JP2004352587A5 - - Google Patents

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JP2004352587A5
JP2004352587A5 JP2003154489A JP2003154489A JP2004352587A5 JP 2004352587 A5 JP2004352587 A5 JP 2004352587A5 JP 2003154489 A JP2003154489 A JP 2003154489A JP 2003154489 A JP2003154489 A JP 2003154489A JP 2004352587 A5 JP2004352587 A5 JP 2004352587A5
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JP
Japan
Prior art keywords
alkali
carbon dioxide
exhaust gas
absorbing solution
liquid
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Pending
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JP2003154489A
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Japanese (ja)
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JP2004352587A (en
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Priority to JP2003154489A priority Critical patent/JP2004352587A/en
Priority claimed from JP2003154489A external-priority patent/JP2004352587A/en
Publication of JP2004352587A publication Critical patent/JP2004352587A/en
Publication of JP2004352587A5 publication Critical patent/JP2004352587A5/ja
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【特許請求の範囲】
【請求項1】
排ガス導入口、アルカリ吸収液導入口、不溶排ガス排出口およびアルカリ吸収液排出口を備え、導入された排ガスとアルカリ吸収液とを気液接触させて該アルカリ吸収液に該排ガス中の二酸化炭素を吸収させる二酸化炭素吸収塔と、
前記二酸化炭素吸収塔のアルカリ吸収液排出口から排出されるアルカリ吸収液を前記アルカリ吸収液導入口に還流させるアルカリ吸収液還流ラインと、
前記アルカリ吸収液還流ライン内に介挿され、または前記アルカリ吸収液還流ラインから分岐する配管で接続されたアルカリ吸収液を収容可能な沈殿槽と
前記沈殿槽に沈殿剤を注入する沈殿剤注入装置と
を具備することを特徴とする排ガス中の二酸化炭素回収システム。
【請求項2】
前記沈殿槽に収容されたアルカリ吸収液中に吸収された二酸化炭素の濃度に対応する濃度を測定する濃度測定装置と、
前記濃度測定装置で測定されたアルカリ吸収液中に吸収された二酸化炭素の濃度に対応する濃度に基づいて、前記アルカリ吸収液還流ラインおよび前記沈殿剤注入装置を制御する制御手段と
をさらに具備することを特徴とする請求項1記載の排ガス中の二酸化炭素回収システム。
【請求項3】
排ガス導入口、アルカリ吸収液導入口、不溶排ガス排出口およびアルカリ吸収液排出口を備え、導入された排ガスとアルカリ吸収液とを気液接触させて該アルカリ吸収液に該排ガス中の二酸化炭素を吸収させる二酸化炭素吸収塔と、
前記二酸化炭素吸収塔のアルカリ吸収液排出口から排出されるアルカリ吸収液を前記アルカリ吸収液導入口に還流させるアルカリ吸収液還流ラインと、
前記アルカリ吸収液還流ライン内に介挿され、または前記アルカリ吸収液還流ラインから分岐する配管で接続されたアルカリ吸収液を収容可能な沈殿槽と、
前記沈殿槽において生成された不溶性化合物が供給され、該不溶性化合物を1つの反応物とするアンモニアソーダ法によって生成された副産物を、沈殿剤として前記沈殿槽に供給する炭酸ナトリウム生成装置と
を具備することを特徴とする排ガス中の二酸化炭素回収システム。
【請求項4】
前記沈殿槽に収容されたアルカリ吸収液中に吸収された二酸化炭素の濃度に対応する濃度を測定する濃度測定装置と、
前記濃度測定装置で測定されたアルカリ吸収液中に吸収された二酸化炭素の濃度に対応する濃度に基づいて、前記アルカリ吸収液還流ラインおよび前記炭酸ナトリウム生成装置を制御する制御手段と
をさらに具備することを特徴とする請求項3記載の排ガス中の二酸化炭素回収システム。
【請求項5】
前記アルカリ吸収液が、灰からアルカリ成分を溶出したものであることを特徴とする請求項1乃至4のいずれか1項記載の排ガス中の二酸化炭素回収システム。
【請求項6】
前記アルカリ吸収液が、炭酸ナトリウム水溶液であることを特徴とする請求項1乃至4のいずれか1項記載の排ガス中の二酸化炭素回収システム。
【請求項7】
前記アルカリ吸収液が、土壌からアルカリ成分を溶出したものであることを特徴とする請求項1乃至4のいずれか1項記載の排ガス中の二酸化炭素回収システム。
【請求項8】
前記沈殿剤が、塩化カルシウムであることを特徴とする請求項1乃至7のいずれか1項記載の排ガス中の二酸化炭素回収システム。
【請求項9】
前記沈殿槽に収容された前記二酸化炭素を吸収したアルカリ吸収液に前記沈殿剤を添加することによって生成される不溶性化合物が、炭酸カルシウムであることを特徴とする請求項1乃至8のいずれか1項記載の排ガス中の二酸化炭素回収システム。
【請求項10】
排ガスとアルカリ吸収液と気液接触させて、二酸化炭素を該アルカリ吸収液に吸収させる吸収工程と、
前記アルカリ吸収液に吸収された二酸化炭素の濃度が所定の値に達するまで、該アルカリ吸収液を排ガスに繰り返して気液接触させる吸収量増加工程と、
前記アルカリ吸収液に吸収された二酸化炭素の濃度が所定の値に達した場合に、該アルカリ吸収液に沈殿剤を添加し、該アルカリ吸収液に吸収された二酸化炭素から不溶性化合物を生成させる不溶性化合物生成工程と
を具備することを特徴とする排ガス中の二酸化炭素回収方法。
【請求項11】
排ガスとアルカリ吸収液と気液接触させて、二酸化炭素を該アルカリ吸収液に吸収させる吸収工程と、
前記アルカリ吸収液に吸収された二酸化炭素の濃度が所定の値に達するまで、該アルカリ吸収液を排ガスに繰り返して気液接触させる吸収量増加工程と、
前記アルカリ吸収液に吸収された二酸化炭素の濃度が所定の値に達した場合に、該アルカリ吸収液に沈殿剤を添加し、該アルカリ吸収液に吸収された二酸化炭素から不溶性化合物を生成させる不溶性化合物生成工程と、
前記生成された不溶性化合物が供給され、該不溶性化合物を1つの反応物とするアンモニアソーダ法によって生成された副産物を、前記不溶性化合物生成工程における沈殿剤として添加する沈殿剤生成工程と
を具備することを特徴とする排ガス中の二酸化炭素回収方法。
[Claims]
(1)
An exhaust gas inlet, an alkali absorbing solution inlet, an insoluble exhaust gas outlet, and an alkali absorbing solution outlet are provided.The introduced exhaust gas and the alkali absorbing solution are brought into gas-liquid contact to cause carbon dioxide in the exhaust gas to flow into the alkali absorbing solution. A carbon dioxide absorption tower to be absorbed,
An alkali absorption liquid reflux line for refluxing the alkali absorption liquid discharged from the alkali absorption liquid outlet of the carbon dioxide absorption tower to the alkali absorption liquid inlet,
A sedimentation tank that can accommodate an alkali absorbing solution inserted in the alkali absorbing solution reflux line or connected by a pipe branched from the alkali absorbing solution reflux line ,
A system for injecting a precipitant into the sedimentation tank; and a system for recovering carbon dioxide in exhaust gas.
(2)
A concentration measuring device for measuring the concentration corresponding to the concentration of the absorbed carbon dioxide in the alkaline absorbent solution contained in the settling tank,
Control means for controlling the alkali absorbing solution reflux line and the precipitant injection device based on a concentration corresponding to the concentration of carbon dioxide absorbed in the alkali absorbing solution measured by the concentration measuring device. The system for recovering carbon dioxide in exhaust gas according to claim 1, wherein:
(3)
An exhaust gas inlet, an alkali absorbing solution inlet, an insoluble exhaust gas outlet, and an alkali absorbing solution outlet are provided.The introduced exhaust gas and the alkali absorbing solution are brought into gas-liquid contact to cause carbon dioxide in the exhaust gas to flow into the alkali absorbing solution. A carbon dioxide absorption tower to be absorbed,
An alkali absorption liquid reflux line for refluxing the alkali absorption liquid discharged from the alkali absorption liquid outlet of the carbon dioxide absorption tower to the alkali absorption liquid inlet,
A sedimentation tank that can accommodate an alkali absorbing solution inserted in the alkali absorbing solution reflux line or connected by a pipe branched from the alkali absorbing solution reflux line,
An insoluble compound generated in the sedimentation tank is supplied, and a by-product generated by the ammonia soda method using the insoluble compound as one reactant is supplied to the sedimentation tank as a precipitant. A system for recovering carbon dioxide in exhaust gas.
(4)
A concentration measuring device that measures the concentration corresponding to the concentration of carbon dioxide absorbed in the alkali absorbing solution contained in the settling tank,
Control means for controlling the alkali absorbent reflux line and the sodium carbonate generator based on a concentration corresponding to the concentration of carbon dioxide absorbed in the alkali absorbent measured by the concentration measuring device. The system for recovering carbon dioxide in exhaust gas according to claim 3, characterized in that:
(5)
The system for recovering carbon dioxide in exhaust gas according to any one of claims 1 to 4, wherein the alkali absorbing solution is obtained by eluted an alkali component from ash.
6.
The system for recovering carbon dioxide in exhaust gas according to any one of claims 1 to 4, wherein the alkali absorbing liquid is an aqueous solution of sodium carbonate.
7.
The system for recovering carbon dioxide in exhaust gas according to any one of claims 1 to 4, wherein the alkali absorbing liquid is obtained by eluted an alkali component from soil.
Claim 8.
The system for recovering carbon dioxide in exhaust gas according to any one of claims 1 to 7, wherein the precipitant is calcium chloride.
9.
Insoluble compounds formed by the addition of the precipitating agent to the alkaline absorbent solution which has absorbed the carbon dioxide contained in the settling tank is any one of claims 1 to 8, characterized in that calcium carbonate 1 The system for recovering carbon dioxide in exhaust gas according to the above item.
10.
Gas-liquid contact with the exhaust gas and the alkali absorbing solution, an absorption step of absorbing carbon dioxide into the alkali absorbing solution,
Until the concentration of carbon dioxide absorbed in the alkali absorption liquid reaches a predetermined value, an absorption amount increasing step of repeatedly bringing the alkali absorption liquid into gas-liquid contact with exhaust gas,
When the concentration of carbon dioxide absorbed in the alkali absorbing solution reaches a predetermined value, a precipitant is added to the alkali absorbing solution to form an insoluble compound from the carbon dioxide absorbed in the alkali absorbing solution. A method for recovering carbon dioxide in exhaust gas, comprising: a compound generation step.
11.
Gas-liquid contact with the exhaust gas and the alkali absorbing solution, an absorption step of absorbing carbon dioxide into the alkali absorbing solution,
Until the concentration of carbon dioxide absorbed in the alkali absorption liquid reaches a predetermined value, an absorption amount increasing step of repeatedly bringing the alkali absorption liquid into gas-liquid contact with exhaust gas,
When the concentration of carbon dioxide absorbed in the alkali absorbing solution reaches a predetermined value, a precipitant is added to the alkali absorbing solution to form an insoluble compound from the carbon dioxide absorbed in the alkali absorbing solution. A compound generation step;
A precipitant generating step in which the generated insoluble compound is supplied, and a by-product generated by the ammonia soda method using the insoluble compound as one reactant is added as a precipitant in the insoluble compound generating step. A method for recovering carbon dioxide from exhaust gas.

【0010】
【課題を解決するための手段】
上記目的を達成するために、本発明の排ガス中の二酸化炭素回収システムは、排ガス導入口、アルカリ吸収液導入口、不溶排ガス排出口およびアルカリ吸収液排出口を備え、導入された排ガスとアルカリ吸収液とを気液接触させて該アルカリ吸収液に該排ガス中の二酸化炭素を吸収させる二酸化炭素吸収塔と、前記二酸化炭素吸収塔のアルカリ吸収液排出口から排出されるアルカリ吸収液を前記アルカリ吸収液導入口に還流させるアルカリ吸収液還流ラインと、前記アルカリ吸収液還流ライン内に介挿され、または前記アルカリ吸収液還流ラインから分岐する配管で接続されたアルカリ吸収液を収容可能な沈殿槽と、前記沈殿槽に沈殿剤を注入する沈殿剤注入装置とを具備することを特徴とする。


[0010]
[Means for Solving the Problems]
In order to achieve the above object, the system for recovering carbon dioxide in exhaust gas of the present invention is provided with an exhaust gas inlet, an alkali absorbing solution inlet, an insoluble exhaust gas outlet, and an alkali absorbing solution outlet. A carbon dioxide absorption tower that causes the alkali absorption liquid to absorb carbon dioxide in the exhaust gas by bringing the liquid into gas-liquid contact with the liquid, and the alkali absorption liquid discharged from the alkali absorption liquid outlet of the carbon dioxide absorption tower. An alkali absorption liquid reflux line for refluxing the liquid introduction port, and a precipitation tank capable of containing an alkali absorption liquid interposed in the alkali absorption liquid reflux line or connected by a pipe branched from the alkali absorption liquid reflux line. And a precipitant injection device for injecting a precipitant into the sedimentation tank .


JP2003154489A 2003-05-30 2003-05-30 System and method for recovering carbon dioxide in exhaust gas Pending JP2004352587A (en)

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Application Number Priority Date Filing Date Title
JP2003154489A JP2004352587A (en) 2003-05-30 2003-05-30 System and method for recovering carbon dioxide in exhaust gas

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JP2004352587A5 true JP2004352587A5 (en) 2006-06-08

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Families Citing this family (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7727374B2 (en) 2004-09-23 2010-06-01 Skyonic Corporation Removing carbon dioxide from waste streams through co-generation of carbonate and/or bicarbonate minerals
MX2008013815A (en) * 2006-04-27 2009-05-11 Harvard College CAPTURE OF CARBON DIOXIDE AND RELATED PROCEDURES.
CA2688023C (en) * 2007-05-24 2013-05-28 Co2 Purification As Device and process for removal of carbon dioxide from combustion gases
JP4895945B2 (en) * 2007-08-28 2012-03-14 東亜熱研株式会社 Carbon dioxide reducing agent and method for reducing carbon dioxide in combustion exhaust gas
PL2205341T3 (en) 2007-09-20 2012-08-31 Skyonic Corp Removing carbon dioxide from waste gas streams through co-generation of carbonate and/or bicarbonate minerals
JP5196482B2 (en) * 2007-09-28 2013-05-15 一般財団法人電力中央研究所 Turbine equipment with alkali carbonate
JP5202221B2 (en) * 2008-10-02 2013-06-05 日立造船株式会社 Method for recovering carbon dioxide in exhaust gas
JP5268719B2 (en) * 2009-03-11 2013-08-21 株式会社東芝 Method and system for removing carbon dioxide in exhaust gas using seawater
AU2011202257B2 (en) * 2010-02-19 2012-11-15 Commonwealth Scientific And Industrial Research Organisation Vapour suppression additive
CN103079676A (en) 2010-07-16 2013-05-01 瑞迪姆Ccs股份有限公司 Method and system for reducing industrial emissions
KR101096179B1 (en) * 2011-10-06 2011-12-22 (주)대우건설 Ca (OH) 2 aqueous solution chicken pox pressurized carbon dioxide removal device and method
KR101096180B1 (en) * 2011-10-06 2011-12-22 (주)대우건설 Exhaust gas recirculation carbon dioxide capture device and method
KR101077574B1 (en) 2011-10-06 2011-10-27 (주)대우건설 Continuous collection apparatus and method for exhaust gas carbon dioxide using calcium hydroxide
KR101140775B1 (en) 2012-03-02 2012-07-12 (주)대우건설 Apparatus for capture of carbon dioxide continuously circulating aqueous solution in duct reactor and the method thereof
CA2937108A1 (en) 2014-01-17 2015-07-23 Skyonic Corporation Acid gas removal from a gaseous stream
KR101644538B1 (en) * 2014-12-18 2016-08-02 재단법인 포항산업과학연구원 Method and apparatus for capturing and resourcing carbon dioxide from flue gas containing carbon dioxide
US10118843B2 (en) * 2015-08-18 2018-11-06 United Arab Emirates University Process for capture of carbon dioxide and desalination
CN110642272B (en) * 2019-09-30 2024-06-28 安徽金禾实业股份有限公司 A alkali-making device for recovering decarbonization waste gas from synthetic ammonia
JP2021154231A (en) * 2020-03-27 2021-10-07 三菱パワー株式会社 Equipment and methods related to combustion exhaust gas purification treatment
JP7344578B2 (en) * 2021-04-26 2023-09-14 株式会社アサカ理研 How to dispose of waste lithium-ion batteries
CN114699890B (en) * 2022-03-09 2024-01-23 中煤能源研究院有限责任公司 System and method for adsorbing and solidifying carbon dioxide by industrial sludge

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