the catalyst.
- the catalyst filling container has a filling port on the upper end surface, it is also easy to refill the catalyst after discharging it, resulting in excellent catalyst replacement work efficiency.
- FIG. 1 is an explanatory diagram of a multi-tube reaction vessel according to an embodiment of the present invention.
- FIG. 2 is an explanatory diagram of a method for discharging a catalyst in the multi-tube reactor shown in FIG. 1 .
- FIG. 2 is an explanatory diagram of a method for replenishing a catalyst in the multi-tube reactor shown in FIG. 1.
- FIG. 2 is an explanatory diagram of another embodiment of a catalyst-filled vessel in the multi-tube reactor shown in FIG. 1 .
- 5A and 5B are detailed explanatory diagrams of the catalyst-filled container shown in FIG. 4, in which FIG. 5(a-1) shows the top surface, FIG. 5(a-2) shows the state in which the lid member 17 has been removed together with the inner cooling pipe 5, and FIG. 5(b) shows the bottom surface.
- a multi-tube reactor 1 As shown in FIG. 1, a multi-tube reactor 1 according to this embodiment includes a catalyst-filled vessel 3, an inner cooling tube 5, and an outer shell vessel 7. Each component will be described in detail below.
- the catalyst-filled vessel 3 is a vessel through which the reaction gas flows and which is filled with a catalyst.
- the catalyst-filled vessel 3 is made of a cylindrical body, but the shape of the vessel 3 is not particularly limited as long as it is cylindrical.
- a gas inlet 9 through which reaction gas enters is provided on the lower side of the catalyst filled container 3, and a gas outlet 11 through which reaction gas (which may contain liquid) is discharged is provided on the upper side of the catalyst filled container 3.
- the catalyst filling container 3 has a filling port 13 at the upper end for filling the catalyst (see Figures 2 and 3), and a discharge port 15 at the lower end for discharging the catalyst, making it possible to discharge the catalyst from the discharge port 15 by gravity. Also, since the catalyst filling container 3 has the filling port 13 on its upper end surface, it is easy to refill the container after discharging the catalyst, and the catalyst replacement work is highly efficient.
- the diameter of the outlet 15 is approximately equal to the outer diameter of the inner cooling pipe 5 when the inner cooling pipe 5 is a straight pipe as shown in Fig. 1. This is to enable the outlet 15 to be closed by the inner cooling pipe 5.
- the diameter of the discharge port 15 may be made slightly smaller than the outer diameter of the portion of the inner cooling pipe 5 located at the discharge port 15.
- the inner cooling pipe 5 passes vertically through the catalyst filled container 3 and is disposed so as to be movable in the vertical direction, and a cooling fluid flows through the inside of the inner cooling pipe 5 to cool the catalyst inside the catalyst filled container 3 .
- the inner cooling pipe 5 is disposed in the center of the catalyst filled vessel 3 .
- the outer diameter of the inner cooling pipe 5 is approximately the same as the diameter of the exhaust port 15, so that when the inner cooling pipe 5 is inserted into the exhaust port 15, the inner cooling pipe 5 functions as a plug to close the exhaust port 15.
- the circumferential surface of the inner cooling pipe 5 is tapered such that the diameter decreases toward the bottom or toward the top (hereinafter referred to as a tapered pipe)
- a tapered pipe it becomes easier to set the outer diameter of the inner cooling pipe 5 and the inner diameter of the outlet 15 than when the inner cooling pipe 5 is a straight pipe, and it becomes easier to make the inner cooling pipe 5 function as a plug that closes the outlet 15.
- a cooling fluid flows from top to bottom, counter flowing to the reaction gas flowing from bottom to top inside the catalyst filled vessel 3.
- the reaction gas and the refrigerant fluid may flow counter to each other, and in some cases, the reaction gas and the refrigerant fluid may flow parallel to each other in order to preferentially cool the superheated section (gas inlet section).
- a lid member 17 is attached to the top of the inner cooling pipe 5 to open and close the filling port 13 at the top of the catalyst filling container 3.
- Cooling fluids include, but are not limited to, air, inert gas, water, seawater, ethylene glycol, etc.
- one inner cooling pipe 5 is arranged inside the catalyst filled container 3, but the present invention is not limited to this, and multiple inner cooling pipes 5 may be arranged inside the catalyst filled container 3. In this way, the cooling efficiency of cooling the catalyst inside the catalyst filled container 3 from the inside can be further improved.
- the outer shell vessel 7 is provided on the outer periphery of the catalyst filled vessel 3 and a cooling fluid flows inside the outer shell vessel 7 to cool the catalyst filled vessel 3 from the outside.
- the outer shell vessel 7 of this embodiment is a cylinder having a larger diameter than the catalyst-filled vessel 3, and is provided with a cooling fluid inlet 19 on the upper side and a cooling fluid outlet 21 on the lower side. Therefore, the flow of the cooling fluid in the outer shell vessel 7 is from top to bottom, similar to the inner cooling pipe 5, and flows counter to the reaction gas.
- the flow directions of the cooling fluid and the reaction gas may be parallel to each other, similar to the relationship between the reaction gas and the cooling fluid described above.
- the catalyst-filled vessel 3 is filled with a catalyst, and a cooling fluid flows through the inner cooling tube 5 and the outer shell vessel 7 .
- reaction heat is generated by the catalytic reaction. This reaction heat is cooled from the inside by the cooling fluid flowing through the inner cooling pipe 5 and from the outside by the cooling fluid flowing through the outer shell vessel 7.
- the heat of the catalytic reaction is cooled from both the inside and the outside, which is very efficient.
- the inner cooling pipe 5 is disposed approximately at the center of the catalyst filled container 3, so that cooling can be performed from the inside without any bias.
- the catalyst filled container 3 is disposed approximately at the center of the outer shell container 7, so that cooling can be performed from the outside without any bias.
- the present invention is not limited to the arrangement in which the inner cooling pipe 5 is disposed at the center of the catalyst filled vessel 3, nor is it limited to the arrangement in which the catalyst filled vessel 3 is disposed at the center of the outer shell vessel 7.
- the catalyst filled container 3 is designed so that the catalyst introduced from the filling port 13 can be discharged from the discharge port 15 by gravity without using any power, and the inner cooling pipe 5 functions as a plug for the discharge port 15 and a cover member 17 is attached to the inner cooling pipe 5. Therefore, as shown in FIG. 2, the catalyst can be discharged by simply pulling out the inner cooling pipe 5. As shown in FIG. 2, the inner cooling pipe 5 does not need to be completely pulled out, but can be moved to a position where the lower end of the inner cooling pipe 5 is above the discharge port 15 to discharge the catalyst. In addition, in the case where the inner cooling pipe 5 is the tapered pipe described above, by moving the inner cooling pipe 5 upward or downward, a gap can be generated between the discharge port 15 and the inner cooling pipe 5, making it possible to discharge the catalyst through the gap.
- the inner cooling tube 5 When filling the catalyst into the catalyst filling container 3 after discharging the catalyst, the inner cooling tube 5 is inserted and the discharge port 15 is closed, and then the catalyst is introduced through the filling port 13, as shown in FIG. 3.
- the cover member 17 can be made movable up and down relative to the inner cooling pipe 5, or, if the cover member 17 is fixed to the inner cooling pipe 5, the length of the inner cooling pipe 5 can be made to have some slack so that it can be in the state shown in Figure 3.
- the catalyst filled in the catalyst filling vessel 3 can be cooled from both the inside and the outside, and therefore the cooling efficiency is excellent.
- the discharge outlet 15 of the catalyst filling container 3 is opened, and the catalyst can be discharged from the discharge outlet 15 by gravity, making it easy to discharge the catalyst and improving the efficiency of catalyst replacement work.
- one pair of catalyst filled container 3 and inner cooling pipe 5 is provided for one outer shell container 7, but the present invention is not limited to this, and multiple pairs of catalyst filled container 3 and inner cooling pipe 5 may be provided for one outer shell container 7.
- the amount of catalyst filled in each catalyst filled container 3 is small, and the thickness of the catalyst in the filled state is thin, so that the cooling efficiency from the inside and outside is improved.
- the above-mentioned catalyst-filled container 3 has the gas inlet 9 provided on the lower side and the gas outlet 11 provided on the upper side.
- the gas inlet 9 may be provided on the bottom surface
- the gas outlet 11 may be provided on the top surface.
- a cutout portion 17a as shown in Fig. 5(a-2) may be provided in the cover member 17.
- a sector-shaped top surface portion 3a supporting the gas outlet port 11 is provided on the top surface of the catalyst-filled container 3 as shown in Figs. 4 and 5(a-1).
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Abstract
Description
反応ガスが通流すると共に触媒が充填される触媒充填容器を備えた反応容器に関し、特に反応容器が多重管になっている多重管式反応容器に関する。 This relates to a reaction vessel equipped with a catalyst-filled vessel through which a reaction gas flows and which is filled with a catalyst, and in particular to a multi-tube reaction vessel in which the reaction vessel has multiple tubes.
触媒反応は多くの場合発熱反応であり、反応器スケールが大きくなると触媒充填層内の異常発熱による反応の暴走や触媒・設備の損傷が懸念されるため、冷却機構が重要である。
例えば、特許文献1では、触媒充填層内に冷媒が流れる伝熱管を設置して充填層から冷却する、という手法が開示されている。
Catalytic reactions are often exothermic, and as the reactor scale increases, there is a concern that abnormal heat generation within the catalyst bed may cause the reaction to go out of control or damage the catalyst and equipment, so a cooling mechanism is important.
For example, Patent Document 1 discloses a method in which a heat transfer tube through which a refrigerant flows is provided in a catalyst packed bed, and cooling is performed from the packed bed.
また、触媒反応は、原料に含まれる不純物による被毒や生成物の触媒表面への付着などにより徐々に触媒の活性が低下してくる。このため、反応器に充填した触媒は定期的に交換されるのが一般的である。 In addition, the activity of the catalyst gradually decreases due to poisoning from impurities in the raw materials and adhesion of the products to the catalyst surface. For this reason, it is common for the catalyst packed in the reactor to be replaced periodically.
触媒の交換方法として、例えば特許文献2では、二重管先端部を切断開口して真空ポンプホースを入れて充填材を吸い出し、再充填後溶接して閉じる、という手法が開示されている。
また、特許文献3では、触媒が充填された管に流体を送って充填物を押し流す、という手法が開示されている。
As a method of replacing a catalyst, for example, Patent Document 2 discloses a technique in which the tip of a double pipe is cut open, a vacuum pump hose is inserted to suck out the filler, and the pipe is refilled and then welded shut.
Furthermore, Patent Document 3 discloses a method in which a fluid is fed into a tube filled with a catalyst to flush the filler.
冷却機構に関し、特許文献1の方法では、充填層内の伝熱管に近い領域の冷却効率は良いが、充填容器壁面近傍など伝熱管から離れた領域は冷却効率が悪いという問題がある。 Regarding the cooling mechanism, the method of Patent Document 1 has a problem in that the cooling efficiency is good in the areas close to the heat transfer tubes in the packed bed, but is poor in areas away from the heat transfer tubes, such as near the wall of the packed container.
また、触媒の交換に関し、特許文献2の方法では、触媒を吸い出す真空ポンプ動力がかかる。また、触媒を吸い上げているため、重力の影響で触媒が落下することもあり、全てを回収するのは難しいという問題がある。
また、特許文献2では、触媒の回収に先立って容器を切断して開放し、充填後には切断部分を溶接して閉じるという作業が必要であり、労力やコストがかかるという問題もある。
In addition, in the method of replacing the catalyst, the vacuum pump power is used to suck out the catalyst. In addition, since the catalyst is sucked up, the catalyst may fall due to the effect of gravity, and there is a problem that it is difficult to recover all of it.
Furthermore, in the method of Patent Document 2, the container must be cut open prior to recovery of the catalyst, and the cut portion must be welded shut after filling, which is problematic in terms of labor and cost.
また、特許文献3の方法では、流体を送るための動力がかかるという問題がある。また、充填物を押し流す場合、容器形状によっては充填材が構造的にトラップされ、全量を回収できないという問題もある。 The method of Patent Document 3 also has the problem that it requires power to transport the fluid. Also, when pushing the filler away, depending on the shape of the container, the filler may be trapped structurally, making it impossible to recover the entire amount.
本発明はかかる課題を解決するためになされたものであり、冷却効率に優れ、充填される触媒の交換が容易な多重管式反応容器を得ることを目的としている。 The present invention was made to solve these problems, and aims to provide a multi-tube reaction vessel that has excellent cooling efficiency and allows easy replacement of the catalyst that is filled inside.
(1)本発明に係る多重管式反応容器は、反応ガスが通流すると共に触媒が充填される触媒充填容器と、前記触媒充填容器内を上下に貫通すると共に上下方向に移動可能に配設されて内部に冷却流体が通流して前記触媒充填容器内の触媒を内側から冷却する内側冷却管と、前記触媒充填容器の外周に設けられて内部に冷却流体が通流して前記触媒充填容器を外側から冷却する外殻容器と、を備え、
前記触媒充填容器は上端面に触媒を充填する充填口を有すると共に下端面に触媒を排出する排出口を有してなり、
前記内側冷却管は、前記触媒充填容器の前記排出口を開閉する栓として機能することを特徴とする特徴とするものである。
(1) A multi-tube reaction vessel according to the present invention comprises a catalyst-filled vessel through which a reaction gas flows and which is filled with a catalyst; an inner cooling pipe which penetrates vertically within the catalyst-filled vessel and is arranged to be movable in the vertical direction and through which a cooling fluid flows to cool the catalyst in the catalyst-filled vessel from the inside; and an outer shell vessel which is provided on the outer periphery of the catalyst-filled vessel and through which a cooling fluid flows to cool the catalyst-filled vessel from the outside,
the catalyst filling container has a filling port at an upper end surface for filling the catalyst and a discharge port at a lower end surface for discharging the catalyst;
The inner cooling pipe functions as a plug for opening and closing the outlet of the catalyst filling vessel.
(2)また、上記(1)に記載のものにおいて、前記触媒充填容器が円筒体からなり前記内側冷却管が前記触媒充填容器の中央に配置されていることを特徴とするものである。 (2) Also, in the above (1), the catalyst-filled container is cylindrical and the inner cooling pipe is arranged in the center of the catalyst-filled container.
(3)また、上記(1)又は(2)に記載のものにおいて、前記触媒充填容器と前記内側冷却管の組を複数組有し、該複数組が一つの外殻容器に設けられていることを特徴とするものである。 (3) Furthermore, in the above (1) or (2), there are multiple sets of the catalyst-filled container and the inner cooling pipe, and the multiple sets are provided in one outer shell container.
本発明においては、反応ガスが通流すると共に触媒が充填される触媒充填容器と、前記触媒充填容器内を上下に貫通すると共に上下方向に移動可能に配設されて内部に冷却流体が通流して前記触媒充填容器内の触媒を内側から冷却する内側冷却管と、前記触媒充填容器の外周に設けられて内部に冷却流体が通流して前記触媒充填容器を外側から冷却する外殻容器と、を備え、
前記触媒充填容器は上端面に触媒を充填する充填口を有すると共に下端面に触媒を排出する排出口を有してなり、前記内側冷却管は、前記触媒充填容器の前記排出口を開閉する栓として機能するようにしたので、以下の効果を奏する。
・触媒充填層を内側と外側の両側から冷却することができるので冷却効率に優れる。
・内側冷却管を上方向に移動することで、触媒充填容器の排出口が開放し、排出口から触媒を重力によって排出することが可能になっているので触媒の排出が容易にでき、また、触媒充填容器の上端面に充填口を有するので触媒排出後の充填も容易であり、触媒交換作業効率に優れる。
In the present invention, a catalyst-filled container through which a reaction gas flows and which is filled with a catalyst is provided, an inner cooling pipe which passes vertically through the catalyst-filled container and is arranged to be movable in the vertical direction and through which a cooling fluid flows to cool the catalyst in the catalyst-filled container from the inside, and an outer shell container which is provided on the outer periphery of the catalyst-filled container and through which a cooling fluid flows to cool the catalyst-filled container from the outside,
The catalyst filling container has a filling port at its upper end surface for filling with catalyst and a discharge port at its lower end surface for discharging the catalyst, and the inner cooling pipe functions as a plug for opening and closing the discharge port of the catalyst filling container, thereby achieving the following effects.
- The catalyst packed bed can be cooled from both the inside and outside, resulting in excellent cooling efficiency.
- By moving the inner cooling pipe upward, the discharge outlet of the catalyst filling container is opened, and the catalyst can be discharged from the discharge outlet by gravity, making it easy to discharge the catalyst.In addition, since the catalyst filling container has a filling port on the upper end surface, it is also easy to refill the catalyst after discharging it, resulting in excellent catalyst replacement work efficiency.
本実施の形態に係る多重管式反応容器1は、図1に示すように、触媒充填容器3と、内側冷却管5と、外殻容器7と、を備えている。
以下、各構成を詳細に説明する。
As shown in FIG. 1, a multi-tube reactor 1 according to this embodiment includes a catalyst-filled vessel 3, an inner cooling tube 5, and an outer shell vessel 7.
Each component will be described in detail below.
<触媒充填容器>
触媒充填容器3は、反応ガスが通流すると共に触媒が充填される容器である。本実施の形態では、図1に示すように、円筒体からなるものであるが、筒状であればその形状は特に限定されない。
触媒充填容器3の下部側面には反応ガスが入るガス導入口9が設けられ、触媒充填容器3の上部側面には反応ガス(液を含む場合あり)が排出されるガス排出口11が設けられている。
<Catalyst filling container>
The catalyst-filled vessel 3 is a vessel through which the reaction gas flows and which is filled with a catalyst. In this embodiment, as shown in Fig. 1, the catalyst-filled vessel 3 is made of a cylindrical body, but the shape of the vessel 3 is not particularly limited as long as it is cylindrical.
A gas inlet 9 through which reaction gas enters is provided on the lower side of the catalyst filled container 3, and a gas outlet 11 through which reaction gas (which may contain liquid) is discharged is provided on the upper side of the catalyst filled container 3.
また、触媒充填容器3は、上端部に触媒を充填する充填口13を有し(図2、図3参照)、下端部に触媒を排出する排出口15を有し、排出口15から触媒を重力によって排出することが可能になっており、また、触媒充填容器3の上端面に充填口13を有するので触媒排出後の充填も容易であり、触媒交換作業効率に優れる。
排出口15の口径は、内側冷却管5が、図1に示すような直管の場合はその外径と略一致している。これは、排出口15を内側冷却管5によって閉止できるようにするためである。そのため、排出口15の周囲にシール部材等を設け、内側冷却管5によって排出口15を封止できるようにするのが好ましい。
なお、内側冷却管5の周面が、下方に向かって又は上方に向かって縮径するテーパー状である場合には、排出口15の口径は、内側冷却管5における排出口15に位置する部位の外径よりもやや小さくすればよい。
In addition, the catalyst filling container 3 has a filling port 13 at the upper end for filling the catalyst (see Figures 2 and 3), and a discharge port 15 at the lower end for discharging the catalyst, making it possible to discharge the catalyst from the discharge port 15 by gravity. Also, since the catalyst filling container 3 has the filling port 13 on its upper end surface, it is easy to refill the container after discharging the catalyst, and the catalyst replacement work is highly efficient.
The diameter of the outlet 15 is approximately equal to the outer diameter of the inner cooling pipe 5 when the inner cooling pipe 5 is a straight pipe as shown in Fig. 1. This is to enable the outlet 15 to be closed by the inner cooling pipe 5. For this reason, it is preferable to provide a seal member or the like around the outlet 15 so that the outlet 15 can be sealed by the inner cooling pipe 5.
In addition, in the case where the peripheral surface of the inner cooling pipe 5 is tapered so that the diameter decreases toward the bottom or toward the top, the diameter of the discharge port 15 may be made slightly smaller than the outer diameter of the portion of the inner cooling pipe 5 located at the discharge port 15.
<内側冷却管>
内側冷却管5は、触媒充填容器3内を上下に貫通すると共に上下方向に移動可能に配設されて内部に冷却流体が通流して触媒充填容器3内の触媒を冷却するものである。
内側冷却管5は、触媒充填容器3の中央に配置されている。
前述したように、内側冷却管5の外径は、排出口15の径と略一致しているので、排出口15に内側冷却管5を挿入したときに、内側冷却管5が排出口15を閉止する栓として機能する。
なお、上述したように、内側冷却管5の周面が、下方に向かって又は上方に向かって縮径するテーパー状である場合(以下、テーパ管という)には、内側冷却管5の外径と排出口15の内径の設定が、内側冷却管5が直観の場合よりも容易となり、内側冷却管5を、排出口15を閉止する栓として機能させやすい。
<Inner cooling pipe>
The inner cooling pipe 5 passes vertically through the catalyst filled container 3 and is disposed so as to be movable in the vertical direction, and a cooling fluid flows through the inside of the inner cooling pipe 5 to cool the catalyst inside the catalyst filled container 3 .
The inner cooling pipe 5 is disposed in the center of the catalyst filled vessel 3 .
As described above, the outer diameter of the inner cooling pipe 5 is approximately the same as the diameter of the exhaust port 15, so that when the inner cooling pipe 5 is inserted into the exhaust port 15, the inner cooling pipe 5 functions as a plug to close the exhaust port 15.
As described above, when the circumferential surface of the inner cooling pipe 5 is tapered such that the diameter decreases toward the bottom or toward the top (hereinafter referred to as a tapered pipe), it becomes easier to set the outer diameter of the inner cooling pipe 5 and the inner diameter of the outlet 15 than when the inner cooling pipe 5 is a straight pipe, and it becomes easier to make the inner cooling pipe 5 function as a plug that closes the outlet 15.
内側冷却管5には、上部から下部に向かって冷却流体が流れ、反応ガスが触媒充填容器3内を下部から上部に向かって流れるのと、対向流れとなっている。なお、この例の様に反応ガスと冷媒流体を対向流にする場合も有れば、過熱部(ガス導入部)を優先的に冷却する効果を狙って反応ガスと冷媒流体を並行流にする場合もある。 In the inner cooling pipe 5, a cooling fluid flows from top to bottom, counter flowing to the reaction gas flowing from bottom to top inside the catalyst filled vessel 3. Note that, as in this example, the reaction gas and the refrigerant fluid may flow counter to each other, and in some cases, the reaction gas and the refrigerant fluid may flow parallel to each other in order to preferentially cool the superheated section (gas inlet section).
内側冷却管5の上部には、触媒充填容器3の上部の充填口13を開閉する蓋部材17が取り付けられている。 A lid member 17 is attached to the top of the inner cooling pipe 5 to open and close the filling port 13 at the top of the catalyst filling container 3.
冷却流体としては、たとえば空気、不活性ガス、水、海水、エチレングリコール等が挙げられるが、これに限定されるものではない。 Cooling fluids include, but are not limited to, air, inert gas, water, seawater, ethylene glycol, etc.
なお、図1に示す例では、触媒充填容器3内に1本の内側冷却管5を配設したものを示しているが、本発明はこれに限定されず、触媒充填容器3内に複数の内側冷却管5を配設するようにしてもよい。このようにすることで、触媒充填容器3内の触媒を内側から冷却する冷却効率をより向上することができる。 In the example shown in FIG. 1, one inner cooling pipe 5 is arranged inside the catalyst filled container 3, but the present invention is not limited to this, and multiple inner cooling pipes 5 may be arranged inside the catalyst filled container 3. In this way, the cooling efficiency of cooling the catalyst inside the catalyst filled container 3 from the inside can be further improved.
<外殻容器>
外殻容器7は、触媒充填容器3の外周に設けられて内部に冷却流体が通流して触媒充填容器3を外側から冷却するものである。
本実施の形態の外殻容器7は、図1に示すように、触媒充填容器3よりも大径の円筒体からなり、上部側面に冷却流体入口19が設けられ、下部側面に冷却流体出口21が設けられている。したがって、外殻容器7の冷却流体の流れは、内側冷却管5と同様に上部から下部となり、反応ガスと対向流となっている。
なお、冷却流体と反応ガスの流れの向きは、上記の反応ガスと冷媒流体の関係と同様に並行流にする場合もある。
<Outer shell container>
The outer shell vessel 7 is provided on the outer periphery of the catalyst filled vessel 3 and a cooling fluid flows inside the outer shell vessel 7 to cool the catalyst filled vessel 3 from the outside.
1, the outer shell vessel 7 of this embodiment is a cylinder having a larger diameter than the catalyst-filled vessel 3, and is provided with a cooling fluid inlet 19 on the upper side and a cooling fluid outlet 21 on the lower side. Therefore, the flow of the cooling fluid in the outer shell vessel 7 is from top to bottom, similar to the inner cooling pipe 5, and flows counter to the reaction gas.
The flow directions of the cooling fluid and the reaction gas may be parallel to each other, similar to the relationship between the reaction gas and the cooling fluid described above.
上記のように構成された多重管式反応容器1においては、触媒充填容器3に触媒が充填され、内側冷却管5及び外殻容器7を冷却流体が流れる。
そして、触媒充填容器3に反応ガスが流れると、触媒反応により反応熱が発生する。この反応熱は、内側冷却管5を流れる冷却流体による内側と、外殻容器7を流れる冷却流体による外側から冷却される。
In the multi-tubular reaction vessel 1 constructed as above, the catalyst-filled vessel 3 is filled with a catalyst, and a cooling fluid flows through the inner cooling tube 5 and the outer shell vessel 7 .
When the reaction gas flows into the catalyst-filled vessel 3, reaction heat is generated by the catalytic reaction. This reaction heat is cooled from the inside by the cooling fluid flowing through the inner cooling pipe 5 and from the outside by the cooling fluid flowing through the outer shell vessel 7.
このように、本実施の形態では、触媒反応熱は内側と外側の両側から冷却されるので、効率がよい。また、内側と外側の両側から冷却可能としたことにより、触媒の温度ムラや、ホットスポット(充填層のごく一部が異常発熱する現象)の出現を抑制することができる。 In this way, in this embodiment, the heat of the catalytic reaction is cooled from both the inside and the outside, which is very efficient. In addition, by being able to cool from both the inside and the outside, it is possible to prevent uneven catalyst temperatures and the occurrence of hot spots (a phenomenon in which a very small part of the packed bed generates abnormal heat).
また、本実施の形態では、内側冷却管5が触媒充填容器3のほぼ中央に配置されているので、偏りなく内側からの冷却が可能である。同様に、触媒充填容器3が外殻容器7のほぼ中央に配置されているので、偏りなく外側からの冷却が可能である。
もっとも、本発明は内側冷却管5を触媒充填容器3の中央に配置するものに限定されず、また触媒充填容器3が外殻容器7の中央に配置されるものにも限定されない。
In this embodiment, the inner cooling pipe 5 is disposed approximately at the center of the catalyst filled container 3, so that cooling can be performed from the inside without any bias. Similarly, the catalyst filled container 3 is disposed approximately at the center of the outer shell container 7, so that cooling can be performed from the outside without any bias.
However, the present invention is not limited to the arrangement in which the inner cooling pipe 5 is disposed at the center of the catalyst filled vessel 3, nor is it limited to the arrangement in which the catalyst filled vessel 3 is disposed at the center of the outer shell vessel 7.
また、本実施の形態では、触媒充填容器3は、充填口13から導入した触媒を排出口15から動力を使うことなく重力によって排出可能になっていると共に、内側冷却管5が排出口15の栓として機能し、内側冷却管5に蓋部材17が取り付けられているので、図2に示すように、内側冷却管5を引き抜くだけで、触媒の排出が可能である。
なお、内側冷却管5は、図2に示すように、完全に引き抜かなくても内側冷却管5の下端が排出口15よりも上になる位置まで移動させれば、触媒の排出は可能である。
また、内側冷却管5が上述したテーパー管の場合には、内側冷却管5を上方又は下方に移動することで、排出口15と内側冷却管5との間に隙間を生じさせて、該隙間から触媒を排出可能とすることもできる。
In addition, in this embodiment, the catalyst filled container 3 is designed so that the catalyst introduced from the filling port 13 can be discharged from the discharge port 15 by gravity without using any power, and the inner cooling pipe 5 functions as a plug for the discharge port 15 and a cover member 17 is attached to the inner cooling pipe 5. Therefore, as shown in FIG. 2, the catalyst can be discharged by simply pulling out the inner cooling pipe 5.
As shown in FIG. 2, the inner cooling pipe 5 does not need to be completely pulled out, but can be moved to a position where the lower end of the inner cooling pipe 5 is above the discharge port 15 to discharge the catalyst.
In addition, in the case where the inner cooling pipe 5 is the tapered pipe described above, by moving the inner cooling pipe 5 upward or downward, a gap can be generated between the discharge port 15 and the inner cooling pipe 5, making it possible to discharge the catalyst through the gap.
触媒を排出後に触媒を触媒充填容器3に充填する場合には、図3に示すように、内側冷却管5を挿入して排出口15を閉じた後、充填口13から導入するようにすればよい。 When filling the catalyst into the catalyst filling container 3 after discharging the catalyst, the inner cooling tube 5 is inserted and the discharge port 15 is closed, and then the catalyst is introduced through the filling port 13, as shown in FIG. 3.
このような操作を可能とするため、蓋部材17を内側冷却管5に対して上下に移動可能にするか、あるいは蓋部材17が内側冷却管5に固定された場合には、内側冷却管5の長さを、図3の状態にできるように、余裕を持たせるようにすればよい。 To enable such an operation, the cover member 17 can be made movable up and down relative to the inner cooling pipe 5, or, if the cover member 17 is fixed to the inner cooling pipe 5, the length of the inner cooling pipe 5 can be made to have some slack so that it can be in the state shown in Figure 3.
以上のように、本実施の形態によれば、触媒充填容器3に充填された触媒を内側と外側の両側から冷却することができるので、冷却効率に優れる。
また、内側冷却管5を上方向に移動することで、触媒充填容器3の排出口15が開放し、排出口15から触媒を重力によって排出することが可能になっているので、触媒の排出が容易にでき、触媒交換作業効率に優れる。
As described above, according to this embodiment, the catalyst filled in the catalyst filling vessel 3 can be cooled from both the inside and the outside, and therefore the cooling efficiency is excellent.
In addition, by moving the inner cooling pipe 5 upward, the discharge outlet 15 of the catalyst filling container 3 is opened, and the catalyst can be discharged from the discharge outlet 15 by gravity, making it easy to discharge the catalyst and improving the efficiency of catalyst replacement work.
上記の例では、一つの外殻容器7に対して、触媒充填容器3と内側冷却管5の組が一つ設けられるものであったが、本発明はこれに限定されるものではなく、一つの外殻容器7に対して触媒充填容器3と内側冷却管5の組が複数設けるようにしてもよい。
この場合において、例えば、図1に示したものと同量の触媒を使用する場合、この態様では各触媒充填容器3に充填する触媒量が少量となり、充填状態における触媒の厚みが薄くなるので、内側及び外側からの冷却効率が向上する。
In the above example, one pair of catalyst filled container 3 and inner cooling pipe 5 is provided for one outer shell container 7, but the present invention is not limited to this, and multiple pairs of catalyst filled container 3 and inner cooling pipe 5 may be provided for one outer shell container 7.
In this case, for example, when using the same amount of catalyst as that shown in Figure 1, in this embodiment, the amount of catalyst filled in each catalyst filled container 3 is small, and the thickness of the catalyst in the filled state is thin, so that the cooling efficiency from the inside and outside is improved.
また、上記の触媒充填容器3は、ガス導入口9が下部側面に設けられ、ガス排出口11が上部側面に設けられたものであったが、図4、図5(b)に示すように、ガス導入口9を底面に設け、また、図4、図5(a-1)に示すように、ガス排出口11を天面に設けるようにしてもよい。
この場合、蓋部材17には、図5(aー2)に示すような切欠き部17aを設けるようにすればよい。このとき触媒充填容器3の天面には、図4、図5(a-1)に示すように、ガス派出口11を支持する扇形形状の天面部3aが設けられることになる。
In addition, the above-mentioned catalyst-filled container 3 has the gas inlet 9 provided on the lower side and the gas outlet 11 provided on the upper side. However, as shown in Figures 4 and 5(b), the gas inlet 9 may be provided on the bottom surface, and as shown in Figures 4 and 5(a-1), the gas outlet 11 may be provided on the top surface.
In this case, a cutout portion 17a as shown in Fig. 5(a-2) may be provided in the cover member 17. In this case, a sector-shaped top surface portion 3a supporting the gas outlet port 11 is provided on the top surface of the catalyst-filled container 3 as shown in Figs. 4 and 5(a-1).
1 多重管式反応容器
3 触媒充填容器
5 内側冷却管
7 外殻容器
9 ガス導入口
11 ガス排出口
13 充填口
15 排出口
17 蓋部材
19 冷却流体入口
21 冷却流体出口
REFERENCE SIGNS LIST 1 multi-tube reaction vessel 3 catalyst-filled vessel 5 inner cooling tube 7 outer vessel 9 gas inlet 11 gas outlet 13 filling port 15 outlet 17 lid member 19 cooling fluid inlet 21 cooling fluid outlet
Claims (3)
前記触媒充填容器は上端面に触媒を充填する充填口を有すると共に下端面に触媒を排出する排出口を有してなり、
前記内側冷却管は、前記触媒充填容器の前記排出口を開閉する栓として機能することを特徴とする特徴とする多重管式反応容器。 a catalyst-filled vessel through which a reaction gas flows and which is filled with a catalyst; an inner cooling pipe which passes vertically through the catalyst-filled vessel and is arranged to be movable in the vertical direction and through which a cooling fluid flows to cool the catalyst in the catalyst-filled vessel from the inside; and an outer shell vessel which is provided on the outer periphery of the catalyst-filled vessel and through which a cooling fluid flows to cool the catalyst in the catalyst-filled vessel from the outside,
the catalyst filling container has a filling port at an upper end surface for filling the catalyst and a discharge port at a lower end surface for discharging the catalyst;
The inner cooling pipe functions as a plug for opening and closing the outlet of the catalyst-filled vessel.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2023095234A JP2024176569A (en) | 2023-06-09 | 2023-06-09 | Multi-tube reaction vessel |
| JP2023-095234 | 2023-06-09 |
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| Publication Number | Publication Date |
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| WO2024252937A1 true WO2024252937A1 (en) | 2024-12-12 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/JP2024/018990 Ceased WO2024252937A1 (en) | 2023-06-09 | 2024-05-23 | Multiple-tube type reaction container |
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| Country | Link |
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| JP (1) | JP2024176569A (en) |
| WO (1) | WO2024252937A1 (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS49125282A (en) * | 1973-04-06 | 1974-11-30 | ||
| JPS6071036A (en) * | 1983-09-29 | 1985-04-22 | ケルンフオルシユングスアンラ−ゲ・ユ−リツヒ・ゲゼルシヤフト・ミト・ベシユレンクテル・ハフツング | Method and apparatus for exchanging catalyst in tubular reactor |
| JPS6320029A (en) * | 1986-07-15 | 1988-01-27 | Mitsubishi Heavy Ind Ltd | reactor |
| JPH05213603A (en) * | 1992-01-31 | 1993-08-24 | Japan Atom Energy Res Inst | Steam reformer |
| JP2005298413A (en) * | 2004-04-13 | 2005-10-27 | Kitakyushu Foundation For The Advancement Of Industry Science & Technology | Highly efficient synthesis method of methanol and apparatus therefor |
-
2023
- 2023-06-09 JP JP2023095234A patent/JP2024176569A/en active Pending
-
2024
- 2024-05-23 WO PCT/JP2024/018990 patent/WO2024252937A1/en not_active Ceased
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS49125282A (en) * | 1973-04-06 | 1974-11-30 | ||
| JPS6071036A (en) * | 1983-09-29 | 1985-04-22 | ケルンフオルシユングスアンラ−ゲ・ユ−リツヒ・ゲゼルシヤフト・ミト・ベシユレンクテル・ハフツング | Method and apparatus for exchanging catalyst in tubular reactor |
| JPS6320029A (en) * | 1986-07-15 | 1988-01-27 | Mitsubishi Heavy Ind Ltd | reactor |
| JPH05213603A (en) * | 1992-01-31 | 1993-08-24 | Japan Atom Energy Res Inst | Steam reformer |
| JP2005298413A (en) * | 2004-04-13 | 2005-10-27 | Kitakyushu Foundation For The Advancement Of Industry Science & Technology | Highly efficient synthesis method of methanol and apparatus therefor |
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| JP2024176569A (en) | 2024-12-19 |
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