JP5579630B2 - Carbon dioxide recovery system - Google Patents

Carbon dioxide recovery system Download PDF

Info

Publication number
JP5579630B2
JP5579630B2 JP2011003532A JP2011003532A JP5579630B2 JP 5579630 B2 JP5579630 B2 JP 5579630B2 JP 2011003532 A JP2011003532 A JP 2011003532A JP 2011003532 A JP2011003532 A JP 2011003532A JP 5579630 B2 JP5579630 B2 JP 5579630B2
Authority
JP
Japan
Prior art keywords
carbon dioxide
container
cooling
capturing material
recovery system
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP2011003532A
Other languages
Japanese (ja)
Other versions
JP2012144393A (en
Inventor
大樹 佐藤
雅人 金枝
周一 菅野
晃平 吉川
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hitachi Ltd
Original Assignee
Hitachi Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP2011003532A priority Critical patent/JP5579630B2/en
Publication of JP2012144393A publication Critical patent/JP2012144393A/en
Application granted granted Critical
Publication of JP5579630B2 publication Critical patent/JP5579630B2/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02CCAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
    • Y02C20/00Capture or disposal of greenhouse gases
    • Y02C20/40Capture or disposal of greenhouse gases of CO2
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/151Reduction of greenhouse gas [GHG] emissions, e.g. CO2

Landscapes

  • Treating Waste Gases (AREA)
  • Separation Of Gases By Adsorption (AREA)
  • Carbon And Carbon Compounds (AREA)

Description

本発明は、二酸化炭素回収システムに関する。   The present invention relates to a carbon dioxide recovery system.

温室効果ガスの排出による地球温暖化の問題が広く認識されてきている。温室効果ガスとしては、二酸化炭素(CO)、メタン(CH)、フロン類(CFCs)等が挙げられるが、排出量が多く、実質的に影響が大きいものは二酸化炭素であり、その排出量の削減が緊急の課題となっている。 The problem of global warming due to greenhouse gas emissions has been widely recognized. Examples of greenhouse gases include carbon dioxide (CO 2 ), methane (CH 4 ), and chlorofluorocarbons (CFCs), but carbon dioxide is the one that has a large emission amount and has a substantial effect on its emission. Reduction of volume is an urgent issue.

特開2007−284272号公報には、二酸化炭素を含有する排ガスと二酸化炭素吸収液とを接触させて二酸化炭素を除去する吸収塔と、二酸化炭素を吸収したリッチ溶液を再生する再生塔と、前記再生塔で二酸化炭素が除去されたリーン溶液を吸収塔で再利用する二酸化炭素回収装置であって、前記吸収塔が、二酸化炭素吸収液で排ガス中の二酸化炭素を吸収する二酸化炭素回収部と、前記二酸化炭素回収部の上部側に設けられ、二酸化炭素を除去したガスを冷却すると共に、同伴する二酸化炭素吸収液を回収する水洗部と、前記水洗部で凝縮された二酸化炭素吸収液を含む凝縮水を、前記水洗部の頂部から直接循環する循環ラインと、前記再生塔から前記吸収塔へ前記リーン溶液を供給するリーン溶液供給管に、前記二酸化炭素吸収液を含む凝縮水の余剰分を供給する余剰凝縮水供給ラインとを具備する二酸化炭素回収装置が開示されている。   JP 2007-284272 A discloses an absorption tower that removes carbon dioxide by contacting an exhaust gas containing carbon dioxide with a carbon dioxide absorbing liquid, a regeneration tower that regenerates a rich solution that has absorbed carbon dioxide, A carbon dioxide recovery device that reuses a lean solution from which carbon dioxide has been removed in a regeneration tower, in an absorption tower, wherein the absorption tower absorbs carbon dioxide in exhaust gas with a carbon dioxide absorbent, A cooling unit that is provided on the upper side of the carbon dioxide recovery unit, cools the gas from which carbon dioxide has been removed, collects the accompanying carbon dioxide absorption liquid, and includes a carbon dioxide absorption liquid condensed in the water washing unit. The carbon dioxide absorbing liquid is supplied to a circulation line that circulates water directly from the top of the water washing section, and a lean solution supply pipe that supplies the lean solution from the regeneration tower to the absorption tower. Carbon dioxide recovery apparatus is disclosed comprising a surplus condensed water supplying line for supplying the surplus condensed water containing.

現在、前記特開2007−284272号公報に記載された二酸化炭素吸収液による二酸化炭素の回収技術が利用され始めているが、二酸化炭素吸収液は吸収液再生時の液の揮発損失等の問題によりランニングコストが高い。   Currently, the carbon dioxide recovery technology using a carbon dioxide absorbing solution described in JP-A-2007-284272 has begun to be used, but the carbon dioxide absorbing solution is running due to problems such as volatilization loss of the solution during the regeneration of the absorbing solution. Cost is high.

そこで、吸収液の揮発損失がないためランニングコストが比較的低い、固体の二酸化炭素捕捉材の開発(特開平5−131116号公報、特開2004−261670号公報、特開2001−70726号公報、特開平8−40715号公報)も進められている。   Therefore, development of a solid carbon dioxide capturing material having a relatively low running cost because there is no volatilization loss of the absorbing liquid (JP-A-5-131116, JP-A-2004-261670, JP-A-2001-70726, Japanese Patent Laid-Open No. 8-40715) is also underway.

前記特開平5−131116号公報は、二酸化炭素または二酸化炭素含有ガスを約20〜100℃において遷移金属担持ゼオライトと接触させる二酸化炭素の捕捉方法が開示されている。   Japanese Patent Laid-Open No. 5-131116 discloses a carbon dioxide capturing method in which carbon dioxide or a carbon dioxide-containing gas is brought into contact with a transition metal-supported zeolite at about 20 to 100 ° C.

また、前記特開2004−261670号公報は、二酸化炭素と水分を含有する排ガスを、シランカップリング剤を化学結合させた支持体と接触せしめ、二酸化炭素と選択的に捕捉させ、脱着する排ガスの処理方法が開示されているが、開示された固体状二酸化炭素捕捉材は二酸化炭素と化学反応して二酸化炭素の構造を大きく変えて化合物を生成するため、反応速度が遅く反応に時間を要する。   JP-A-2004-261670 discloses that exhaust gas containing carbon dioxide and moisture is brought into contact with a support chemically bonded with a silane coupling agent to selectively capture and desorb carbon dioxide. Although a treatment method is disclosed, since the disclosed solid carbon dioxide capturing material chemically reacts with carbon dioxide to greatly change the structure of carbon dioxide to produce a compound, the reaction rate is slow and the reaction takes time.

前記特開2001−70726号公報は、二酸化炭素または二酸化炭素含有ガスを約300〜500℃において酸化マグネシウムを主成分とした捕捉材と接触させる二酸化炭素捕捉方法が開示されている。   Japanese Patent Laid-Open No. 2001-70726 discloses a carbon dioxide capturing method in which carbon dioxide or a carbon dioxide-containing gas is brought into contact with a capturing material mainly composed of magnesium oxide at about 300 to 500 ° C.

前記特開平8−40715号公報は、水和物を含む炭酸カリウムを乾燥させて得る多孔質物質を捕捉材として、二酸化炭素を接触捕捉する捕捉材が開示されている。   JP-A-8-40715 discloses a capturing material that captures carbon dioxide in contact with a porous material obtained by drying potassium carbonate containing hydrate as a capturing material.

特開2007−284272号公報JP 2007-284272 A 特開平5−131116号公報JP-A-5-131116 特開2004−261670号公報JP 2004-261670 A 特開2001−70726号公報JP 2001-70726 A 特開平8−40715号公報JP-A-8-40715

しかしながら、上記特開2007−284272号公報、特開平5−131116号公報、特開2004−261670号公報、特開2001−70726号公報、特開平8−40715号公報に記載された技術は、いずれも固体の二酸化炭素補足材を利用する時の二酸化炭素補足反応の反応熱による温度上昇、及びこの温度上昇によって二酸化炭素補足材による二酸化炭素の補足量低下について全く考慮されていない。   However, any of the techniques described in JP 2007-284272 A, JP 5-131116 A, JP 2004-261670 A, JP 2001-70726 A, and JP 8-40715 A However, no consideration is given to the temperature increase due to the heat of reaction of the carbon dioxide capture reaction when using a solid carbon dioxide capture material, and the decrease in the amount of carbon dioxide captured by the carbon dioxide supplement material due to this temperature increase.

本発明の目的は、固体の二酸化炭素捕捉材を用いた場合に、捕捉材及び捕捉材を内包する容器の温度上昇による二酸化炭素の捕捉量の低下を抑制して二酸化炭素回収システムの効率を向上する二酸化炭素回収システムを提供することにある。   The object of the present invention is to improve the efficiency of a carbon dioxide recovery system by suppressing a decrease in the amount of captured carbon dioxide due to a rise in temperature of the container containing the capture material and the capture material when a solid carbon dioxide capture material is used. It is to provide a carbon dioxide recovery system.

本発明の二酸化炭素回収システムは、二酸化炭素を含有する二酸化炭素含有ガスから固体の二酸化炭素捕捉材を用いて二酸化炭素を捕捉分離する二酸化炭素回収システムにおいて、固体の捕捉材を収容する容器と、前記容器を形成する壁部材の内部に前記補足材を冷却する冷却媒体を流下する第1の冷却手段となる冷却配管を配設し、前記冷却配管に冷却媒体を流通させて前記容器に収容された前記捕捉材の温度の上昇を抑制するように構成したことを特徴とする。   The carbon dioxide recovery system of the present invention is a carbon dioxide recovery system that captures and separates carbon dioxide from a carbon dioxide-containing gas containing carbon dioxide using a solid carbon dioxide capture material, and a container that contains a solid capture material; A cooling pipe serving as a first cooling means for flowing down a cooling medium for cooling the supplementary material is disposed inside a wall member forming the container, and the cooling medium is circulated through the cooling pipe and is accommodated in the container. Further, the invention is characterized in that it is configured to suppress an increase in temperature of the capturing material.

また本発明の二酸化炭素回収システムは、二酸化炭素を含有する二酸化炭素含有ガスから固体の二酸化炭素捕捉材を用いて二酸化炭素を捕捉分離する二酸化炭素回収システムにおいて、
固体の捕捉材を収容する容器と、前記容器を形成する壁部材の内部に前記補足材を冷却する冷却媒体を流下する第1の冷却手段となる冷却配管を配設し、前記容器の壁部材の内部に配設された第1の冷却手段に冷却媒体を供給する流路の上流側に該冷却媒体を冷却する第2の冷却手段を配設し、前記容器に収容された前記捕捉材の温度の上昇を抑制するように構成したことを特徴とする。
The carbon dioxide recovery system of the present invention is a carbon dioxide recovery system that captures and separates carbon dioxide from a carbon dioxide-containing gas containing carbon dioxide using a solid carbon dioxide capture material.
A container for storing a solid capturing material, and a cooling pipe serving as a first cooling means for flowing a cooling medium for cooling the supplementary material inside a wall member forming the container, and the wall member of the container A second cooling means for cooling the cooling medium is disposed upstream of the flow path for supplying the cooling medium to the first cooling means disposed in the interior of the trapping material. It is characterized by being configured to suppress an increase in temperature.

本発明によれば、固体の二酸化炭素捕捉材を用いた場合に、捕捉材及び捕捉材を内包する容器の温度上昇による二酸化炭素の捕捉量の低下を抑制して二酸化炭素回収システムの効率を向上する二酸化炭素回収システムを実現することができる。   According to the present invention, when a solid carbon dioxide capturing material is used, the decrease in the amount of captured carbon dioxide due to the temperature rise of the capturing material and the container containing the capturing material is suppressed to improve the efficiency of the carbon dioxide recovery system. A carbon dioxide recovery system can be realized.

本発明の参考例1である二酸化炭素含有ガスから二酸化炭素を分離回収する二酸化炭素回収システムを示す概略構成図。The schematic block diagram which shows the carbon dioxide collection system which isolate | separates and collects a carbon dioxide from the carbon dioxide containing gas which is the reference example 1 of this invention. 二酸化炭素捕捉材の温度分布の経時変化を表わした特性図。The characteristic view showing the time-dependent change of the temperature distribution of a carbon dioxide capture material. 図1に示した参考例1の二酸化炭素回収システムにおける二酸化炭素捕捉材を内包する容器を二酸化炭素含有ガス流通方向に対して平行に切った状況を示す部分断面図。The fragmentary sectional view which shows the condition which cut | disconnected the container which contains the carbon dioxide capture material in the carbon dioxide collection system of the reference example 1 shown in FIG. 1 in parallel with the carbon dioxide containing gas distribution direction. 図1に示した参考例1の二酸化炭素回収システムにおける二酸化炭素捕捉材を内包する容器を二酸化炭素含有ガス流通方向に対して平行に切った状況を示す部分断面図。The fragmentary sectional view which shows the condition which cut | disconnected the container which contains the carbon dioxide capture material in the carbon dioxide collection system of the reference example 1 shown in FIG. 1 in parallel with the carbon dioxide containing gas distribution direction. 本発明の第1実施例である二酸化炭素含有ガスから二酸化炭素を分離回収する二酸化炭素回収システムにおける二酸化炭素捕捉材を内包する容器を二酸化炭素含有ガス流通方向に対して平行に切った状況を示した部分断面図であり、容器内部の二酸化炭素捕捉材を冷却する冷却配管を流れる冷却媒体の流量を制御する制御装置の概略構成を併せて示した図。The state which cut | disconnected the container which contains the carbon dioxide capture material in the carbon dioxide recovery system which isolate | separates and collects carbon dioxide from the carbon dioxide containing gas which is 1st Example of this invention in parallel with the carbon dioxide containing gas distribution direction is shown. FIG. 5 is a partial cross-sectional view illustrating a schematic configuration of a control device that controls a flow rate of a cooling medium flowing through a cooling pipe for cooling a carbon dioxide capturing material inside the container. 本発明の第2実施例である二酸化炭素含有ガスから二酸化炭素を分離回収する二酸化炭素回収システムにおける二酸化炭素捕捉材を内包する容器を複数個設置しており、これらの容器を二酸化炭素含有ガス流通方向に対して平行に切った状況を示した部分断面図であり、容器内部の二酸化炭素捕捉材を冷却する冷却配管を流れる冷却媒体の流量を制御する制御装置の概略構成を併せて示した図。A plurality of containers containing a carbon dioxide capturing material in a carbon dioxide recovery system for separating and recovering carbon dioxide from a carbon dioxide-containing gas according to a second embodiment of the present invention are installed, and these containers are used to distribute carbon dioxide-containing gas. It is the fragmentary sectional view which showed the situation cut | disconnected in parallel with the direction, and the figure which showed together schematic structure of the control apparatus which controls the flow volume of the cooling medium which flows through the cooling piping which cools the carbon dioxide capture material inside a container . 本発明の参考例2である二酸化炭素含有ガスから二酸化炭素を分離回収する二酸化炭素回収システムを示す概略構成図。The schematic block diagram which shows the carbon dioxide collection system which isolate | separates and collects a carbon dioxide from the carbon dioxide containing gas which is the reference example 2 of this invention. 二酸化炭素捕捉時の捕捉材の温度分布を計算する際に用いた諸条件を示す図。The figure which shows various conditions used when calculating the temperature distribution of the capture | acquisition material at the time of a carbon dioxide capture. それぞれの二酸化炭素捕捉反応熱における二酸化炭素捕捉材の最高温度を示す図。The figure which shows the maximum temperature of the carbon dioxide capture material in each carbon dioxide capture reaction heat.

本発明が対象としている固体の二酸化炭素捕捉材を利用した二酸化炭素回収システムは、二酸化炭素吸収液を利用した二酸化炭素回収システムで生じる吸収液の劣化という課題を解決できる方法であるため、固体の二酸化炭素捕捉材の開発が進められてきている。   The carbon dioxide recovery system using the solid carbon dioxide capturing material targeted by the present invention is a method that can solve the problem of deterioration of the absorption liquid that occurs in the carbon dioxide recovery system using the carbon dioxide absorption liquid. Development of carbon dioxide capture materials has been promoted.

一方、発明者らが鋭意検討を行った結果、固体の二酸化炭素捕捉材を利用した場合、二酸化炭素捕捉時の捕捉反応熱によって、捕捉材及び捕捉材を内包する容器の温度が過度に上昇し、捕捉量を減少させる可能性があることが分かった。   On the other hand, as a result of intensive studies by the inventors, when a solid carbon dioxide capturing material is used, the temperature of the container containing the capturing material and the capturing material increases excessively due to the capture reaction heat at the time of capturing the carbon dioxide. It has been found that there is a possibility of reducing the amount of capture.

従って、二酸化炭素を捕捉する前の二酸化炭素含有ガスを予め冷却するか、二酸化炭素捕捉反応時に二酸化炭素捕捉材を内包する容器を適宜冷却することで、二酸化炭素捕捉反応熱による二酸化炭素捕捉量の減少を抑制することができる。   Therefore, the carbon dioxide-containing gas before capturing carbon dioxide is cooled in advance, or the container containing the carbon dioxide capturing material is appropriately cooled at the time of carbon dioxide capturing reaction. Reduction can be suppressed.

この二酸化炭素捕捉材を内包する容器を冷却する方法としては、容器の壁部材を直接冷却する方法や、容器の壁部材内に冷却配管を配設してこの冷却配管に冷却媒体を流通させて冷却する方法などがある。   As a method of cooling the container containing the carbon dioxide capturing material, a method of directly cooling the wall member of the container or a cooling pipe disposed in the wall member of the container and allowing a cooling medium to flow through the cooling pipe. There is a method of cooling.

二酸化炭素捕捉材を内包する容器に前記冷却配管を配設する配置方法は、二酸化炭素含有ガスの流通方向に沿って冷却配管を配置しても良いし、二酸化炭素含有ガスの流通方向の上流部から下流部にかけて幾つかの段階に分けて、各段階に冷却配管を配置しても良い。   The arrangement method of arranging the cooling pipe in the container containing the carbon dioxide capturing material may be arranged along the flow direction of the carbon dioxide-containing gas, or upstream of the flow direction of the carbon dioxide-containing gas. The cooling pipe may be arranged in each stage divided into several stages from the downstream to the downstream.

また、二酸化炭素含有ガスから二酸化炭素を吸着・分離する固体の二酸化炭素捕捉材としては、例えば、シリカ、アルミナ、チタニア、ジルコニア、セリア、及びゼオライトなどの無機酸化物を用いても良いし、MOFs(Metal−Organic Frameworks)やZIFs(Zeolitic Imidazolate Frameworks)のような有機金属化合物や、炭酸アルカリ金属、炭酸水素アルカリ金属、炭酸アルカリ土類金属、又は炭酸水素アルカリ土類金属を用いても良く、又、これらを熱処理したものを用いても良い。
参考例1
Further, as a solid carbon dioxide capturing material for adsorbing and separating carbon dioxide from a carbon dioxide-containing gas, for example, inorganic oxides such as silica, alumina, titania, zirconia, ceria, and zeolite may be used, or MOFs (Metal-Organic Frameworks) and ZIFs (Zeolytic Imidazolate Frameworks), or an organic metal compound, an alkali metal carbonate, an alkali metal hydrogen carbonate, an alkaline earth metal carbonate, or an alkaline earth metal hydrogen carbonate may be used. These may be heat-treated.
[ Reference Example 1 ]

本発明の参考例1である固体の二酸化炭素捕捉材を利用した二酸化炭素回収システムについて、図1乃至図4を用いて説明する。 A carbon dioxide recovery system using a solid carbon dioxide capturing material as Reference Example 1 of the present invention will be described with reference to FIGS.

図1に示した本発明の参考例1である固体の二酸化炭素捕捉材を利用した二酸化炭素回収システムにおいては、開閉バルブ4aを備えた二酸化炭素含有ガス流路1を通じて供給される二酸化炭素を含有するガスから二酸化炭素を捕捉分離する固体の二酸化炭素捕捉材8を内包した容器5は、並列に4基設置されている。 In the carbon dioxide recovery system using the solid carbon dioxide capturing material, which is Reference Example 1 of the present invention shown in FIG. 1, contains carbon dioxide supplied through a carbon dioxide containing gas flow path 1 provided with an opening / closing valve 4a. Four containers 5 containing solid carbon dioxide capturing material 8 for capturing and separating carbon dioxide from the gas to be separated are installed in parallel.

前記固体の二酸化炭素捕捉材8としては、前記した様に、例えば、シリカ、アルミナ、チタニア、ジルコニア、セリア、及びゼオライトなどの無機酸化物を用いても良いし、MOFs(Metal−Organic Frameworks)やZIFs(Zeolitic Imidazolate Frameworks)のような有機金属化合物や、炭酸アルカリ金属、炭酸水素アルカリ金属、炭酸アルカリ土類金属、又は炭酸水素アルカリ土類金属を用いても良く、又、これらを熱処理したものを用いても良い。   As the solid carbon dioxide capturing material 8, as described above, for example, inorganic oxides such as silica, alumina, titania, zirconia, ceria and zeolite may be used, MOFs (Metal-Organic Frameworks), An organic metal compound such as ZIFs (Zeolytic Imidazolate Frameworks), an alkali metal carbonate, an alkali metal hydrogen carbonate, an alkaline earth metal carbonate, or an alkaline earth metal hydrogen carbonate may be used. It may be used.

前記4基設置された固体の二酸化炭素捕捉材8をそれぞれ内包した容器5には、開閉バルブ4bを備えた高純度二酸化炭素ガス流路2を通じて二酸化炭素ガスがそれぞれ供給され、同様に4基設置された前記容器5に開閉バルブ4cを備えた水蒸気ガス流路3を通じて水蒸気ガスがそれぞれ供給されている。   Carbon dioxide gas is supplied to the containers 5 containing the solid carbon dioxide capturing materials 8 installed in the four units through the high-purity carbon dioxide gas flow path 2 provided with the opening / closing valve 4b. Water vapor gas is supplied to each of the containers 5 through the water vapor gas flow path 3 provided with the opening / closing valve 4c.

4基設置された固体の二酸化炭素捕捉材を内包する前記容器5はいずれも同じ機能を具備しており、二酸化炭素回収システムにおける二酸化炭素捕捉過程、二酸化炭素パージ過程、二酸化炭素脱離過程及び冷却過程の4つの過程が順に繰り返して実行される。   The four containers 5 containing the solid carbon dioxide capturing material installed have the same function, and the carbon dioxide capturing process, carbon dioxide purging process, carbon dioxide desorption process and cooling in the carbon dioxide recovery system. The four processes are repeated in sequence.

1つ目の二酸化炭素捕捉過程では、二酸化炭素含有ガス流路1を通じて供給する二酸化炭素含有ガスを、開閉バルブ4aを操作して固体の二酸化炭素捕捉材8を内包する4基ある容器5のうち、1つの容器5のみに流通させ、二酸化炭素含有ガスに含まれた二酸化炭素を二酸化炭素捕捉材8によって捕捉する。そして二酸化炭素が除去された後のガスは開閉バルブ35を操作して前記容器5の出口側に配設した二酸化炭素除去ガス流路6を通じて大気中に排出する。   In the first carbon dioxide capturing process, the carbon dioxide-containing gas supplied through the carbon dioxide-containing gas flow path 1 is operated by operating the on-off valve 4a and including the four containers 5 containing the solid carbon dioxide capturing material 8. The carbon dioxide contained in the carbon dioxide-containing gas is captured by the carbon dioxide capturing material 8 through only one container 5. The gas after the carbon dioxide is removed is discharged into the atmosphere through the carbon dioxide removal gas flow path 6 disposed on the outlet side of the container 5 by operating the opening / closing valve 35.

2つ目の二酸化炭素パージ過程では、4基ある容器5のうち、二酸化炭素捕捉量が飽和した二酸化炭素捕捉材8を内包する容器5へ、開閉バルブ4aを操作して二酸化炭素含有ガス流路1を通じて供給していた二酸化炭素含有ガスの流通を停止する。   In the second carbon dioxide purge process, the carbon dioxide-containing gas flow path is operated by operating the opening / closing valve 4a to the container 5 containing the carbon dioxide capturing material 8 in which the carbon dioxide capturing amount is saturated among the four containers 5. The distribution of the carbon dioxide-containing gas supplied through 1 is stopped.

次に、開閉バルブ4bを操作して、前記容器5内へ高純度二酸化炭素ガス流路2を通じて供給する二酸化炭素を流通させて二酸化炭素以外のガスを前記容器5からパージする。この時、前記容器5から排出されるガスは、開閉バルブ35を操作して二酸化炭素除去ガス流路6を通じて大気中に排出する。   Next, the open / close valve 4 b is operated to circulate carbon dioxide supplied through the high-purity carbon dioxide gas flow path 2 into the container 5 to purge gases other than carbon dioxide from the container 5. At this time, the gas discharged from the container 5 is discharged into the atmosphere through the carbon dioxide removal gas channel 6 by operating the opening / closing valve 35.

最後に、開閉バルブ4b及び開閉バルブ35をそれぞれ操作して、前記容器5内への二酸化炭素ガスの流通と前記容器5からの二酸化炭素除去ガスの排出をそれぞれ停止する。   Finally, the on-off valve 4b and the on-off valve 35 are operated to stop the flow of carbon dioxide gas into the container 5 and the discharge of carbon dioxide removal gas from the container 5, respectively.

3つ目の二酸化炭素脱離過程では、開閉バルブ4cを操作して、水蒸気ガス流路3を通じて前記容器5に水蒸気ガスを供給して該容器5を昇温する。   In the third carbon dioxide desorption process, the open / close valve 4 c is operated to supply water vapor gas to the container 5 through the water vapor gas flow path 3 to raise the temperature of the container 5.

水蒸気ガス流路3を通じて水蒸気を前記容器5に流通させることによって、前記容器5に収容されている固体の二酸化炭素捕捉材8に捕捉している二酸化炭素を脱離させ、開閉バルブ36を操作して前記容器5の出口に配設した二酸化炭素回収流路7を通じて二酸化炭素捕捉材8から脱離させ二酸化炭素を回収する。   By circulating water vapor through the water vapor gas flow path 3 to the container 5, carbon dioxide trapped in the solid carbon dioxide capturing material 8 accommodated in the container 5 is desorbed, and the open / close valve 36 is operated. The carbon dioxide is recovered from the carbon dioxide capturing material 8 through the carbon dioxide recovery flow path 7 disposed at the outlet of the container 5.

4つ目の冷却過程では、固体の二酸化炭素補足材8及び前記二酸化炭素捕捉材8を内包する容器5を、冷却配管11を通じて供給する冷却媒体によって冷却する。以上の4つの過程を、固体の二酸化炭素補足材8を内包する4基の容器5でそれぞれ繰り返すことで、二酸化炭素含有ガスに含まれた二酸化炭素を連続的に脱離させて回収するシステムとなり得る。   In the fourth cooling process, the solid carbon dioxide capturing material 8 and the container 5 containing the carbon dioxide capturing material 8 are cooled by a cooling medium supplied through a cooling pipe 11. By repeating the above four processes in each of the four containers 5 containing the solid carbon dioxide supplement material 8, the carbon dioxide contained in the carbon dioxide-containing gas is continuously desorbed and recovered. obtain.

1基の容器5内に要求される固体の二酸化炭素捕捉材8の量は、1つ目の二酸化炭素捕捉過程における二酸化炭素含有ガスの流通時間と二酸化炭素含有ガスの流通量、及び二酸化炭素含有ガスの二酸化炭素濃度によって決定すれば良い。   The amount of the solid carbon dioxide capturing material 8 required in one container 5 is the distribution time of the carbon dioxide containing gas, the circulation amount of the carbon dioxide containing gas in the first carbon dioxide capturing process, and the carbon dioxide containing amount. What is necessary is just to determine with the carbon dioxide concentration of gas.

二酸化炭素を含有するガスから二酸化炭素を捕捉分離する固体の二酸化炭素捕捉材を用いて二酸化炭素を回収する本参考例1の二酸化炭素回収システムは、二酸化炭素捕捉過程、二酸化炭素パージ過程、二酸化炭素脱離過程、及び冷却過程の4過程を1サイクルとして構成される。 The carbon dioxide recovery system of this Reference Example 1 that recovers carbon dioxide using a solid carbon dioxide capturing material that captures and separates carbon dioxide from a gas containing carbon dioxide includes a carbon dioxide capture process, a carbon dioxide purge process, carbon dioxide The four processes of the desorption process and the cooling process are configured as one cycle.

1サイクルを120分、つまり1過程を30分で運転すると仮定し、二酸化炭素捕捉時の捕捉材の温度分布を、図8に示す諸条件の下で、一次元熱流体として扱い計算した。なお、図8に記載した諸条件は1000MW級の火力発電所の排ガスをモデルとしている。ただし、二酸化炭素捕捉材8を内包する容器5は断熱であると仮定した。   Assuming that one cycle is operated for 120 minutes, that is, one process is operated for 30 minutes, the temperature distribution of the trapping material at the time of capturing carbon dioxide was calculated as one-dimensional thermal fluid under various conditions shown in FIG. The conditions described in FIG. 8 are modeled on exhaust gas from a 1000 MW class thermal power plant. However, it was assumed that the container 5 containing the carbon dioxide capturing material 8 is thermally insulated.

様々な二酸化炭素捕捉反応熱における二酸化炭素捕捉材の最高温度を図9に示した。また、二酸化炭素捕捉反応熱が10kcal/molである二酸化炭素捕捉材を用いた場合の、二酸化炭素補足材温度分布の計算結果を図2に示した。   FIG. 9 shows the maximum temperature of the carbon dioxide capturing material at various heats of carbon dioxide capturing reaction. Moreover, the calculation result of the carbon dioxide supplement material temperature distribution at the time of using the carbon dioxide capture material whose carbon dioxide capture reaction heat is 10 kcal / mol was shown in FIG.

図9に示す通り、二酸化炭素回収システムの二酸化炭素捕捉材温度は、捕捉反応熱としては非常に低い10kcal/molの二酸化炭素捕捉材を用いた場合であっても、捕捉材温度は147℃まで上昇することが判明した。   As shown in FIG. 9, the carbon dioxide capture material temperature of the carbon dioxide recovery system is up to 147 ° C. even when a carbon dioxide capture material of 10 kcal / mol, which is very low as the heat of capture reaction, is used. It turned out to rise.

二酸化炭素捕捉温度を50℃とする二酸化炭素捕捉材は、通常120〜150℃前後で二酸化炭素を脱離するように想定しているため、147℃までの温度上昇により、二酸化炭素捕捉材の二酸化炭素捕捉量は大きく低減することが予測出来る。   Since the carbon dioxide capture material having a carbon dioxide capture temperature of 50 ° C. is normally assumed to desorb carbon dioxide at around 120 to 150 ° C., the carbon dioxide capture material has a carbon dioxide capture temperature of 147 ° C. It can be predicted that the carbon capture amount will be greatly reduced.

従って、二酸化炭素捕捉材による二酸化炭素捕捉量の低減に対処するためには本実施例である二酸化炭素回収システムに記載した様に、二酸化炭素回収システムに冷却手段を設置し、又は後述する本発明の参考例2である二酸化炭素回収システムに記載した様に、二酸化炭素回収システムに冷却手段を設置すると共に、この二酸化炭素回収システムの前段にも別の冷却手段を更に設置することが必須となる。 Therefore, in order to cope with a reduction in the amount of carbon dioxide captured by the carbon dioxide capturing material, as described in the carbon dioxide recovery system of this embodiment, a cooling means is installed in the carbon dioxide recovery system, or the present invention described later. As described in the carbon dioxide recovery system that is Reference Example 2 , the cooling means is installed in the carbon dioxide recovery system, and another cooling means is also required to be installed in the previous stage of the carbon dioxide recovery system. .

図2に示した二酸化炭素捕捉材の温度分布の経時変化を表わしたグラフから理解できるように、二酸化炭素捕捉材中に温度の高い部分と低い部分が生じることが分かる。例えば、二酸化炭素含有ガスを二酸化炭素捕捉材に20分流通した後において、二酸化炭素捕捉材の位置であるガス流れの上流部では二酸化炭素の捕捉飽和に至ると捕捉反応熱が発生しないが、50℃の二酸化炭素含有ガスは流通し続けているため前記二酸化炭素捕捉材は冷却される。   As can be understood from the graph showing the change over time of the temperature distribution of the carbon dioxide trapping material shown in FIG. 2, it can be seen that a high temperature portion and a low temperature portion are generated in the carbon dioxide trapping material. For example, after the carbon dioxide-containing gas is circulated through the carbon dioxide capturing material for 20 minutes, the capture reaction heat is not generated when the carbon dioxide capturing material reaches the carbon dioxide capturing saturation in the upstream portion of the gas flow. Since the carbon dioxide-containing gas at 0 ° C. continues to flow, the carbon dioxide capturing material is cooled.

二酸化炭素捕捉材の位置であるガス流れの最下流部では、二酸化炭素捕捉反応が生じないため、反応熱が発生せず、二酸化炭素捕捉材の温度は低いままである。一方、二酸化炭素捕捉材の位置であるガス流れの上流部と下流部との間では、二酸化炭素捕捉材は二酸化炭素を捕捉して反応熱によって温度が上昇し、上流部より流通する二酸化炭素含有ガスの冷却効果も小さい。従って、前記二酸化炭素捕捉材中には温度分布が生じるので、適切な冷却手段を設置することによって前記二酸化炭素捕捉材を効率よく冷却することが可能となる。
次に本発明の参考例1である固体の二酸化炭素捕捉材を利用した二酸化炭素回収システムについて、更に詳細に説明する。
In the most downstream portion of the gas flow, which is the position of the carbon dioxide capturing material, no carbon dioxide capturing reaction occurs, so no reaction heat is generated, and the temperature of the carbon dioxide capturing material remains low. On the other hand, between the upstream part and the downstream part of the gas flow that is the position of the carbon dioxide capturing material, the carbon dioxide capturing material captures carbon dioxide and the temperature rises due to reaction heat, and the carbon dioxide content that circulates from the upstream part The gas cooling effect is also small. Accordingly, since a temperature distribution is generated in the carbon dioxide capturing material, it is possible to efficiently cool the carbon dioxide capturing material by installing an appropriate cooling means.
Next, the carbon dioxide recovery system using the solid carbon dioxide capturing material which is Reference Example 1 of the present invention will be described in more detail.

図1に示した本参考例1の二酸化炭素回収システムでは、並列に4基設置された前記容器5の内部には、固体の二酸化炭素捕捉材8がそれぞれ収容されており、容器5に供給された二酸化炭素含有ガスを、この固体の二酸化炭素捕捉材8によって補足するようになっている。 In the carbon dioxide recovery system of the first reference example shown in FIG. 1, solid carbon dioxide capturing materials 8 are accommodated in the containers 5 installed in parallel, and supplied to the containers 5. The carbon dioxide-containing gas is supplemented by the solid carbon dioxide capturing material 8.

前記固体の二酸化炭素捕捉材8を収容した容器5は、図3の部分断面図に詳細に示されたように、前記容器5の壁部材9内部の内壁側で二酸化炭素捕捉材8の外周側に位置する領域には、冷却媒体を流通させる冷却配管11が該容器5の周方向にスパイラル状に配設されており、前記容器5の壁部材9内部の前記冷却配管11の外周側に位置する領域には、冷却媒体を流通させる別の冷却配管10が該容器5の長手方向に沿って垂直状に複数本配設されている。 As shown in detail in the partial sectional view of FIG. 3, the container 5 containing the solid carbon dioxide capturing material 8 is on the outer wall side of the carbon dioxide capturing material 8 on the inner wall side inside the wall member 9 of the container 5. The cooling pipe 11 for circulating the cooling medium is disposed in a spiral shape in the circumferential direction of the container 5 in the region located at the outer peripheral side of the cooling pipe 11 inside the wall member 9 of the container 5. A plurality of other cooling pipes 10 for circulating the cooling medium are arranged in the vertical direction along the longitudinal direction of the container 5.

前記容器5には図1に示したように、二酸化炭素含有ガスを容器5に供給する開閉バルブ4aを備えた二酸化炭素含有ガス流路1と、二酸化炭素以外のガスをパージするために高純度の二酸化炭素ガスを容器5に供給する開閉バルブ4bを備えた高純度二酸化炭素ガス流路2と、二酸化炭素捕捉材8に捕捉した二酸化炭素を脱離させるために容器5を昇温させる水蒸気を供給する開閉バルブ4cを備えた水蒸気ガス流路3とがそれぞれ配設されている。   As shown in FIG. 1, the container 5 has a carbon dioxide-containing gas flow path 1 having an opening / closing valve 4a for supplying a carbon dioxide-containing gas to the container 5, and a high purity for purging gases other than carbon dioxide. High-purity carbon dioxide gas flow path 2 provided with open / close valve 4b for supplying carbon dioxide gas to container 5 and steam for raising the temperature of container 5 in order to desorb carbon dioxide captured by carbon dioxide capturing material 8 A water vapor gas flow path 3 having a supply opening / closing valve 4c is provided.

前記容器5には、容器5内に設置された二酸化炭素捕捉材8によって捕捉され、二酸化炭素が除去された後のガスを該容器5から大気中に排出する、開閉バルブ35を備えた二酸化炭素除去ガス流路6が配設されている。   The container 5 is provided with an open / close valve 35 that discharges the gas, which is captured by the carbon dioxide capturing material 8 installed in the container 5 and from which the carbon dioxide has been removed, to the atmosphere. A removal gas channel 6 is provided.

また、前記二酸化炭素除去ガス流路6は、高純度二酸化炭素ガス流路2から供給された二酸化炭素を流通させて二酸化炭素以外のガスをパージする際に、前記容器5から二酸化炭素以外のガスを大気中に排出する流路としても使用される。   Further, the carbon dioxide removal gas flow path 6 is a gas other than carbon dioxide from the container 5 when the carbon dioxide supplied from the high purity carbon dioxide gas flow path 2 is circulated to purge a gas other than carbon dioxide. It is also used as a flow path for discharging gas into the atmosphere.

前記容器5には、水蒸気ガス流路3から供給された水蒸気による昇温によって、二酸化炭素捕捉材8で捕捉していた二酸化炭素を脱離させ、この離脱した二酸化炭素を回収する、開閉バルブ36を備えた二酸化炭素回収流路7が配設されている。   An opening / closing valve 36 is provided in the container 5 to desorb carbon dioxide captured by the carbon dioxide capturing material 8 by temperature rise by water vapor supplied from the water vapor gas flow path 3 and recover the separated carbon dioxide. A carbon dioxide recovery flow path 7 is provided.

図4は本参考例1の二酸化炭素回収システムにおける二酸化炭素捕捉材8を内包する容器5を、二酸化炭素含有ガスの流通方向に対して平行に切った部分断面図であり、複数の冷却配管11が容器5及び容器壁部材9を貫通して配置して、これらの冷却配管11を流れる冷却媒体を調節することによって容器5及び前記容器5に収容した二酸化炭素捕捉材8を効果的に冷却するものある。 FIG. 4 is a partial cross-sectional view of the container 5 containing the carbon dioxide capturing material 8 in the carbon dioxide recovery system of the first reference example cut in parallel to the flow direction of the carbon dioxide-containing gas. Is disposed through the container 5 and the container wall member 9, and the cooling medium flowing through these cooling pipes 11 is adjusted to effectively cool the container 5 and the carbon dioxide capturing material 8 accommodated in the container 5. There are things.

二酸化炭素含有ガスから二酸化炭素を捕捉する二酸化炭素捕捉材8の温度が上昇した際に、二酸化炭素捕捉材8を内包する容器5及び容器5の壁部材9を貫通するように配置した前記冷却配管11が、二酸化炭素含有ガス流れ方向の上流部から下流部にかけてパラレル状に複数に分かれて配設されており、パラレル状に配設されたこれら複数の冷却配管11を流れる冷却媒体により、二酸化炭素含有ガスの流れ方向の上流部から下流部にかけて徐々に温度が上昇していく二酸化炭素捕捉材8の熱を抑制することが可能となる。   When the temperature of the carbon dioxide capturing material 8 that captures carbon dioxide from the carbon dioxide-containing gas rises, the cooling pipe disposed so as to penetrate the container 5 containing the carbon dioxide capturing material 8 and the wall member 9 of the container 5. 11 is divided into a plurality of parallel arrangements from an upstream portion to a downstream portion in the flow direction of the carbon dioxide-containing gas, and carbon dioxide is generated by a cooling medium flowing through the plurality of cooling pipes 11 arranged in parallel. It becomes possible to suppress the heat of the carbon dioxide capturing material 8 whose temperature gradually increases from the upstream portion to the downstream portion in the flow direction of the contained gas.

即ち、二酸化炭素含有ガスから二酸化炭素を捕捉する時、二酸化炭素捕捉材8の温度は二酸化炭素含有ガスの流れの上流部より二酸化炭素含有ガス流れの下流部にかけて、温度が上昇して下流部では所望値を超える温度分布となる可能性がある。   That is, when carbon dioxide is captured from the carbon dioxide-containing gas, the temperature of the carbon dioxide capturing material 8 increases from the upstream portion of the carbon dioxide-containing gas flow to the downstream portion of the carbon dioxide-containing gas flow. The temperature distribution may exceed the desired value.

そこで、冷却配管を二酸化炭素含有ガス流れに沿って垂直状に設置した場合、二酸化炭素捕捉材8の下流部が低温の状態であるにも拘わらず、垂直状に設置した冷却配管を流れる冷却媒体は二酸化炭素捕捉材8の高温部から得た熱を下流側の二酸化炭素捕捉材8の低温部に伝熱して所望値を超える温度に加熱してしまう恐れがある。   Therefore, when the cooling pipe is installed vertically along the carbon dioxide-containing gas flow, the cooling medium flowing through the vertically installed cooling pipe even though the downstream portion of the carbon dioxide capturing material 8 is in a low temperature state. May transfer the heat obtained from the high temperature part of the carbon dioxide capturing material 8 to the low temperature part of the carbon dioxide capturing material 8 on the downstream side and heat it to a temperature exceeding the desired value.

そこで、本参考例1の二酸化炭素回収システムでは、二酸化炭素捕捉材8を内包する容器5及び容器5の壁部材9を貫通するように配置した前記冷却配管11が、二酸化炭素含有ガスの流れ方向の上流部から下流部にかけてパラレル状に複数に分かれて配設させ、これらの冷却配管11に冷却媒体を流下することにより、二酸化炭素含有ガスの流れの下流側に位置する二酸化炭素捕捉材8の温度上昇を抑制することが可能となる。 Therefore, in the carbon dioxide recovery system according to the first reference example , the cooling pipe 11 disposed so as to penetrate the container 5 containing the carbon dioxide capturing material 8 and the wall member 9 of the container 5 has a flow direction of the carbon dioxide-containing gas. The carbon dioxide capturing material 8 located on the downstream side of the flow of the carbon dioxide-containing gas is arranged by being divided into a plurality of parts in parallel from the upstream portion to the downstream portion and flowing the cooling medium through these cooling pipes 11. It becomes possible to suppress the temperature rise.

本参考例1によれば、固体の二酸化炭素捕捉材を用いた場合に、捕捉材及び捕捉材を内包する容器の温度上昇による二酸化炭素の捕捉量の低下を抑制して二酸化炭素回収システムの効率を向上する二酸化炭素回収システムを実現することができる。 According to the first reference example , when a solid carbon dioxide capturing material is used, the decrease in the amount of captured carbon dioxide due to the temperature increase of the capturing material and the container containing the capturing material is suppressed, thereby improving the efficiency of the carbon dioxide recovery system. The carbon dioxide recovery system which improves can be realized.

次に本発明の第1実施例である二酸化炭素回収システムについて図5を用いて説明する。 Next, a carbon dioxide recovery system according to a first embodiment of the present invention will be described with reference to FIG.

図5に示した本実施例の二酸化炭素回収システムは、図1乃至図4に示した参考例1の二酸化炭素回収システムと基本的な構成は共通しているので、両者に共通した説明は省略し、相違する部分について以下に説明する。 The carbon dioxide recovery system of this embodiment shown in FIG. 5 has the same basic configuration as the carbon dioxide recovery system of Reference Example 1 shown in FIGS. Differences will be described below.

図5に示した本実施例の二酸化炭素回収システムにおいて、固体の二酸化炭素捕捉材8を内包する容器5及び前記容器5の壁部材9を貫通するように配置した前記冷却配管11が、二酸化炭素含有ガス流れ方向の上流部から下流部にかけてパラレル状に複数に分かれて配設されており、パラレル状に配設されたこれら複数の冷却配管11には該冷却配管11を流れる冷却媒体の温度を検出する複数の温度検出器17及び冷却配管11を流れる冷却媒体の流量を調節する複数の流量調節器18がそれぞれ設置されている。   In the carbon dioxide recovery system of the present embodiment shown in FIG. 5, the cooling pipe 11 disposed so as to penetrate the container 5 containing the solid carbon dioxide capturing material 8 and the wall member 9 of the container 5 includes carbon dioxide. The plurality of cooling pipes 11 arranged in parallel are arranged in parallel from the upstream part to the downstream part in the flow direction of the contained gas, and the temperature of the cooling medium flowing through the cooling pipe 11 is set in the plurality of cooling pipes 11 arranged in parallel. A plurality of temperature detectors 17 to be detected and a plurality of flow rate adjusters 18 for adjusting the flow rate of the cooling medium flowing through the cooling pipe 11 are installed.

更に前記温度検出器17で検出された冷却配管11を流れる冷却媒体の検出温度に基づいて二酸化炭素含有ガスの流れ方向の上流部から下流部にかけての任意位置における二酸化炭素捕捉材8の温度を所望の温度にそれぞれ調節するために、前記流量調節器18に冷却配管11を流れる冷却媒体の流量を調節する指令信号を演算して出力する制御装置19が設置されている。   Furthermore, based on the detected temperature of the cooling medium flowing through the cooling pipe 11 detected by the temperature detector 17, the temperature of the carbon dioxide capturing material 8 at an arbitrary position from the upstream portion to the downstream portion in the flow direction of the carbon dioxide-containing gas is desired. In order to adjust the flow rate to the respective temperatures, a control device 19 for calculating and outputting a command signal for adjusting the flow rate of the cooling medium flowing through the cooling pipe 11 is installed in the flow rate regulator 18.

上記した本実施例の二酸化炭素回収システムでは、図5の右側に二酸化炭素捕捉材の位置と温度との関係を温度分布として示したように、二酸化炭素捕捉材8が二酸化炭素含有ガスから二酸化炭素を捕捉する際に二酸化炭素捕捉材8の一部の温度が上昇した場合に、二酸化炭素捕捉材8の温度は二酸化炭素含有ガスの流れの上流部と下流部との中間の位置で温度が上昇した高温部となる破線で示したような温度分布となる可能性が高い。   In the carbon dioxide recovery system of the present embodiment described above, the carbon dioxide capture material 8 is transformed from carbon dioxide-containing gas to carbon dioxide as shown on the right side of FIG. When the temperature of a part of the carbon dioxide capturing material 8 rises when capturing carbon dioxide, the temperature of the carbon dioxide capturing material 8 increases at a position intermediate between the upstream portion and the downstream portion of the flow of the carbon dioxide-containing gas. There is a high possibility that the temperature distribution is as shown by the broken line, which is the high temperature part.

そこで、制御装置19によって、固体の二酸化炭素捕捉材8を内包する容器5及び容器の壁部材9を貫通するよう配置したパラレル状に複数配設した冷却配管11に流れる冷却媒体の流量を制御して、前記容器5に収納した二酸化炭素捕捉材8を冷却し該二酸化炭素捕捉材8の温度分布を所望の温度分布となるように調節する。   Therefore, the control device 19 controls the flow rate of the cooling medium flowing through the cooling pipes 11 arranged in parallel so as to pass through the container 5 containing the solid carbon dioxide capturing material 8 and the wall member 9 of the container. Then, the carbon dioxide capturing material 8 accommodated in the container 5 is cooled, and the temperature distribution of the carbon dioxide capturing material 8 is adjusted to a desired temperature distribution.

伝熱管となる前記冷却配管11は二酸化炭素含有ガスの流れ方向の上流部から下流部にかけてパラレル状に複数配設されている。前記容器5に二酸化炭素含有ガスが流入して二酸化炭素捕捉材8の温度が上昇すると、複数の冷却配管11にそれぞれ設置した温度検出器17によって当該冷却配管11が配設された近傍の位置の二酸化炭素捕捉材8の温度を検出して制御装置19に入力する。   A plurality of the cooling pipes 11 serving as heat transfer tubes are arranged in parallel from the upstream portion to the downstream portion in the flow direction of the carbon dioxide-containing gas. When the carbon dioxide-containing gas flows into the container 5 and the temperature of the carbon dioxide capturing material 8 rises, the temperature detector 17 installed in each of the plurality of cooling pipes 11 is located at a position near the cooling pipe 11. The temperature of the carbon dioxide capturing material 8 is detected and input to the control device 19.

前記制御装置19では、この温度検出器17で検出した検出温度と、当該位置の二酸化炭素捕捉材8の所望の温度を設定した設定値と比較して、所望の温度にするために前記冷却配管11に供給すべき冷却媒体の流量を演算し、冷却配管11を流れる冷却媒体の流量を調節する指令信号を流量調節器18に出力して該流量調節器18を操作し、二酸化炭素捕捉材8の任意の位置の近辺の冷却配管11を流れる冷却媒体の流量を調節することで、前記二酸化炭素捕捉材8の温度分布を、図5の右側に二酸化炭素捕捉材の位置と温度との関係を実線で最終的な温度分布として示したように、二酸化炭素捕捉材8の温度は二酸化炭素含有ガス流れの上流部より二酸化炭素含有ガス流れの下流部にかけて、高温部の無い実線で示したようなほぼ一様の温度分布を持つように制御する。   The control device 19 compares the detected temperature detected by the temperature detector 17 with a set value in which the desired temperature of the carbon dioxide capturing material 8 at the position is set, so that the cooling pipe is used to obtain the desired temperature. 11 calculates a flow rate of the cooling medium to be supplied to 11, outputs a command signal for adjusting the flow rate of the cooling medium flowing through the cooling pipe 11 to the flow rate adjuster 18, operates the flow rate adjuster 18, and operates the carbon dioxide trap 8 The temperature distribution of the carbon dioxide capturing material 8 is adjusted by adjusting the flow rate of the cooling medium flowing through the cooling pipe 11 in the vicinity of the arbitrary position, and the relationship between the position and temperature of the carbon dioxide capturing material is shown on the right side of FIG. As indicated by the solid line as the final temperature distribution, the temperature of the carbon dioxide capturing material 8 is as shown by the solid line without the high temperature part from the upstream part of the carbon dioxide containing gas flow to the downstream part of the carbon dioxide containing gas flow. Almost uniform Controlled to have a degree distribution.

二酸化炭素捕捉材8の温度上昇の感知方法は、温度検出器17の設置以外にも、テスト運転による経験的予測手段や熱流体シミュレーションによる温度予測手段によっても良い。   The method for detecting the temperature rise of the carbon dioxide capturing material 8 may be an empirical prediction means by a test operation or a temperature prediction means by a thermal fluid simulation in addition to the installation of the temperature detector 17.

上記したような制御を行うことにより、二酸化炭素捕捉材8に生じる高温部の位置に対してその近傍に配設された冷却配管11を流下する冷却媒体の流量だけを増加させて、二酸化炭素捕捉材8の温度をぼぼ均一な温度分布に調節することが可能となり、結果として二酸化炭素捕捉材8の温度調節に必要な前記冷却配管11に供給する冷却媒体の総流量を減少させることが出来る。   By performing the control as described above, only the flow rate of the cooling medium flowing down the cooling pipe 11 disposed in the vicinity of the position of the high temperature portion generated in the carbon dioxide capturing material 8 is increased, and the carbon dioxide capturing is performed. The temperature of the material 8 can be adjusted to a substantially uniform temperature distribution, and as a result, the total flow rate of the cooling medium supplied to the cooling pipe 11 necessary for adjusting the temperature of the carbon dioxide capturing material 8 can be reduced.

上記したように、本実施例の二酸化炭素回収システムでは、二酸化炭素含有ガス流れ方向の上流部から下流部にかけてパラレル状に配設されたこれら複数の冷却配管11を流れる冷却媒体の流量を調節することにより、二酸化炭素捕捉材8を効率的に冷却して前記二酸化炭素捕捉材8の温度をほぼ一様の温度分布にすることが可能にある。   As described above, in the carbon dioxide recovery system of the present embodiment, the flow rate of the cooling medium flowing through the plurality of cooling pipes 11 arranged in parallel from the upstream portion to the downstream portion in the flow direction of the carbon dioxide-containing gas is adjusted. As a result, the carbon dioxide capturing material 8 can be efficiently cooled to make the temperature of the carbon dioxide capturing material 8 substantially uniform.

本実施例によれば、固体の二酸化炭素捕捉材を用いた場合に、捕捉材及び捕捉材を内包する容器の温度上昇による二酸化炭素の捕捉量の低下を抑制して二酸化炭素回収システムの効率を向上する二酸化炭素回収システムを実現することができる。   According to the present embodiment, when a solid carbon dioxide capturing material is used, the decrease in the amount of captured carbon dioxide due to the temperature rise in the container containing the capturing material and the capturing material is suppressed, thereby improving the efficiency of the carbon dioxide recovery system. An improved carbon dioxide recovery system can be realized.

次に本発明の第2実施例である二酸化炭素回収システムについて図6を用いて説明する。 Next, a carbon dioxide recovery system according to a second embodiment of the present invention will be described with reference to FIG.

本実施例の二酸化炭素回収システムは、図5に示した第1実施例の二酸化炭素回収システムと基本的な構成は共通しているので、両者に共通した説明は省略し、相違する部分について以下に説明する。 Since the basic configuration of the carbon dioxide recovery system of this embodiment is the same as that of the carbon dioxide recovery system of the first embodiment shown in FIG. Explained.

図6に示した本実施例の二酸化炭素回収システムでは、二酸化炭素捕捉材を収容する容器として、二酸化炭素含有ガスが流れる容器5aと、水蒸気ガスが流れる容器5bとを備えている。   The carbon dioxide recovery system of the present embodiment shown in FIG. 6 includes a container 5a through which carbon dioxide-containing gas flows and a container 5b through which water vapor gas flows as containers for storing the carbon dioxide capturing material.

即ち、二酸化炭素含有ガスが流れて二酸化炭素捕捉過程にある二酸化炭素捕捉材8aを内包する容器5aと、水蒸気ガスが流れて二酸化炭素昇温脱離過程にある二酸化炭素捕捉材8bを内包する容器5bとを備え、容器5a、5bの内部及びこれらの容器5a、5bの壁部材9a、9bを貫通し、これらの容器5a、5bに共通してパラレル状に複数個配設されて冷却媒体を流下させる冷却配管11によって繋いだ構造を備えており、二酸化炭素含有ガス及び水蒸気ガスの流通方向に対して容器5a、5bを平行に切った断面図を示している。   That is, a container 5a enclosing a carbon dioxide capturing material 8a in which a carbon dioxide-containing gas flows and in the process of capturing carbon dioxide, and a container enclosing a carbon dioxide capturing material 8b in the process of rising and desorbing carbon dioxide by flowing of water vapor gas 5b, and penetrates the inside of the containers 5a and 5b and the wall members 9a and 9b of these containers 5a and 5b. The structure connected with the cooling piping 11 to flow down is provided, and sectional drawing which cut | disconnected the containers 5a and 5b in parallel with respect to the distribution direction of a carbon dioxide containing gas and water vapor | steam gas is shown.

図6に示した本実施例の二酸化炭素回収システムは、図5に示した第1実施例の二酸化炭素回収システムの場合と同様に、パラレル状に複数個配設された前記冷却配管11に温度検出器17及び流量調節器18がそれぞれ設置され、前記温度検出器17で検出した検出温度に基づいて前記流量調節器18を操作し前記冷却配管11を流下する冷却媒体の流量を調節する制御装置19が設置された構成となっている。 The carbon dioxide recovery system of the present embodiment shown in FIG. 6 is similar to the carbon dioxide recovery system of the first embodiment shown in FIG. A detector 17 and a flow rate adjuster 18 are respectively installed, and a control device for adjusting the flow rate of the cooling medium flowing down the cooling pipe 11 by operating the flow rate adjuster 18 based on the detected temperature detected by the temperature detector 17. 19 is installed.

本実施例の二酸化炭素回収システムでは、二酸化炭素含有ガスが流れる二酸化炭素捕捉過程にある容器5aに収容された二酸化炭素捕捉材8aの一部の温度が上昇した際に、二酸化炭素捕捉材8aを内包する容器5a及び容器の壁部材9aを貫通するように配置したパラレル状に複数配設した共通の冷却配管11を流下する冷却媒体の流量を制御装置19によって調節して冷却し前記二酸化炭素捕捉材8aの温度分布を制御する。   In the carbon dioxide recovery system of the present embodiment, when the temperature of a part of the carbon dioxide capture material 8a accommodated in the container 5a in the carbon dioxide capture process in which the carbon dioxide-containing gas flows is increased, the carbon dioxide capture material 8a is Capture the carbon dioxide by adjusting the flow rate of the cooling medium flowing down through the common cooling pipes 11 arranged in parallel so as to pass through the container 5a and the wall member 9a of the container, by adjusting by the control device 19 The temperature distribution of the material 8a is controlled.

そして二酸化炭素捕捉材8aにおける捕捉反応熱によって、共通して配設された冷却配管11を流れる冷却媒体が得た熱を、水蒸気ガスが流れる二酸化炭素昇温脱離過程にある容器5bに収容された二酸化炭素捕捉材8bへパラレル状に複数配設した共通の冷却配管11を通じて流下する冷却媒体によって移動させることで、前記二酸化炭素捕捉材8bを加熱して昇温する。   Then, the heat obtained by the cooling medium flowing through the commonly arranged cooling pipe 11 by the trapping reaction heat in the carbon dioxide trapping material 8a is accommodated in the container 5b in the carbon dioxide temperature rising and desorption process in which the steam gas flows. The carbon dioxide capturing material 8b is heated and heated by being moved by a cooling medium flowing down through a common cooling pipe 11 arranged in parallel to the carbon dioxide capturing material 8b.

水蒸気ガスが流れる二酸化炭素昇温脱離過程にある容器5bに収容された二酸化炭素捕捉材8bは、この共通した冷却配管11を流下する熱を得た冷却媒体による加熱と、容器5bのガス流入口より流通させる水蒸気ガスによって、二酸化炭素捕捉材8bから二酸化炭素を速やかに脱離することができる。   The carbon dioxide capturing material 8b accommodated in the container 5b in the temperature rising and desorption process in which the water vapor gas flows is heated by the cooling medium that has obtained heat flowing down the common cooling pipe 11, and the gas flow in the container 5b. Carbon dioxide can be quickly desorbed from the carbon dioxide capturing material 8b by the water vapor gas flowing from the inlet.

尚、二酸化炭素含有ガスが流れて二酸化炭素捕捉過程にある容器5aに収容された二酸化炭素捕捉材8aと、水蒸気ガスが流れて二酸化炭素昇温脱離過程にある容器5bに収容された二酸化炭素捕捉材8bのそれぞれの温度分布の制御については、図5に示した第1実施例の二酸化炭素回収システムの場合と同様であり、パラレル状に複数個配設された共通した冷却配管11に設置した前記温度検出器17で検出した検出温度に基づいて制御装置19により前記流量調節器18を操作して前記冷却配管11を流下する冷却媒体の流量を調節することで制御しているので、これらについての説明は省略する。 In addition, the carbon dioxide capture | acquisition material 8a accommodated in the container 5a in which the carbon dioxide containing gas flows and is in the carbon dioxide capture process, and the carbon dioxide accommodated in the container 5b in the carbon dioxide temperature rising desorption process by flowing the steam gas The control of the temperature distribution of each of the trapping materials 8b is the same as in the case of the carbon dioxide recovery system of the first embodiment shown in FIG. 5, and is installed in a common cooling pipe 11 arranged in parallel. Since the control device 19 operates the flow rate regulator 18 based on the detected temperature detected by the temperature detector 17 to adjust the flow rate of the cooling medium flowing down the cooling pipe 11, these are controlled. The description about is omitted.

以上のように、二酸化炭素昇温脱離過程にあり加熱が必要な容器5bに収容された二酸化炭素捕捉材8bを、二酸化炭素捕捉過程にある容器5aに収容された二酸化炭素捕捉材8aで発生した二酸化炭素捕捉反応熱を利用して冷却媒体を介して加熱することができるので、二酸化炭素捕捉反応熱を有効に回収することが出来る。   As described above, the carbon dioxide scavenging material 8b accommodated in the container 5b that is in the process of heating and desorbing carbon dioxide and needs to be heated is generated in the carbon dioxide scavenging material 8a accommodated in the container 5a in the carbon dioxide capturing process. Since the carbon dioxide capture reaction heat can be used for heating through the cooling medium, the carbon dioxide capture reaction heat can be effectively recovered.

本実施例によれば、固体の二酸化炭素捕捉材を用いた場合に、捕捉材及び捕捉材を内包する容器の温度上昇による二酸化炭素の捕捉量の低下を抑制して二酸化炭素回収システムの効率を向上する二酸化炭素回収システムを実現することができる。
参考例2
According to the present embodiment, when a solid carbon dioxide capturing material is used, the decrease in the amount of captured carbon dioxide due to the temperature rise in the container containing the capturing material and the capturing material is suppressed, thereby improving the efficiency of the carbon dioxide recovery system. An improved carbon dioxide recovery system can be realized.
[ Reference Example 2 ]

次に本発明の参考例2である二酸化炭素回収システムについて図7を用いて説明する。 Next, a carbon dioxide recovery system that is a reference example 2 of the present invention will be described with reference to FIG.

図7に示した参考例2の二酸化炭素回収システムは、図1乃至図4に示した参考例1の二酸化炭素回収システムと基本的な構成は共通しているので、両者に共通した説明は省略し、相違する部分について以下に説明する。 Since the basic configuration of the carbon dioxide recovery system of Reference Example 2 shown in FIG. 7 is the same as that of the carbon dioxide recovery system of Reference Example 1 shown in FIGS. 1 to 4, description common to both is omitted. Differences will be described below.

図7に示した本参考例2の二酸化炭素回収システムにおいては、二酸化炭素回収システムの前段となる二酸化炭素含有ガス流路1の開閉バルブ4aの上流側の位置に、二酸化炭素含有ガス流路1を流れる二酸化炭素含有ガスを冷却する冷却手段26を備えたシステムである。 In the carbon dioxide recovery system of the present Reference Example 2 shown in FIG. 7, the carbon dioxide-containing gas flow path 1 is located at the upstream side of the opening / closing valve 4a of the carbon dioxide-containing gas flow path 1 that is the previous stage of the carbon dioxide recovery system. It is the system provided with the cooling means 26 which cools the carbon dioxide containing gas which flows through.

本参考例2の二酸化炭素回収システムでは、冷却手段26によって固体の二酸化炭素捕捉材8を内包する容器5に供給する二酸化炭素含有ガスを冷却することにより、二酸化炭素含有ガスの二酸化炭素含有率が高い場合に、二酸化炭素以外の冷却対象ガス量が小さくできるため特に効率的である。 In the carbon dioxide recovery system of this reference example 2, the carbon dioxide containing gas supplied to the container 5 containing the solid carbon dioxide capturing material 8 is cooled by the cooling means 26 so that the carbon dioxide content of the carbon dioxide containing gas is reduced. When it is high, the amount of gas to be cooled other than carbon dioxide can be reduced, which is particularly efficient.

一般に、固体の二酸化炭素捕捉材8への二酸化炭素捕捉反応の活性化エネルギーが小さいものに関しては、低温である方が二酸化炭素をより多く捕捉する。従って、二酸化炭素回収システムの前段で二酸化炭素含有ガスを冷却しない場合と比べて、容器5に内包する固体の二酸化炭素捕捉材8の容量を低減することが可能となり、また、二酸化炭素捕捉材8の温度上昇も抑制することが可能となる。   In general, for the carbon dioxide capturing material 8 having a small activation energy for the carbon dioxide capturing reaction to the solid carbon dioxide capturing material 8, the carbon dioxide is captured more at a lower temperature. Accordingly, it is possible to reduce the capacity of the solid carbon dioxide capturing material 8 included in the container 5 as compared with the case where the carbon dioxide-containing gas is not cooled in the previous stage of the carbon dioxide recovery system, and the carbon dioxide capturing material 8 It is also possible to suppress the temperature rise.

本参考例2によれば、固体の二酸化炭素捕捉材を用いた場合に、捕捉材及び捕捉材を内包する容器の温度上昇による二酸化炭素の捕捉量の低下を抑制して二酸化炭素回収システムの効率を向上する二酸化炭素回収システムを実現することができる。 According to the present Reference Example 2 , when a solid carbon dioxide capturing material is used, the decrease in the amount of captured carbon dioxide due to the temperature increase of the capturing material and the container containing the capturing material is suppressed, thereby improving the efficiency of the carbon dioxide recovery system. The carbon dioxide recovery system which improves can be realized.

本発明は二酸化炭素を含む排ガスから二酸化炭素を捕捉分離して回収する二酸化炭素回収システムに適用可能である。   The present invention can be applied to a carbon dioxide recovery system that captures and separates and recovers carbon dioxide from exhaust gas containing carbon dioxide.

1:二酸化炭素含有ガス流路、2:高純度二酸化炭素ガス流路、3:水蒸気ガス流路、4a、4b、4c、35、36:開閉バルブ、5、5a、5b:容器、6:二酸化炭素除去ガス流路、7:二酸化炭素回収流路、8、8a、8b:二酸化炭素捕捉材、9:容器の壁部材、10、11:冷却配管、17:温度検出器、18:流量調節器、19:制御装置、26:冷却手段。   1: Carbon dioxide containing gas flow path, 2: High purity carbon dioxide gas flow path, 3: Water vapor gas flow path, 4a, 4b, 4c, 35, 36: Open / close valve, 5, 5a, 5b: Container, 6: Dioxide Carbon removal gas flow path, 7: Carbon dioxide recovery flow path, 8, 8a, 8b: Carbon dioxide capture material, 9: Wall member of container, 10, 11: Cooling piping, 17: Temperature detector, 18: Flow rate regulator , 19: control device, 26: cooling means.

Claims (8)

二酸化炭素を含有する二酸化炭素含有ガスから固体の二酸化炭素捕捉材を用いて二酸化炭素を捕捉分離する二酸化炭素回収システムにおいて、
固体の捕捉材を収容する容器と、前記容器を形成する壁部材の内部に前記捕捉材を冷却する冷却媒体を流下する第1の冷却手段となる冷却配管を配設し、前記冷却配管に冷却媒体を流通させて前記容器に収容された前記捕捉材の温度の上昇を抑制するように構成し、
固体の捕捉材を収容する前記容器の壁部材の内部にそれぞれ配設された第1の冷却手段を構成する冷却配管は、パラレル状に配設された複数の水平配管と、複数の垂直配管とから構成され、
前記複数の水平配管がそれぞれ流量調節手段を備えていることを特徴とする二酸化炭素回収システム。
In a carbon dioxide recovery system for capturing and separating carbon dioxide from a carbon dioxide-containing gas containing carbon dioxide using a solid carbon dioxide capturing material,
A cooling pipe serving as a first cooling means for flowing down a cooling medium for cooling the trapping material is disposed inside the container for storing the solid trapping material and a wall member forming the container, and the cooling pipe is cooled. Configured to suppress an increase in temperature of the trapping material accommodated in the container by circulating a medium;
The cooling pipes constituting the first cooling means respectively disposed inside the wall member of the container for storing the solid capturing material are a plurality of horizontal pipes arranged in parallel, a plurality of vertical pipes, Consisting of
The carbon dioxide recovery system, wherein each of the plurality of horizontal pipes includes a flow rate adjusting means.
二酸化炭素を含有する二酸化炭素含有ガスから固体の二酸化炭素捕捉材を用いて二酸化炭素を捕捉分離する二酸化炭素回収システムにおいて、
固体の捕捉材を収容する容器と、前記容器を形成する壁部材の内部に前記捕捉材を冷却する冷却媒体を流下する第1の冷却手段となる冷却配管を配設し、前記冷却配管に冷却媒体を流通させて前記容器に収容された前記捕捉材の温度の上昇を抑制するように構成し、
固体の捕捉材を収容する容器は前記捕捉材に二酸化炭素含有ガスが流れる第1の容器と、前記捕捉材に水蒸気ガスが流れる第2の容器との複数個配設し、前記複数個配設された各容器の壁部材の内部に配設される第1の冷却手段を構成する冷却配管はパラレル状に配設された複数の水平配管を備えており、これらの複数の水平配管を備えた前記冷却配管が前記第1の容器と第2の容器に亘って共通した冷却配管として配設するように構成され、
前記複数の水平配管がそれぞれ流量調節手段を備えていることを特徴とする二酸化炭素回収システム。
In a carbon dioxide recovery system for capturing and separating carbon dioxide from a carbon dioxide-containing gas containing carbon dioxide using a solid carbon dioxide capturing material,
A cooling pipe serving as a first cooling means for flowing down a cooling medium for cooling the trapping material is disposed inside the container for storing the solid trapping material and a wall member forming the container, and the cooling pipe is cooled. Configured to suppress an increase in temperature of the trapping material accommodated in the container by circulating a medium;
A plurality of containers for storing the solid capturing material are provided, a first container in which carbon dioxide-containing gas flows in the capturing material and a second container in which water vapor gas flows in the capturing material. The cooling pipes constituting the first cooling means arranged inside the wall member of each container are provided with a plurality of horizontal pipes arranged in parallel, and the plurality of horizontal pipes were provided. The cooling pipe is arranged as a common cooling pipe across the first container and the second container,
The carbon dioxide recovery system, wherein each of the plurality of horizontal pipes includes a flow rate adjusting means.
二酸化炭素を含有する二酸化炭素含有ガスから固体の二酸化炭素捕捉材を用いて二酸化炭素を捕捉分離する二酸化炭素回収システムにおいて、
固体の捕捉材を収容する容器と、前記容器を形成する壁部材の内部に前記捕捉材を冷却する冷却媒体を流下する第1の冷却手段となる冷却配管を配設し、前記容器の壁部材の内部に配設された第1の冷却手段に冷却媒体を供給する流路の上流側に該冷却媒体を冷却する第2の冷却手段を配設し、前記容器に収容された前記捕捉材の温度の上昇を抑制するように構成し、
固体の捕捉材を収容する前記容器の壁部材の内部にそれぞれ配設された第1の冷却手段を構成する冷却配管は、パラレル状に配設された複数の水平配管と、複数の垂直配管とから構成され、
前記複数の水平配管がそれぞれ流量調節手段を備えていることを特徴とする二酸化炭素回収システム。
In a carbon dioxide recovery system for capturing and separating carbon dioxide from a carbon dioxide-containing gas containing carbon dioxide using a solid carbon dioxide capturing material,
A container for storing a solid capturing material, and a cooling pipe serving as a first cooling means for flowing down a cooling medium for cooling the capturing material in a wall member forming the container, and the wall member of the container A second cooling means for cooling the cooling medium is disposed upstream of the flow path for supplying the cooling medium to the first cooling means disposed in the interior of the trapping material. Configured to suppress the rise in temperature,
The cooling pipes constituting the first cooling means respectively disposed inside the wall member of the container for storing the solid capturing material are a plurality of horizontal pipes arranged in parallel, a plurality of vertical pipes, Consisting of
The carbon dioxide recovery system, wherein each of the plurality of horizontal pipes includes a flow rate adjusting means.
二酸化炭素を含有する二酸化炭素含有ガスから固体の二酸化炭素捕捉材を用いて二酸化炭素を捕捉分離する二酸化炭素回収システムにおいて、
固体の捕捉材を収容する容器と、前記容器を形成する壁部材の内部に前記捕捉材を冷却する冷却媒体を流下する第1の冷却手段となる冷却配管を配設し、前記容器の壁部材の内部に配設された第1の冷却手段に冷却媒体を供給する流路の上流側に該冷却媒体を冷却する第2の冷却手段を配設し、前記容器に収容された前記捕捉材の温度の上昇を抑制するように構成し、
固体の捕捉材を収容する容器は前記捕捉材に二酸化炭素含有ガスが流れる第1の容器と、前記捕捉材に水蒸気ガスが流れる第2の容器との複数個配設し、前記複数個配設された各容器の壁部材の内部に配設される第1の冷却手段を構成する冷却配管はパラレル状に配設された複数の水平配管を備えており、これらの複数の水平配管を備えた前記冷却配管が前記第1の容器と第2の容器に亘って共通した冷却配管として配設するように構成され、
前記複数の水平配管がそれぞれ流量調節手段を備えていることを特徴とする二酸化炭素回収システム。
In a carbon dioxide recovery system for capturing and separating carbon dioxide from a carbon dioxide-containing gas containing carbon dioxide using a solid carbon dioxide capturing material,
A container for storing a solid capturing material, and a cooling pipe serving as a first cooling means for flowing down a cooling medium for cooling the capturing material in a wall member forming the container, and the wall member of the container A second cooling means for cooling the cooling medium is disposed upstream of the flow path for supplying the cooling medium to the first cooling means disposed in the interior of the trapping material. Configured to suppress the rise in temperature,
A plurality of containers for storing the solid capturing material are provided, a first container in which carbon dioxide-containing gas flows in the capturing material and a second container in which water vapor gas flows in the capturing material. The cooling pipes constituting the first cooling means arranged inside the wall member of each container are provided with a plurality of horizontal pipes arranged in parallel, and the plurality of horizontal pipes were provided. The cooling pipe is arranged as a common cooling pipe across the first container and the second container,
The carbon dioxide recovery system, wherein each of the plurality of horizontal pipes includes a flow rate adjusting means.
請求項1乃至請求項4のいずれか1項に記載した二酸化炭素回収システムにおいて、
固体の捕捉材を収容する前記容器の壁部材の内部に配設された前記第1の冷却手段を構成するパラレル状に配設された複数の水平配管にそれぞれ設置されており、該水平配管内を流通する冷却媒体の温度を検出する温度検出器と、前記水平配管内を流通する冷却媒体の流量を調節する流量調節器と、前記温度検出器で検出した冷却媒体の温度の検出値に基づいて前記容器内の温度分布を演算すると共に、この演算した温度分布が設定された所望の温度分布状況となるように前記流量調節器に対して冷却媒体の流量を調節する指令信号を出力する制御装置を設けていることを特徴とする二酸化炭素回収システム。
In the carbon dioxide recovery system according to any one of claims 1 to 4,
Installed in each of a plurality of horizontal pipes arranged in parallel to constitute the first cooling means arranged in the wall member of the container containing the solid capturing material, A temperature detector for detecting the temperature of the cooling medium flowing through the flow pipe, a flow rate regulator for adjusting the flow rate of the cooling medium flowing through the horizontal pipe, and a detected value of the temperature of the cooling medium detected by the temperature detector Control for calculating the temperature distribution in the container and outputting a command signal for adjusting the flow rate of the cooling medium to the flow rate regulator so that the calculated temperature distribution becomes a set desired temperature distribution state A carbon dioxide recovery system comprising an apparatus.
請求項2又は請求項4に記載した二酸化炭素回収システムにおいて、
前記第1の容器に配設された第1の冷却手段を構成する共通した冷却配管を流れる冷却媒体が前記第1の容器に収容した前記二酸化炭素捕捉材を流れる二酸化炭素含有ガスから得た熱を、熱交換によって前記の共通した冷却配管を流れる冷却媒体を通じて前記第2の容器に収容した水蒸気ガスが流れる前記二酸化炭素捕捉材の加熱に用いるように構成されていることを特徴とする二酸化炭素回収システム。
In the carbon dioxide recovery system according to claim 2 or 4 ,
Heat obtained from a carbon dioxide-containing gas flowing through the carbon dioxide capturing material housed in the first container by a cooling medium flowing through a common cooling pipe constituting the first cooling means disposed in the first container The carbon dioxide is used for heating the carbon dioxide capturing material in which the water vapor gas stored in the second container flows through the cooling medium flowing through the common cooling pipe by heat exchange. Collection system.
請求項1乃至請求項4のいずれか1項に記載した二酸化炭素回収システムにおいて、
前記容器に収容する固体の捕捉材に供給される前記二酸化炭素含有ガスは、0℃以上80℃以下の二酸化炭素含有ガスであることを特徴とする二酸化炭素回収システム。
In the carbon dioxide recovery system according to any one of claims 1 to 4,
The carbon dioxide-containing gas supplied to the solid capturing material accommodated in the container is a carbon dioxide-containing gas having a temperature of 0 ° C. or higher and 80 ° C. or lower.
請求項1乃至請求項4のいずれか1項に記載した二酸化炭素回収システムにおいて、
前記容器に収容する固体の捕捉材に供給される前記二酸化炭素含有ガスは、製鉄所又は火力発電所から排出される排ガスであることを特徴とする二酸化炭素回収システム。
In the carbon dioxide recovery system according to any one of claims 1 to 4,
The carbon dioxide containing system supplied to the solid capturing material accommodated in the container is an exhaust gas discharged from an iron mill or a thermal power plant.
JP2011003532A 2011-01-12 2011-01-12 Carbon dioxide recovery system Expired - Fee Related JP5579630B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2011003532A JP5579630B2 (en) 2011-01-12 2011-01-12 Carbon dioxide recovery system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2011003532A JP5579630B2 (en) 2011-01-12 2011-01-12 Carbon dioxide recovery system

Publications (2)

Publication Number Publication Date
JP2012144393A JP2012144393A (en) 2012-08-02
JP5579630B2 true JP5579630B2 (en) 2014-08-27

Family

ID=46788382

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2011003532A Expired - Fee Related JP5579630B2 (en) 2011-01-12 2011-01-12 Carbon dioxide recovery system

Country Status (1)

Country Link
JP (1) JP5579630B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5897734B2 (en) * 2012-12-13 2016-03-30 株式会社日立製作所 CO2 recovery device and operation method thereof
EP3345674A4 (en) 2015-08-31 2019-03-20 Hitachi Chemical Co., Ltd. Exhaust-gas treatment equipment and gas-capture-material deterioration-state estimating method

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60153919A (en) * 1984-01-25 1985-08-13 Hitachi Ltd Adsorption and regeneration of adsorbing tower
JPS61245818A (en) * 1985-04-25 1986-11-01 Mitsubishi Heavy Ind Ltd Removal of carbon dioxide
JPS62236413A (en) * 1986-04-09 1987-10-16 松下電器産業株式会社 Perishable food storage apparatus
JP2781135B2 (en) * 1993-12-15 1998-07-30 北陸電力株式会社 Gas separation and recovery equipment

Also Published As

Publication number Publication date
JP2012144393A (en) 2012-08-02

Similar Documents

Publication Publication Date Title
CA2785320C (en) Heat recovery system of the boiler with co2 capture system
JP6107695B2 (en) Carbon dioxide recovery device and carbon dioxide recovery method
JP5855130B2 (en) Carbon dioxide chemical absorption system with steam recompression equipment
WO2011132660A1 (en) Exhaust gas treatment system having carbon dioxide removal device
US20190178574A1 (en) Carbon dioxide recovery method and recovery apparatus
CN105032113B (en) Process for capturing carbon dioxide in flue gas based on wet reclamation technology
JP5253509B2 (en) Mercury removal system for carbon dioxide recovery equipment in combustion exhaust gas, and mercury removal operation method for carbon dioxide recovery equipment in combustion exhaust gas
CA2771516A1 (en) Co2 recovery apparatus
WO2015115275A1 (en) Gas absorption and regeneration apparatus and method for operating same
CN203540289U (en) Treating and recovering device of organic waste gas with low concentration and large air volume
JP5914300B2 (en) CO2 solid adsorbent system
JP2010069371A (en) Apparatus for recovering carbon dioxide in coal boiler exhaust gas in thermal power plant and method for recovering carbon dioxide
WO2017126149A1 (en) Carbon dioxide separation/recovery device, combustion system using same, thermal power generation system using same, and method for separating and recovering carbon dioxide
CN105006264A (en) High temperature gas-cooled reactor helium purification regeneration system and regeneration method
JP5579630B2 (en) Carbon dioxide recovery system
EP2781249A1 (en) Carbon dioxide capture equipment
JP5665120B2 (en) Argon gas purification method and purification apparatus
WO2012073552A1 (en) Co2 recovery system
JP4772307B2 (en) Dry desulfurization apparatus, mercury removal method from dry desulfurization apparatus, and regeneration tower
JP2021035654A (en) Co2 separation method and facility
CN118512876A (en) Low-temperature adsorption and carbon capture coupling system for flue gas
TWI507352B (en) Purifying method and purifying apparatus for argon gas
JP2005103335A (en) Thermal desorption type oxygen concentrating apparatus
JP5897734B2 (en) CO2 recovery device and operation method thereof
JP2000212581A (en) Gas purifier using carbonyl sulfide hydrolysis catalyst

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20121109

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20130925

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20131008

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20131206

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20140204

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20140401

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20140701

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20140709

R150 Certificate of patent or registration of utility model

Ref document number: 5579630

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

LAPS Cancellation because of no payment of annual fees