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JP4869367B2 - Carbon dioxide recovery device - Google Patents
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JP4869367B2 - Carbon dioxide recovery device - Google Patents

Carbon dioxide recovery device Download PDF

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JP4869367B2
JP4869367B2 JP2009056708A JP2009056708A JP4869367B2 JP 4869367 B2 JP4869367 B2 JP 4869367B2 JP 2009056708 A JP2009056708 A JP 2009056708A JP 2009056708 A JP2009056708 A JP 2009056708A JP 4869367 B2 JP4869367 B2 JP 4869367B2
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carbon dioxide
recovery device
heat transfer
scraping
scraping member
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JP2010208889A (en
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慶太 香川
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Chugoku Electric Power Co Inc
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    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
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    • Y02P20/151Reduction of greenhouse gas [GHG] emissions, e.g. CO2

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Description

本発明は、二酸化炭素を含むガスから効率的に二酸化炭素を回収する二酸化酸素回収装置に関する。   The present invention relates to an oxygen dioxide recovery device that efficiently recovers carbon dioxide from a gas containing carbon dioxide.

一般に、火力発電所や化学プラント等において、石炭、石油又はLNG等の化石燃料を燃焼させることで発生する排ガス中には、多量の二酸化炭素が含まれており、環境面を考慮すると排ガス中に含まれる二酸化炭素を効率的に回収する必要がある。   In general, exhaust gas generated by burning fossil fuels such as coal, oil, or LNG in thermal power plants or chemical plants contains a large amount of carbon dioxide. It is necessary to efficiently recover the contained carbon dioxide.

排ガス中に含まれる二酸化炭素を回収する手法として、排ガス中の二酸化炭素をドライアイスとして固化させて分離する手法が知られている。例えば、特許文献1には、二酸化炭素回収容器の内部に排ガスを供給し、この二酸化炭素回収容器の内部を冷却することで、排ガス中に含まれる二酸化炭素を二酸化炭素回収容器の内面にドライアイスとして付着させる手法が提案されている。   As a technique for recovering carbon dioxide contained in exhaust gas, a technique for solidifying and separating carbon dioxide in exhaust gas as dry ice is known. For example, in Patent Document 1, exhaust gas is supplied to the inside of a carbon dioxide recovery container, and the inside of the carbon dioxide recovery container is cooled so that carbon dioxide contained in the exhaust gas is dried on the inner surface of the carbon dioxide recovery container. A method of adhering is proposed.

特開2007−69057号公報JP 2007-69057 A

しかしながら、特許文献1で対案された手法では、二酸化炭素回収容器の内面に付着したドライアイスを回収するために、二酸化炭素回収容器自体に振動を加えて、この振動により二酸化炭素回収容器に付着したドライアイスを分離させる必要があった。そのため、二酸化炭素回収容器に過度の力が恒常的に加えられることになり、二酸化炭素回収容器が疲労してしまう。そして、このような疲労によって二酸化炭素回収容器の気密性が損なわれて、この二酸化炭素回収容器から排ガスが漏洩するおそれがあった。   However, in the technique proposed in Patent Document 1, in order to recover the dry ice adhering to the inner surface of the carbon dioxide recovery container, the carbon dioxide recovery container itself is vibrated and attached to the carbon dioxide recovery container by this vibration. It was necessary to separate the dry ice. Therefore, excessive force is constantly applied to the carbon dioxide recovery container, and the carbon dioxide recovery container becomes fatigued. And the fatigue | tightness of the carbon dioxide collection container was impaired by such fatigue, and there existed a possibility that exhaust gas might leak from this carbon dioxide collection container.

つまり、従来の手法においては、経年的に二酸化炭素回収容器に振動が加えられる結果、二酸化炭素回収容器が劣化して破損する場合があり、効率的に二酸化炭素の回収を行えなくなってしまうことがある。   In other words, in the conventional method, as a result of vibration applied to the carbon dioxide recovery container over time, the carbon dioxide recovery container may be deteriorated and damaged, and the carbon dioxide cannot be efficiently recovered. is there.

従って、本発明は、排ガスが流入する容器を劣化させることなく、効率的に二酸化炭素を回収できる二酸化炭素回収装置を提供することを目的とする。   Therefore, an object of the present invention is to provide a carbon dioxide recovery device that can efficiently recover carbon dioxide without deteriorating a container into which exhaust gas flows.

(1)本発明は、ガス中に含まれる二酸化炭素を固化させて回収する二酸化炭素回収装置であって、筒状に構成されると共に高さ方向が鉛直方向に沿うように配置され、前記ガスが導入される回収装置本体と、前記回収装置本体の内部に略鉛直方向に延びて配置され、内部を冷媒が流通する伝熱管と、前記伝熱管の周面に付着した固化された二酸化炭素を掻き落とす掻き落とし手段と、前記回収装置本体の下方に配置され前記掻き落とし手段により掻き落とされた固化された二酸化炭素が収容される収容部と、を備え、前記掻き落とし手段は、前記伝熱管の周面に近接して鉛直方向に移動可能な掻き落とし部材と、前記掻き落とし部材を鉛直方向に駆動させる駆動手段と、を備え、前記掻き落とし部材は、前記回収装置本体における水平方向の断面形状と略同形の板状部材により構成され、該板状部材には、前記伝熱管が挿通される伝熱管挿通穴及び前記回収装置本体の内部に導入されたガスが流通するガス流通穴が形成される二酸化炭素回収装置に関する。 (1) The present invention is a carbon dioxide recovery device that solidifies and recovers carbon dioxide contained in a gas, and is configured to have a cylindrical shape and a height direction along a vertical direction. A recovery apparatus main body into which the refrigerant is introduced, a heat transfer pipe that is arranged in the recovery apparatus main body so as to extend in a substantially vertical direction, and in which the refrigerant flows, and solidified carbon dioxide adhering to the peripheral surface of the heat transfer pipe Scraping means for scraping off, and an accommodating portion for storing the solidified carbon dioxide disposed below the recovery apparatus main body and scraped off by the scraping means , wherein the scraping means is the heat transfer tube. A scraping member that is movable in the vertical direction in the vicinity of the peripheral surface, and a drive unit that drives the scraping member in the vertical direction. The scraping member is a horizontal direction in the recovery device main body. The plate-shaped member has a heat transfer tube insertion hole through which the heat transfer tube is inserted and a gas flow hole through which the gas introduced into the recovery device main body flows. It relates to a carbon dioxide recovery device to be formed .

(1)に記載の二酸化炭素回収装置によれば、伝熱管に付着し固化した二酸化炭素を掻き落として収容部に回収するようにしたので、回収装置本体に振動を加える必要がない。よって、疲労等によって回収装置本体の気密性が損なわれることがなく、効率的に二酸化炭素の回収を行える。   According to the carbon dioxide recovery device described in (1), the carbon dioxide that has adhered to the heat transfer tube and solidified is scraped off and recovered in the accommodating portion, so there is no need to apply vibration to the recovery device body. Therefore, the carbon dioxide can be efficiently recovered without impairing the airtightness of the recovery device body due to fatigue or the like.

)に記載の二酸化炭素回収装置によれば、掻き落とし部材を、伝熱管の周面に近接して鉛直方向に移動可能に配置し、この掻き落とし部材を鉛直方向に駆動させた。よって、伝熱管に付着し固化した二酸化炭素を容易にしかも効率的に掻き落とすことができる。 According to the carbon dioxide recovery device described in ( 1 ), the scraping member is disposed so as to be movable in the vertical direction in the vicinity of the peripheral surface of the heat transfer tube, and the scraping member is driven in the vertical direction. Therefore, the carbon dioxide adhered to the heat transfer tube and solidified can be easily and efficiently scraped off.

)に記載の二酸化炭素回収装置によれば、掻き落とし部材を、回収装置本体における水平方向の断面形状と略同形の板状部材によって構成し、板状部材に伝熱管が挿通される伝熱管挿通穴及び回収装置本体の内部に導入されたガスが流通するガス流通穴を形成した。これにより、掻き落とし部材を、伝熱管をガイドとしつつ、伝熱管に付着し固化した二酸化炭素を良好に掻き落とすことができる。また、ガス流通穴を通ってガスが流通するから、ガスによって掻き落とし部材の移動が損なわれることがない。 According to the carbon dioxide recovery device described in ( 1 ), the scraping member is configured by a plate-like member that is substantially the same shape as the horizontal cross-sectional shape of the recovery device body, and the heat transfer tube is inserted through the plate-like member. A gas flow hole through which the gas introduced into the heat pipe insertion hole and the inside of the recovery apparatus main body flows was formed. Thereby, the carbon dioxide which adhered to the heat exchanger tube and solidified can be scraped off favorably, using the scraper member as a guide for the heat exchanger tube. Further, since the gas flows through the gas flow hole, the movement of the scraping member is not impaired by the gas.

)本発明は、()に記載の二酸化炭素回収装置において、前記駆動手段は、前記回収装置本体の上面を貫通して配置されるシリンダと、該シリンダに摺動可能に収容され先端側が前記掻き落とし部材に連結されるピストンとを備えるものである。 ( 2 ) The present invention provides the carbon dioxide recovery device according to ( 1 ), wherein the driving means includes a cylinder disposed through the upper surface of the recovery device main body, and a tip slidably accommodated in the cylinder. The side is provided with a piston connected to the scraping member.

)に記載の二酸化炭素回収装置によれば、駆動手段を、回収装置本体の上面を貫通して配置されるシリンダと、このシリンダに摺動可能に収容され先端側が掻き落とし部材に連結されるピストンとにより構成した。よって、簡単な機構で掻き落とし部材を鉛直方向に駆動させられる。 According to the carbon dioxide recovery device described in ( 2 ), the driving means includes a cylinder disposed through the upper surface of the recovery device body, and is slidably accommodated in the cylinder, and the tip side is coupled to the scraping member. And a piston. Therefore, the scraping member can be driven in the vertical direction with a simple mechanism.

)本発明は、(1)又は(2)のいずれかに記載の二酸化炭素回収装置において、前記収容部は、複数の収容容器により構成され、前記回収装置本体の底面側には、前記複数の収容容器のうちの所定の収容容器に固化された二酸化炭素を供給する切替手段が設けられるものである。 ( 3 ) The present invention provides the carbon dioxide recovery device according to any one of (1) and (2 ), wherein the storage portion is configured by a plurality of storage containers, Switching means for supplying solidified carbon dioxide to a predetermined storage container among the plurality of storage containers is provided.

)に記載の二酸化炭素回収装置によれば、収容部を、複数の収容容器で構成し、回収装置本体の底面側に、複数の収容容器のうちの所定の収容容器に固化された二酸化炭素を供給する切替手段を設けた。よって、必要に応じて収容容器を選択することができ、二酸化炭素の回収中においても、使用していない収容容器のメンテナンスを行える。 According to the carbon dioxide recovery device described in ( 3 ), the storage unit is configured with a plurality of storage containers, and the carbon dioxide solidified into a predetermined storage container among the plurality of storage containers is formed on the bottom surface side of the recovery device body. Switching means for supplying carbon was provided. Therefore, the storage container can be selected as necessary, and maintenance of unused storage containers can be performed even during the recovery of carbon dioxide.

)本発明は、()に記載の二酸化炭素回収装置において、前記複数の収容容器それぞれは、密閉性及び耐圧性を有する容器により構成されるものである。 ( 4 ) According to the present invention, in the carbon dioxide recovery device described in ( 3 ), each of the plurality of storage containers is configured by a container having airtightness and pressure resistance.

)に記載の二酸化炭素回収装置によれば、収容容器の各々が密閉性及び耐圧性を有しているので、固化した二酸化炭素を加圧することなく大気圧で放置すれば、自然に温度が上昇し、固化した二酸化炭素は液体となって、液体二酸化炭素として貯蔵できる。 According to the carbon dioxide recovery device described in ( 4 ), since each of the storage containers has hermeticity and pressure resistance, if the solidified carbon dioxide is left at atmospheric pressure without pressurization, the temperature naturally increases. The solidified carbon dioxide becomes liquid and can be stored as liquid carbon dioxide.

)本発明は、(1)又は(2)に記載の二酸化炭素回収装置において、前記掻き落とし部材を前記回収装置本体における所定の待機位置と該待機位置よりも下側に位置する駆動位置との間で移動させるように前記駆動手段を制御する制御手段を更に備えるものである。 ( 5 ) The present invention provides the carbon dioxide recovery device according to (1) or (2 ) , wherein the scraping member is a predetermined standby position in the recovery device main body and a drive position positioned below the standby position. Control means for controlling the driving means so as to be moved between the two.

)に記載の二酸化炭素回収装置によれば、掻き落とし部材を所定の待機位置と駆動位置との間で移動させるようにした。よって、伝熱管に付着し固化した二酸化炭素を簡単に掻き落とすことができる。 According to the carbon dioxide recovery device described in ( 5 ), the scraping member is moved between the predetermined standby position and the drive position. Therefore, carbon dioxide adhering to the heat transfer tube and solidified can be easily scraped off.

)本発明は、()に記載の二酸化炭素回収装置において、前記制御手段は、前記掻き落とし部材を所定の時間間隔で移動させると共に、前記待機位置から前記駆動位置に前記掻き落とし部材を駆動させた後、直ちに前記掻き落とし部材を前記駆動位置から前記待機位置に復帰させるよう前記駆動手段を制御するものである。 ( 6 ) In the carbon dioxide recovery device according to ( 5 ), the control unit moves the scraping member at a predetermined time interval and moves the scraping member from the standby position to the driving position. Immediately after driving, the drive means is controlled so that the scraping member is returned from the drive position to the standby position.

)に記載の二酸化炭素回収装置によれば、掻き落とし部材を所定の時間間隔で移動させ、待機位置から駆動位置に掻き落とし部材を駆動させた後、直ちに掻き落とし部材を駆動位置から待機位置に復帰させるように駆動手段を制御した。よって、掻き落とし部材が復帰する際には、伝熱管に二酸化炭素が付着していることがほとんどないから、二酸化炭素の回収に支障を来たすおそれがない。 According to the carbon dioxide recovery device described in ( 6 ), the scraping member is moved at a predetermined time interval, and after the scraping member is driven from the standby position to the driving position, the scraping member is immediately standby from the driving position. The drive means was controlled to return to the position. Therefore, when the scraping member returns, carbon dioxide is hardly attached to the heat transfer tube, so that there is no possibility of hindering the collection of carbon dioxide.

本発明によれば、伝熱管に付着し固化した二酸化炭素を掻き落として収容部に回収するようにしたので、回収装置本体に振動を加える必要がない。よって、疲労等によって回収装置本体の気密性が損なわれることがなく、効率的に二酸化炭素の回収を行える。   According to the present invention, carbon dioxide that has adhered to the heat transfer tube and solidified is scraped off and collected in the accommodating portion, so there is no need to apply vibration to the collection device body. Therefore, the carbon dioxide can be efficiently recovered without impairing the airtightness of the recovery device body due to fatigue or the like.

本発明の二酸化炭素回収装置の一実施形態を示す斜視図である。It is a perspective view showing one embodiment of a carbon dioxide recovery device of the present invention. 図1に示す二酸化炭素回収装置において、掻き落とし部材が待機位置にある状態を一部破断して概略的に示す図である。In the carbon dioxide recovery device shown in FIG. 1, it is a diagram schematically showing a state in which a scraping member is in a standby position with a part broken away. 図1に示す二酸化炭素回収装置において、掻き落とし部材が待機位置と駆動位置との間に位置する状態を一部破断して概略的に示す図である。FIG. 2 is a diagram schematically showing a state in which the scraping member is positioned between a standby position and a drive position in a partially broken state in the carbon dioxide recovery apparatus shown in FIG. 1. 図1に示す二酸化炭素回収装置において、掻き落とし部材が駆動位置にある状態を一部破断して概略的に示す図である。FIG. 2 is a diagram schematically showing a state in which the scraping member is in a driving position with a part broken away in the carbon dioxide recovery device shown in FIG. 1. 本二酸化炭素回収装置で用いられる掻き落とし部材の他の例を示す図である。It is a figure which shows the other example of the scraping member used with this carbon dioxide recovery apparatus.

以下、本発明の二酸化炭素回収装置の好ましい一実施形態について図面を参照ながら説明する。   Hereinafter, a preferred embodiment of the carbon dioxide recovery device of the present invention will be described with reference to the drawings.

図1は本発明の二酸化炭素回収装置10の一実施形態を示す斜視図である。
二酸化炭素回収装置10は、例えば、石炭、石油又はLNG等を燃料として用いる火力発電所で用いられ、当該火力発電所からの排ガス中に含まれる二酸化炭素を固化させて回収する。
FIG. 1 is a perspective view showing an embodiment of the carbon dioxide recovery apparatus 10 of the present invention.
The carbon dioxide recovery device 10 is used in, for example, a thermal power plant that uses coal, petroleum, LNG, or the like as a fuel, and solidifies and recovers carbon dioxide contained in exhaust gas from the thermal power plant.

二酸化炭素回収装置10は、回収装置本体11と、この回収装置本体11の内部に配置される伝熱管14と、掻き落とし手段を構成する掻き落とし部材17及びこの掻き落とし部材17を駆動させる駆動手段としての駆動装置18と、この駆動装置18を制御する制御手段としての制御装置30と、回収装置本体11の底面側に設けられる切替手段としての切替装置26と、回収装置本体11の下方に配置される収容部19と、を備える。   The carbon dioxide recovery device 10 includes a recovery device main body 11, a heat transfer tube 14 disposed inside the recovery device main body 11, a scraping member 17 constituting scraping means, and a driving means for driving the scraping member 17. A drive device 18 as a control device, a control device 30 as a control means for controlling the drive device 18, a switching device 26 as a switching means provided on the bottom side of the recovery device main body 11, and a lower portion of the recovery device main body 11. And an accommodating portion 19 to be provided.

回収装置本体11は、鉛直方向に沿って延びる円筒形状を有している(つまり、回収装置本体11は、その高さが鉛直方向に沿うように配置されている)。
回収装置本体11の上端近傍における側面には、排ガス導入管12が連結され、回収装置本体11の下端近傍における側面には排ガス導出管13が連結されている。排ガス導入管12から回収装置本体11の内部に導入された排ガスは、二酸化炭素が取り除かれた二酸化炭素除去排ガス(以下、単に除去排ガスと呼ぶ)として排ガス導出管13から導出される。
The collection device main body 11 has a cylindrical shape extending along the vertical direction (that is, the collection device main body 11 is arranged so that its height is along the vertical direction).
An exhaust gas introduction pipe 12 is connected to a side surface in the vicinity of the upper end of the recovery apparatus main body 11, and an exhaust gas outlet pipe 13 is connected to a side surface in the vicinity of the lower end of the recovery apparatus main body 11. The exhaust gas introduced into the recovery apparatus main body 11 from the exhaust gas introduction pipe 12 is led out from the exhaust gas outlet pipe 13 as carbon dioxide-removed exhaust gas from which carbon dioxide has been removed (hereinafter simply referred to as removed exhaust gas).

伝熱管14は、回収装置本体11の内部に複数本配置されている。これら複数本の伝熱管14は、回収装置本体11の内部においては、略鉛直方向に延びている。伝熱管14の内部には、液体窒素等の冷媒が流通する。なお、これら伝熱管14は、回収装置本体11の中心軸を中心として、等角度間隔で配列することが好ましい。   A plurality of heat transfer tubes 14 are arranged inside the recovery apparatus main body 11. The plurality of heat transfer tubes 14 extend in a substantially vertical direction inside the recovery apparatus main body 11. A refrigerant such as liquid nitrogen circulates inside the heat transfer tube 14. The heat transfer tubes 14 are preferably arranged at equiangular intervals with the central axis of the recovery device body 11 as the center.

伝熱管14の下端側は、図1に示すように、放射状に径方向外側に延び、回収装置本体11の側面を貫通して、環状の連結管15に接続されている。そして、連結管15を介して伝熱管14に、前述の冷媒が導入される。一方、伝熱管14の上端側は、回収装置本体11の上面を貫通して、環状の連結管16に接続されている。そして、伝熱管14の内部を流通する冷媒は、連結管16を介して導出される。つまり、冷媒は連結管15、伝熱管14、及び連結管16を通って流れ、冷却装置(図示せず)で再度所定の温度(例えば、−110℃〜−120℃:この温度は二酸化炭素が固化されてドライアイスとなる温度である)に冷却され、再び連結管15から伝熱管14に導入される。   As shown in FIG. 1, the lower end side of the heat transfer tube 14 extends radially outward, passes through the side surface of the recovery device main body 11, and is connected to an annular connecting tube 15. Then, the aforementioned refrigerant is introduced into the heat transfer tube 14 via the connecting tube 15. On the other hand, the upper end side of the heat transfer tube 14 passes through the upper surface of the recovery device main body 11 and is connected to the annular connecting tube 16. And the refrigerant | coolant which distribute | circulates the inside of the heat exchanger tube 14 is derived | led-out via the connection pipe 16. FIG. That is, the refrigerant flows through the connecting pipe 15, the heat transfer pipe 14, and the connecting pipe 16, and again at a predetermined temperature (for example, −110 ° C. to −120 ° C .: this temperature is generated by carbon dioxide) in a cooling device (not shown). It is cooled to a temperature at which it becomes solidified and becomes dry ice), and is again introduced into the heat transfer tube 14 from the connecting tube 15.

掻き落とし部材17は、回収装置本体11の水平方向断面形状と略同形の円形板状部材である。この掻き落とし部材17には、複数本の伝熱管14が挿通される複数の伝熱管挿通穴20と、回収装置本体11の内部に導入された排ガスが流通する複数のガス流通穴21とが形成されている。複数の伝熱管挿通穴20の内周面と伝熱管14の外周面との間には、適度なクリアランス(例えば、1mm〜3mm)が形成されている。すなわち、複数の伝熱管挿通穴20の内周面は、伝熱管14の外周面に近接して配置されている。複数のガス流通穴21は、掻き落とし部材17の中心から略同心円上に、略等間隔で設けられている。   The scraping member 17 is a circular plate-like member having substantially the same shape as the horizontal sectional shape of the recovery apparatus main body 11. The scraping member 17 is formed with a plurality of heat transfer tube insertion holes 20 through which the plurality of heat transfer tubes 14 are inserted, and a plurality of gas flow holes 21 through which the exhaust gas introduced into the recovery device main body 11 flows. Has been. An appropriate clearance (for example, 1 mm to 3 mm) is formed between the inner peripheral surface of the plurality of heat transfer tube insertion holes 20 and the outer peripheral surface of the heat transfer tube 14. That is, the inner peripheral surfaces of the plurality of heat transfer tube insertion holes 20 are arranged close to the outer peripheral surface of the heat transfer tube 14. The plurality of gas flow holes 21 are provided at substantially equal intervals on a substantially concentric circle from the center of the scraping member 17.

駆動装置18は、掻き落とし部材17を鉛直方向に沿って駆動させる。この駆動装置18は、シリンダ22と、このシリンダ22に摺動可能に収容されるピストン23と、を備える。シリンダ22は、回収装置本体11の上面を貫通して配置されている。ピストン23の先端側は、掻き落とし部材17に連結されている。この駆動装置18によれば、シリンダ22内に流体が供給されると、ピストン23は鉛直方向下方に移動する。これにより、掻き落とし部材17は、鉛直方向下方に移動する。また、シリンダ22内から流体が排出されると、ピストン23は鉛直方向上方に移動する。これにより、掻き落とし部材17は、鉛直方向上方に移動する。   The driving device 18 drives the scraping member 17 along the vertical direction. The drive device 18 includes a cylinder 22 and a piston 23 slidably accommodated in the cylinder 22. The cylinder 22 is disposed so as to penetrate the upper surface of the recovery apparatus main body 11. The tip end side of the piston 23 is connected to the scraping member 17. According to this drive device 18, when fluid is supplied into the cylinder 22, the piston 23 moves downward in the vertical direction. As a result, the scraping member 17 moves downward in the vertical direction. When the fluid is discharged from the cylinder 22, the piston 23 moves upward in the vertical direction. As a result, the scraping member 17 moves upward in the vertical direction.

収容部19は、複数の収容容器24,25を備えて構成される。これら収容容器24,25は、掻き落とし部材17により掻き落とされた固化された二酸化炭素を収容する。収容容器24,25のそれぞれは、密閉性及び耐圧性を有している。収容容器24,25には、それぞれ開閉弁27,28が設けられている。これら開閉弁27,28の開閉操作により収容容器24,25の内部に収容された二酸化炭素は、配管を通って導出される。   The accommodating part 19 includes a plurality of accommodating containers 24 and 25. The storage containers 24 and 25 store the solidified carbon dioxide scraped off by the scraping member 17. Each of the storage containers 24 and 25 has airtightness and pressure resistance. The storage containers 24 and 25 are provided with on-off valves 27 and 28, respectively. The carbon dioxide stored in the storage containers 24 and 25 by the opening and closing operation of these on-off valves 27 and 28 is led out through the piping.

切替装置26は、掻き落とし部材17により掻き落とされた固化された二酸化炭素を、複数の収容容器24,25のうちの所定の収容容器に選択的に供給する。   The switching device 26 selectively supplies the solidified carbon dioxide scraped off by the scraping member 17 to a predetermined storage container among the plurality of storage containers 24, 25.

制御装置30は、駆動装置18を制御して、掻き落とし部材17を回収装置本体11における上方側の待機位置A(図2参照)と、この待機位置Aよりも下側に位置する駆動位置B(図4参照)との間で移動させる(図2参照)。
また、制御装置30は、駆動装置18を制御して、掻き落とし部材17を所定の時間間隔で移動させると共に、待機位置から駆動位置に前記掻き落とし部材17を駆動させた後、直ちに掻き落とし部材17を駆動位置から待機位置に復帰させる。
The control device 30 controls the drive device 18 so that the scraping member 17 is placed on the upper standby position A (see FIG. 2) of the recovery device main body 11 and the drive position B located below the standby position A. (See FIG. 4).
In addition, the control device 30 controls the driving device 18 to move the scraping member 17 at a predetermined time interval, and after driving the scraping member 17 from the standby position to the driving position, the scraping member immediately. 17 is returned from the drive position to the standby position.

次に、本実施形態の二酸化炭素回収装置10の動作について、図2〜図4を参照しながら(なお、図2〜図4においては、制御装置30等は省略されている)説明する。
先ず、駆動装置18を駆動させて、掻き落とし部材17を、排ガス導入管12の取り付け位置よりも僅かに下側の所定の位置である待機位置Aに位置させる。
この状態で、回収装置本体11の内部には、排ガス導入管12を介して二酸化炭素を含む排ガスが供給される。回収装置本体11の内部に導入された排ガス中に含まれる二酸化炭素は、伝熱管14の内部を流通する冷媒によって冷却され、伝熱管14の表面で固化しドライアイスとなって付着する(図2参照)。二酸化炭素が除去された除去排ガスは、排ガス導出管13を介して外部に排出される。
Next, the operation of the carbon dioxide recovery apparatus 10 of the present embodiment will be described with reference to FIGS.
First, the driving device 18 is driven, and the scraping member 17 is positioned at a standby position A that is a predetermined position slightly below the attachment position of the exhaust gas introduction pipe 12.
In this state, exhaust gas containing carbon dioxide is supplied into the recovery apparatus main body 11 through the exhaust gas introduction pipe 12. The carbon dioxide contained in the exhaust gas introduced into the inside of the recovery apparatus main body 11 is cooled by the refrigerant circulating in the heat transfer tube 14, solidifies on the surface of the heat transfer tube 14, and adheres as dry ice (FIG. 2). reference). The removed exhaust gas from which carbon dioxide has been removed is discharged to the outside through the exhaust gas outlet pipe 13.

制御装置30は、予め設定された時間間隔で駆動装置18を駆動制御する。すなわち、制御装置30は、シリンダ22内に流体を供給して、ピストン23を鉛直方向下方に移動させる。これにより、掻き落とし部材17は、駆動位置Bまで鉛直方向下方に移動する(図3及び図4参照)。ここで、伝熱管14の表面側には、適度なクリアランスをあけて伝熱管挿通穴20の内周面が位置しているから、伝熱管14の表面に付着したドライアイスは、掻き落とし部材17の下向きへの移動によって、伝熱管14の表面から掻き落とされて、下方に落下する。
また、制御装置30は、掻き落とし部材17が駆動位置Bに到達すると、直ちに、シリンダ22内から流体を排出させてピストン23を鉛直方向上方に移動させる。これにより、掻き落とし部材17は、鉛直方向上方に移動して待機位置Aに復帰する。ここで、制御装置30は、掻き落とし部材17が駆動位置Bに到達すると、直ちに掻き落とし部材17を待機位置Aまで復帰させるので、掻き落とし部材17が駆動位置Bから待機位置Aに復帰するときには、伝熱管14の表面にはドライアイスは付着しない。
The control device 30 drives and controls the drive device 18 at a preset time interval. That is, the control device 30 supplies fluid into the cylinder 22 and moves the piston 23 downward in the vertical direction. As a result, the scraping member 17 moves downward in the vertical direction to the drive position B (see FIGS. 3 and 4). Here, since the inner peripheral surface of the heat transfer tube insertion hole 20 is located on the surface side of the heat transfer tube 14 with an appropriate clearance, the dry ice attached to the surface of the heat transfer tube 14 is scraped off by the scraping member 17. Due to the downward movement, it is scraped off from the surface of the heat transfer tube 14 and falls downward.
Further, when the scraping member 17 reaches the drive position B, the control device 30 immediately discharges the fluid from the cylinder 22 and moves the piston 23 upward in the vertical direction. As a result, the scraping member 17 moves upward in the vertical direction and returns to the standby position A. Here, when the scraping member 17 reaches the driving position B, the control device 30 immediately returns the scraping member 17 to the standby position A. Therefore, when the scraping member 17 returns from the driving position B to the standby position A, The dry ice does not adhere to the surface of the heat transfer tube 14.

制御装置30は、タイマー(図示せず)を内蔵しており、所定の時間間隔で駆動装置18に上述の処理を実行させる。   The control device 30 has a built-in timer (not shown), and causes the drive device 18 to execute the above-described processing at predetermined time intervals.

回収装置本体11の底面側に落下したドライアイスは、切替装置26に達し、ここで収容容器24又は25に振り分けられる。例えば、収容容器24及び25に貯蔵されたドライアイスの量に応じて、切替装置26は、ドライアイスを収容容器24又は25に供給し、収容容器24及び25に貯蔵されるドライアイスの量が不均一とならないようにする。   The dry ice that has fallen to the bottom surface side of the recovery device main body 11 reaches the switching device 26 and is distributed to the storage container 24 or 25 here. For example, according to the amount of dry ice stored in the storage containers 24 and 25, the switching device 26 supplies the dry ice to the storage containers 24 or 25, and the amount of dry ice stored in the storage containers 24 and 25 is reduced. Avoid unevenness.

収容容器24,25は、密閉性及び耐圧性を有する容器により構成されている。これにより、収容容器24,25内に収容されたドライアイスは、収容容器24,25内部の温度上昇により、液体二酸化炭素となった状態で保管される。   The storage containers 24 and 25 are constituted by containers having airtightness and pressure resistance. Thereby, the dry ice accommodated in the storage containers 24 and 25 is stored in a state of liquid carbon dioxide due to the temperature rise inside the storage containers 24 and 25.

以上の二酸化炭素回収装置10によれば、以下のような効果を奏する。   According to the carbon dioxide recovery device 10 described above, the following effects can be obtained.

排ガス中に含まれる二酸化炭素を、伝熱管14の表面にドライアイスとして付着させ、掻き落とし部材を伝熱管14に沿って移動させて、伝熱管14の表面に付着したドライアイスを掻き落として収容容器24,25に回収させた。これにより、回収装置本体11に振動が加えることなく、二酸化炭素を回収できるので、回収装置本体11が疲労しない。つまり、疲労によって回収装置本体11の気密性が損なわれて、回収装置本体11から排ガスが漏洩することはない。その結果、常に効率的に二酸化炭素の回収を行うことができる。   The carbon dioxide contained in the exhaust gas is attached to the surface of the heat transfer tube 14 as dry ice, and the scraping member is moved along the heat transfer tube 14 to scrape and store the dry ice attached to the surface of the heat transfer tube 14. The containers 24 and 25 were collected. Thereby, since the carbon dioxide can be recovered without applying vibration to the recovery device main body 11, the recovery device main body 11 is not fatigued. That is, the airtightness of the recovery apparatus main body 11 is not impaired by fatigue, and the exhaust gas does not leak from the recovery apparatus main body 11. As a result, carbon dioxide can always be efficiently recovered.

また、掻き落とし部材17には、ガス流通穴21を形成した。これにより、掻き落とし部材17が伝熱管14をガイドとして鉛直方向に移動する際に、回収装置本体11に導入された排ガスは、ガス流通穴21を通って流通する。よって、回収装置本体11に導入された排ガスによって掻き落とし部材17の移動が損なわれることはがない。   Further, a gas flow hole 21 was formed in the scraping member 17. Thereby, when the scraping member 17 moves in the vertical direction using the heat transfer tube 14 as a guide, the exhaust gas introduced into the recovery apparatus main body 11 flows through the gas flow hole 21. Therefore, the movement of the scraping member 17 is not impaired by the exhaust gas introduced into the recovery apparatus main body 11.

また、収容容器24,25を密閉性及び耐圧性を有する容器により構成した。これにより、収容容器24,25内に収容されたドライアイスは、収容容器24,25内部の温度上昇により、液体二酸化炭素となった状態で保管される。よって、回収した二酸化炭素を配管により容易に移送できるので、当該液体二酸化炭素を別に冷媒として使用することもできる。   In addition, the storage containers 24 and 25 are constituted by containers having airtightness and pressure resistance. Thereby, the dry ice accommodated in the storage containers 24 and 25 is stored in a state of liquid carbon dioxide due to the temperature rise inside the storage containers 24 and 25. Therefore, since the recovered carbon dioxide can be easily transferred by piping, the liquid carbon dioxide can be used as a refrigerant separately.

以上、本発明の実施形態について説明したが、本発明は上述した実施形態に限るものではない。また、本発明の実施形態に記載された効果は、本発明から生じる最も好適な効果を列挙したに過ぎず、本発明による効果は、本発明の実施例に記載されたものに限定されるものではない。   As mentioned above, although embodiment of this invention was described, this invention is not restricted to embodiment mentioned above. The effects described in the embodiments of the present invention are only the most preferable effects resulting from the present invention, and the effects of the present invention are limited to those described in the embodiments of the present invention. is not.

例えば、本実施形態では、掻き落とし部材17として円板形状のものを用いたが、掻き落とし部材17はこれに限られることなく、伝熱管14の表面に付着したドライアイスを効果的に掻き落とすことのできるものであれば、他の形状でもよい。   For example, in the present embodiment, a disc-shaped member is used as the scraping member 17, but the scraping member 17 is not limited to this, and effectively scrapes dry ice adhering to the surface of the heat transfer tube 14. Other shapes are possible as long as they can be used.

すなわち、図5に示すように、掻き落とし部材17が複数のパイプ体17aを有し、伝熱管14のそれぞれをパイプ体17aに一対一で挿通する。掻き落とし部材17は、例えば、回収装置本体11の中心軸上に位置する連結体(小円板状)17bを備え、この連結体17bにパイプ体17aがそれぞれリンク部材17cによって連結される。そして、ピストン23の先端が連結体17bに連結されて、駆動装置18によって、連結体17b、つまり、パイプ体17aを鉛直方向に移動し、伝熱管14の表面に付着したドライアイスを掻き落とす。   That is, as shown in FIG. 5, the scraping member 17 has a plurality of pipe bodies 17a, and each of the heat transfer tubes 14 is inserted into the pipe body 17a on a one-to-one basis. The scraping member 17 includes, for example, a connecting body (small disc shape) 17b positioned on the central axis of the recovery apparatus main body 11, and the pipe bodies 17a are connected to the connecting body 17b by link members 17c, respectively. And the front-end | tip of piston 23 is connected with the connection body 17b, the drive body 18 moves the connection body 17b, ie, the pipe body 17a, in the vertical direction, and scrapes off the dry ice adhering to the surface of the heat exchanger tube 14.

また、本実施形態では、駆動装置18をシリンダ22及びピストンにより構成したが、これに限らない。すなわち、駆動装置18を、回収装置本体11の外周面に配置した磁石により構成してもよい。この場合には、掻き落とし部材を磁性部材により構成し、外周面に配置した磁石を上下方向に移動させることで掻き落とし部材を移動させられる。   Moreover, in this embodiment, although the drive device 18 was comprised with the cylinder 22 and the piston, it is not restricted to this. That is, the drive device 18 may be configured by a magnet disposed on the outer peripheral surface of the collection device main body 11. In this case, the scraping member is made of a magnetic member, and the scraping member can be moved by moving the magnet disposed on the outer peripheral surface in the vertical direction.

また、本実施形態では、複数の伝熱管挿通穴20の内周面と伝熱管14の外周面との間に、適度なクリアランスを形成したが、これに限らない。すなわち、複数の伝熱管挿通穴の内周面と伝熱管の外周面とを接触させてもよい。この場合、伝熱管挿通穴の内周面をゴム等の弾性部材により構成することで、伝熱管と伝熱管挿通穴とが接触することによる伝熱管又は掻き落とし部材の破損を防止できる。   In the present embodiment, an appropriate clearance is formed between the inner peripheral surface of the plurality of heat transfer tube insertion holes 20 and the outer peripheral surface of the heat transfer tube 14, but the present invention is not limited to this. That is, you may contact the inner peripheral surface of a some heat exchanger tube penetration hole, and the outer peripheral surface of a heat exchanger tube. In this case, by constituting the inner peripheral surface of the heat transfer tube insertion hole with an elastic member such as rubber, the heat transfer tube or the scraping member can be prevented from being damaged due to the contact between the heat transfer tube and the heat transfer tube insertion hole.

10 二酸化炭素回収装置
11 回収装置本体
12 排ガス導入管
13 排ガス導出管
14 伝熱管
15,16 連結管
17 掻き落とし部材
18 駆動装置
19 収容部
20 伝熱管挿通穴
21 ガス流通穴
22 シリンダ
23 ピストン
24,25 収容容器
26 切替装置
27,28 開閉弁
DESCRIPTION OF SYMBOLS 10 Carbon dioxide recovery apparatus 11 Recovery apparatus main body 12 Exhaust gas inlet pipe 13 Exhaust gas outlet pipe 14 Heat transfer pipe 15, 16 Connecting pipe 17 Scraping member 18 Drive device 19 Housing part 20 Heat transfer pipe insertion hole 21 Gas flow hole 22 Cylinder 23 Piston 24, 25 Container 26 Switching device 27, 28 On-off valve

Claims (6)

ガス中に含まれる二酸化炭素を固化させて回収する二酸化炭素回収装置であって、
筒状に構成されると共に高さ方向が鉛直方向に沿うように配置され、前記ガスが導入される回収装置本体と、
前記回収装置本体の内部に略鉛直方向に延びて配置され、内部を冷媒が流通する伝熱管と、
前記伝熱管の周面に付着した固化された二酸化炭素を掻き落とす掻き落とし手段と、
前記回収装置本体の下方に配置され前記掻き落とし手段により掻き落とされた固化された二酸化炭素が収容される収容部と、を備え
前記掻き落とし手段は、前記伝熱管の周面に近接して鉛直方向に移動可能な掻き落とし部材と、
前記掻き落とし部材を鉛直方向に駆動させる駆動手段と、を備え、
前記掻き落とし部材は、前記回収装置本体における水平方向の断面形状と略同形の板状部材により構成され、該板状部材には、前記伝熱管が挿通される伝熱管挿通穴及び前記回収装置本体の内部に導入されたガスが流通するガス流通穴が形成される二酸化炭素回収装置。
A carbon dioxide recovery device for solidifying and recovering carbon dioxide contained in gas,
A recovery device main body configured in a cylindrical shape and arranged so that the height direction is along the vertical direction, and the gas is introduced,
A heat transfer tube disposed in the recovery device main body so as to extend in a substantially vertical direction, and in which a refrigerant flows;
Scraping means for scraping off the solidified carbon dioxide adhering to the peripheral surface of the heat transfer tube;
A storage section for storing solidified carbon dioxide that is disposed below the recovery apparatus main body and scraped off by the scraping means ;
The scraping means is a scraping member that is movable in the vertical direction in the vicinity of the peripheral surface of the heat transfer tube;
Drive means for driving the scraping member in a vertical direction,
The scraping member is constituted by a plate-like member having substantially the same cross-sectional shape in the horizontal direction in the recovery device body, and the plate-like member has a heat transfer tube insertion hole through which the heat transfer tube is inserted and the recovery device body. A carbon dioxide recovery device in which a gas circulation hole through which a gas introduced into the gas flows is formed .
前記駆動手段は、前記回収装置本体の上面を貫通して配置されるシリンダと、該シリンダに摺動可能に収容され先端側が前記掻き落とし部材に連結されるピストンと、を備える請求項に記載の二酸化炭素回収装置。 Said drive means, according to claim 1 comprising a cylinder disposed through the upper surface of the collection device main body, a piston slidably accommodated in the distal end side in the cylinder is connected to the dumping member scraping said, the Carbon dioxide recovery equipment. 前記収容部は、複数の収容容器により構成され、
前記回収装置本体の底面側には、前記複数の収容容器のうちの所定の収容容器に固化された二酸化炭素を供給する切替手段が設けられる請求項1又は2に記載の二酸化炭素回収装置。
The container is composed of a plurality of containers.
The recovery device on the bottom side of the body, the carbon dioxide recovery apparatus according to claim 1 or 2 switching means is provided for supplying carbon dioxide solidified in a predetermined container of the plurality of container.
前記複数の収容容器それぞれは、密閉性及び耐圧性を有する容器により構成される請求項に記載の二酸化炭素回収装置。 The carbon dioxide recovery device according to claim 3 , wherein each of the plurality of storage containers is configured by a container having airtightness and pressure resistance. 前記掻き落とし部材を前記回収装置本体における所定の待機位置と該待機位置よりも下側に位置する駆動位置との間で移動させるように前記駆動手段を制御する制御手段を更に備える請求項1又は2に記載の二酸化炭素回収装置。 Claim 1 or further comprising a control means for controlling said drive means to move between a driving position located below the predetermined standby position and該待machine position in the collecting device body the scraper 2. The carbon dioxide recovery device according to 2. 前記制御手段は、前記掻き落とし部材を所定の時間間隔で移動させると共に、前記待機位置から前記駆動位置に前記掻き落とし部材を駆動させた後、直ちに前記掻き落とし部材を前記駆動位置から前記待機位置に復帰させるよう前記駆動手段を制御する請求項記載の二酸化炭素回収装置。 The control means moves the scraping member at a predetermined time interval, drives the scraping member from the standby position to the driving position, and immediately moves the scraping member from the driving position to the standby position. The carbon dioxide recovery device according to claim 5, wherein the drive means is controlled to return to the normal state.
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