JP2010046599A - Method for regenerating cleaning performance of acidic gas absorbing/removing agent and apparatus for absorbing acidic gas - Google Patents

Method for regenerating cleaning performance of acidic gas absorbing/removing agent and apparatus for absorbing acidic gas Download PDF

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JP2010046599A
JP2010046599A JP2008212341A JP2008212341A JP2010046599A JP 2010046599 A JP2010046599 A JP 2010046599A JP 2008212341 A JP2008212341 A JP 2008212341A JP 2008212341 A JP2008212341 A JP 2008212341A JP 2010046599 A JP2010046599 A JP 2010046599A
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absorption
removal agent
acid gas
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acidic gas
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Hiroshi Hachiman
大志 八幡
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Panasonic Corp
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Abstract

<P>PROBLEM TO BE SOLVED: To solve such a problem that since the removal performance of the conventional acidic gas absorbing/removing agent is deteriorated gradually owing to long-term use, it is necessary to regenerate the used acidic gas absorbing/removing agent and it is also necessary to restrain the strength reduction thereof when regenerated and shorten the regeneration time. <P>SOLUTION: The acidic gas absorbing/removing agent is obtained by immersing a material which is prepared by mixing a small amount of cellulose ether in a main component comprising calcium sulfate, calcium hydroxide and activated carbon, kneading the obtained mixture, compacting the kneaded mixture and hardening the compacted mixture, in an aqueous solution of a hydroxide or carbonate of sodium or potassium. After the acidic gas absorbing/removing agent is used for a long period of time, the used acidic gas absorbing/removing agent is washed with a sulfite aqueous solution. As a result, the regeneration time can be shortened and the strength reduction thereof when regenerated can be restrained. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

本発明は、窒素酸化物やイオウ酸化物などの酸性ガスを吸収除去する除去剤の浄化性能再生方法、さらには酸性ガス吸収処理装置を提供するものである。   The present invention provides a purification performance regeneration method for a removing agent that absorbs and removes acidic gases such as nitrogen oxides and sulfur oxides, and further an acidic gas absorption treatment apparatus.

窒素酸化物やイオウ酸化物などの酸性ガスを吸収除去する除去剤が知られている(例えば、特許文献1参照)。従来のこの酸性ガス吸収除去剤の構成は図5に示す通りであり、1は硫酸カルシウム、2は水酸化カルシウム、3は活性炭、4は不定形炭素、5はナトリウムまたはカリウムの水酸化物または炭酸塩である。   A remover that absorbs and removes acidic gases such as nitrogen oxides and sulfur oxides is known (see, for example, Patent Document 1). The structure of this conventional acid gas absorption and removal agent is as shown in FIG. 5. 1 is calcium sulfate, 2 is calcium hydroxide, 3 is activated carbon, 4 is amorphous carbon, 5 is sodium or potassium hydroxide or Carbonate.

類似組成の酸性ガス吸収除去剤は、他にもあり結合剤として用いている不定形炭素は、非イオン性の水溶性セルロースエーテルとしている(例えば、特許文献2参照)。また、類似組成の酸性ガス吸収除去剤として、アルカリ金属またはアルカリ金属土類金属の水酸化物や炭酸塩などのアルカリと、硫酸カルシウムなどのセメント材と、粉末活性炭からなる混練成型硬化物が知られている(例えば、特許文献3参照)。   There are other acid gas absorption / removal agents having a similar composition, and the amorphous carbon used as a binder is a nonionic water-soluble cellulose ether (see, for example, Patent Document 2). Also known as an acidic gas absorption and removal agent of similar composition is a kneaded and molded cured product comprising an alkali such as an alkali metal or alkali metal earth metal hydroxide or carbonate, a cement material such as calcium sulfate, and powdered activated carbon. (For example, see Patent Document 3).

これらの酸性ガス吸収除去剤は、長期間の使用で活性が低下した場合、主に水洗浄によって浄化性能の再生を行っていた。
特許第2778031号公報 特開2004−230322号公報 特開昭52−123987号公報
When the activity of these acidic gas absorption / removal agents decreases after long-term use, the purification performance is regenerated mainly by washing with water.
Japanese Patent No. 2778031 JP 2004-230322 A JP 52-123987 A

従来の酸性ガス吸収除去剤は、長期間の使用で除去剤内に吸収された酸性ガス成分(硝酸化合物)が蓄積されると、活性が低下し浄化性能が低下していた。その浄化性能の再生方法として、水洗浄を行い酸性ガス吸収除去剤に蓄積された硝酸化合物を水へ溶出することで浄化性能の再生を行ってきた。この方法によると、硝酸化合物と共に吸収除去剤の成分である硫酸カルシウム、水酸化カルシウムなども洗浄水中に溶出し、吸収除去剤自体の強度が低下するという課題があった。また、吸収除去剤に蓄積された硝酸化合物を溶出するためには洗浄時間が4〜5時間必要であり、再生時間を短縮することが求められていた。   Conventional acid gas absorption / removal agents have reduced activity and reduced purification performance when acid gas components (nitric acid compounds) that have been absorbed in the removal agent after long-term use are accumulated. As a method for regenerating the purification performance, the purification performance has been regenerated by washing with water and eluting the nitrate compound accumulated in the acid gas absorption and removal agent into water. According to this method, there is a problem that calcium sulfate, calcium hydroxide and the like, which are components of the absorption removing agent, are eluted together with the nitric acid compound in the washing water, and the strength of the absorption removing agent itself is reduced. Moreover, in order to elute the nitrate compound accumulated in the absorption and removal agent, 4 to 5 hours of washing time is required, and it has been required to shorten the regeneration time.

上記課題を解決するために、本発明は、硫酸カルシウムと水酸化カルシウムと活性炭の主成分にセルロースエーテルを少量混合した混練成型硬化物を、ナトリウムまたはカリウムの水酸化物または炭酸塩の水溶液に浸漬して得た酸性ガス吸収除去剤において、長期間使用して窒素酸化物やイオウ酸化物などの酸性ガスを多量吸収して寿命となった寿命往来品の活性を回復するために、亜硫酸塩水溶液で洗浄するものである。   In order to solve the above-mentioned problems, the present invention immerses a kneaded molded cured product obtained by mixing a small amount of cellulose ether with the main components of calcium sulfate, calcium hydroxide and activated carbon in an aqueous solution of sodium or potassium hydroxide or carbonate. In order to recover the activity of products that have been used for a long time by absorbing a large amount of acid gases such as nitrogen oxides and sulfur oxides, It is to be washed with.

さらに、本発明では亜硫酸塩水溶液で洗浄した酸性ガス吸収除去剤をナトリウムまたはカリウムの水酸化物または炭酸塩の水溶液に浸漬することにより、吸収除去剤の浄化性能再生と再生後の浄化性能持続時間の延長を図るものである。   Furthermore, in the present invention, the acid gas absorption and removal agent washed with the sulfite aqueous solution is immersed in an aqueous solution of sodium or potassium hydroxide or carbonate, thereby regenerating the purification performance of the absorption removal agent and the purification performance duration after regeneration. Is intended to be extended.

本発明により、水洗浄による吸収除去剤自体の強度低下抑制、再生時間の短縮化が可能となる。   According to the present invention, it is possible to suppress the strength reduction of the absorbent removal agent itself by water washing and to shorten the regeneration time.

また、この酸性ガス吸収除去剤を二酸化窒素もしくは二酸化イオウを含有する気体が流れる気体流路に配置した処理装置とすると、−20〜120℃の雰囲気温度で優れた酸性ガス吸収容量を有する酸性ガス吸収処理装置が実現できる。   Further, when this acidic gas absorption / removal agent is a treatment device arranged in a gas flow path through which a gas containing nitrogen dioxide or sulfur dioxide flows, an acidic gas having an excellent acidic gas absorption capacity at an atmospheric temperature of -20 to 120 ° C. An absorption processing apparatus can be realized.

第1の発明の酸性ガス吸収除去剤再生方法は、硫酸カルシウムと水酸化カルシウムと活性炭の主成分にセルロースエーテルを少量混合した混練成型硬化物を、ナトリウムまたはカリウムの水酸化物または炭酸塩の水溶液に浸漬して得た酸性ガス吸収除去剤において、長期間使用後の吸収除去剤を亜硫酸塩水溶液で洗浄することにより、該吸収除去剤の活性を回復させるものである。これより、長期にわたり使用し続け酸性ガス除去性能が低下した酸性ガス吸収除去剤の酸性ガス浄化性能を回復させることができ、吸収除去剤自体の強度低下を抑えられると共に、繰り返し何度も使用可能であるため長期間高い酸性ガス除去性能を保つことができる。さらに再生時間も短縮することができる。   The acid gas absorption / removal agent regeneration method according to the first aspect of the present invention comprises a kneaded and molded product obtained by mixing a small amount of cellulose ether with the main components of calcium sulfate, calcium hydroxide and activated carbon, an aqueous solution of sodium or potassium hydroxide or carbonate In the acidic gas absorption / removal agent obtained by immersing in water, the absorption / removal agent after long-term use is washed with a sulfite aqueous solution to recover the activity of the absorption / removal agent. This makes it possible to recover the acid gas purification performance of the acid gas absorption and removal agent that has continued to be used for a long period of time and the acid gas removal performance has been reduced. Therefore, high acid gas removal performance can be maintained for a long time. Furthermore, the playback time can be shortened.

第2の発明の酸性ガス吸収除去剤再生方法は、第1の発明で使用する亜硫酸塩水溶液を亜硫酸ナトリウム水溶液としたものである。これにより吸収除去剤自体の強度低下を抑えられると共に、繰り返し何度も使用可能であるため長期間高い酸性ガス除去性能を保つことができる。さらに再生時間も短縮することができる。   In the method for regenerating an acidic gas absorption / removal agent of the second invention, the aqueous sulfite solution used in the first invention is an aqueous sodium sulfite solution. As a result, a decrease in strength of the absorption / removal agent itself can be suppressed, and a high acid gas removal performance can be maintained for a long time because it can be used repeatedly. Furthermore, the playback time can be shortened.

第3の発明の酸性ガス吸収除去剤再生方法は、第2の発明で使用する亜硫酸ナトリウム水溶液の濃度を0.2〜5重量%としたものである。酸性ガス吸収除去剤再生液の濃度を最適化しているので、より一層吸収除去剤自体の強度低下を抑えられると共に、繰り返し何度も使用可能であるため長期間高い酸性ガス除去性能を保つことができる。さらに再生時間も短縮することができる。   In the method for regenerating an acidic gas absorption and removal agent of the third invention, the concentration of the aqueous sodium sulfite solution used in the second invention is 0.2 to 5% by weight. Since the concentration of the acid gas absorption and removal agent regeneration solution is optimized, it is possible to further suppress the strength reduction of the absorption and removal agent itself and to maintain high acid gas removal performance for a long time because it can be used repeatedly. it can. Furthermore, the playback time can be shortened.

第4の発明の酸性ガス吸収除去剤再生方法は、第1〜3いずれか1項に記載の酸性ガス吸収除去剤再生方法において、亜硫酸塩水溶液で洗浄し、乾燥後水酸化ナトリウム水溶液に浸漬することにより吸収除去剤の活性を回復させる浄化性能再生方法である。これにより、吸収除去剤自体の強度低下の抑制のほか、再生後の吸収除去剤の酸性ガス除去性能を長期間高く保つことができる。   The acid gas absorption / removal agent regeneration method of the fourth invention is the acid gas absorption / removal agent regeneration method according to any one of items 1 to 3, wherein the acid gas absorption / removal agent regeneration method is washed with a sulfite aqueous solution, dried and then immersed in an aqueous sodium hydroxide solution. This is a purification performance regeneration method for recovering the activity of the absorption remover. Thereby, besides the suppression of the strength reduction of the absorption / removal agent itself, the acid gas removal performance of the absorption / removal agent after regeneration can be kept high for a long period of time.

第5の発明の酸性ガス吸収除去剤再生方法は、第1〜3いずれか1項に記載の酸性ガス吸収除去剤再生方法において、亜硫酸塩水溶液で洗浄し、乾燥後水酸化カリウム水溶液に浸漬することにより吸収除去剤の活性を回復させる浄化性能再生方法である。これにより、吸収除去剤自体の強度低下の抑制のほか、再生後の吸収除去剤の酸性ガス除去性能を長期間高く保つことができる。   The acid gas absorption / removal agent regeneration method of the fifth invention is the acid gas absorption / removal agent regeneration method according to any one of items 1 to 3, wherein the acid gas absorption / removal agent regeneration method is washed with a sulfite aqueous solution, dried and then immersed in an aqueous potassium hydroxide solution. This is a purification performance regeneration method for recovering the activity of the absorption remover. Thereby, besides the suppression of the strength reduction of the absorption / removal agent itself, the acid gas removal performance of the absorption / removal agent after regeneration can be kept high for a long period of time.

第6の発明の酸性ガス吸収除去剤再生方法は、第1〜3いずれか1項に記載の酸性ガス吸収除去剤再生方法において、亜硫酸塩水溶液で洗浄し、乾燥後炭酸ナトリウム水溶液に浸漬することにより吸収除去剤の活性を回復させる浄化性能再生方法である。これにより、吸収除去剤自体の強度低下の抑制のほか、再生後の吸収除去剤の酸性ガス除去性能を長期間高く保つことができる。   The acid gas absorption / removal agent regeneration method of the sixth invention is the acid gas absorption / removal agent regeneration method according to any one of items 1 to 3, wherein the acid gas absorption / removal agent regeneration method is washed with an aqueous sulfite solution, dried and then immersed in an aqueous sodium carbonate solution. This is a purification performance regeneration method for recovering the activity of the absorption remover. Thereby, besides the suppression of the strength reduction of the absorption / removal agent itself, the acid gas removal performance of the absorption / removal agent after regeneration can be kept high for a long period of time.

第7の発明の酸性ガス吸収除去剤再生方法は、第1〜3いずれか1項に記載の酸性ガス吸収除去剤再生方法において、亜硫酸塩水溶液で洗浄し、乾燥後炭酸カリウム水溶液に浸漬することにより吸収除去剤の活性を回復させる浄化性能再生方法である。これにより、吸収除去剤自体の強度低下の抑制のほか、再生後の吸収除去剤の酸性ガス除去性能を長期間高く保つことができる。   The acid gas absorption / removal agent regeneration method of the seventh invention is the acid gas absorption / removal agent regeneration method according to any one of items 1 to 3, wherein the acid gas absorption / removal agent regeneration method is washed with a sulfite aqueous solution, dried and then immersed in an aqueous potassium carbonate solution. This is a purification performance regeneration method for recovering the activity of the absorption remover. Thereby, besides the suppression of the strength reduction of the absorption / removal agent itself, the acid gas removal performance of the absorption / removal agent after regeneration can be kept high for a long period of time.

第8の発明の酸性ガス吸収時処理装置は、第1〜7のいずれか1項に記載の再生方法で得た酸性ガス吸収除去剤を、ニ酸化窒素もしくは二酸化イオウを含有する気体が流れる気体流路に配置した前記酸性ガスを除去する処理装置とした。酸性ガス吸収除去剤は、−20〜120℃雰囲気という最適温度に保持されているため、優れた酸性ガス吸収容量を有する。酸性ガス吸収除去剤は、120℃を超えない温度雰囲気に配置しているので、その構成成分である硫酸カルシウムが脱水して体積膨張することや、この組成のセルロースエーテルが熱分解することが抑制され、寿命が低下することがない。その結果、酸性ガスの除去性能を満足し、かつ長期間使用して活性が低下した酸性ガス吸収除去剤を繰り返し利用可能できる酸性ガス吸収処理装置が得られる。   The processing apparatus for absorbing acidic gas according to the eighth invention is a gas in which a gas containing nitrogen dioxide or sulfur dioxide flows as the acidic gas absorption / removal agent obtained by the regeneration method according to any one of the first to seventh aspects. A treatment apparatus for removing the acidic gas arranged in the flow path was used. The acid gas absorption / removal agent has an excellent acid gas absorption capacity because it is maintained at an optimum temperature of -20 to 120 ° C. Since the acid gas absorption / removal agent is placed in an atmosphere that does not exceed 120 ° C., it suppresses dehydration of the component calcium sulfate and volume expansion and thermal decomposition of the cellulose ether of this composition. The life is not reduced. As a result, an acid gas absorption treatment apparatus that satisfies the acid gas removal performance and can repeatedly use the acid gas absorption / removal agent that has been used for a long time and has decreased activity is obtained.

第9の発明の酸性ガス吸収処理装置は、特に第8の発明で使用する酸性ガス吸収処理装置を、自動車トンネル排ガスまたは自動車道路沿道大気を浄化する装置に適用した。自動車トンネル排ガスや自動車道路沿道大気は、自動車排気ガスに含まれる水分により、一般環境より相対湿度が高く、窒素酸化物や硫黄酸化物の浄化性能が向上する利点がある。このため、自動車トンネル排ガスまたは自動車道路沿道大気中に含まれる窒素酸化物や硫黄酸化物を長時間にわたり吸収除去することができる。   In the acidic gas absorption treatment apparatus of the ninth invention, the acidic gas absorption treatment apparatus used in the eighth invention is applied to an apparatus for purifying automobile tunnel exhaust gas or automobile roadside atmosphere. The exhaust gas from the automobile tunnel and the atmosphere along the automobile road have an advantage that the relative humidity is higher than the general environment due to moisture contained in the automobile exhaust gas, and the purification performance of nitrogen oxides and sulfur oxides is improved. For this reason, it is possible to absorb and remove nitrogen oxides and sulfur oxides contained in automobile tunnel exhaust gas or automobile roadside atmosphere over a long period of time.

(実施の形態1)
図4は、本発明の再生方法で得た酸性ガス吸収除去剤を、二酸化窒素もしくは二酸化イオウを含有する気体が流れる気体流路に配置した処理装置である。酸性ガス吸収除去剤は、−20〜120℃雰囲気に保持する。そのため、優れた酸性ガス吸収容量を有する。また、酸性ガス吸収除去剤は、120℃を超えない温度雰囲気に配置しているので、その構成成分である硫酸カルシウムが脱水して体積膨張することや、この組成のセルロースエーテルが熱分解することが抑制され、寿命が低下することがない。その結果、酸性ガスの除去性能を満足し、かつ長期間使用して活性が低下した酸性ガス吸収除去剤を繰り返し利用可能できる酸性ガス吸収処理装置が得られる。更に、本酸性ガス吸収処理装置は自動車トンネルにも適用できる。自動車トンネルには、自動車排気ガスに含まれる水分により、一般環境より相対湿度が高く、窒素酸化物や硫黄酸化物の浄化性能が向上する利点がある。このため、自動車トンネル排ガスに含まれる窒素酸化物や硫黄酸化物を長時間にわたり吸収除去することができる。
(Embodiment 1)
FIG. 4 shows a processing apparatus in which the acidic gas absorption / removal agent obtained by the regeneration method of the present invention is disposed in a gas flow path through which a gas containing nitrogen dioxide or sulfur dioxide flows. The acid gas absorption / removal agent is maintained in an atmosphere of -20 to 120 ° C. Therefore, it has an excellent acid gas absorption capacity. In addition, since the acid gas absorption / removal agent is arranged in a temperature atmosphere that does not exceed 120 ° C., calcium sulfate, which is a component thereof, dehydrates and expands in volume, and the cellulose ether of this composition is thermally decomposed. Is suppressed, and the lifetime is not reduced. As a result, an acid gas absorption treatment apparatus that satisfies the acid gas removal performance and can repeatedly use the acid gas absorption / removal agent that has been used for a long time and has decreased activity is obtained. Furthermore, the present acid gas absorption treatment apparatus can be applied to an automobile tunnel. The automobile tunnel has the advantage that the relative humidity is higher than the general environment due to the moisture contained in the automobile exhaust gas, and the purification performance of nitrogen oxides and sulfur oxides is improved. For this reason, nitrogen oxides and sulfur oxides contained in automobile tunnel exhaust gas can be absorbed and removed for a long time.

以下、実施例で詳細に説明する。   Examples will be described in detail below.

図1は本発明の一実施例による酸性ガス吸収除去剤の再生フロー図であり、この方法にて再生試験を行った結果を以下に示す。   FIG. 1 is a regeneration flow chart of an acid gas absorption / removal agent according to an embodiment of the present invention. The results of a regeneration test performed by this method are shown below.

(実施例1)
酸性ガスとして実際のディーゼル排ガスを通気させた酸性ガス吸収除去剤を試験サンプルとして、サンプルを洗浄液で洗浄し、洗浄完了後の洗浄水中に溶出した全窒素量を測定した。洗浄液は水と亜硫酸ナトリウム水溶液(濃度5%)とした。洗浄時間は1時間、2.5時間、4時間とした。
Example 1
The acid gas absorption and removal agent in which actual diesel exhaust gas was passed as acid gas was used as a test sample, and the sample was washed with a washing solution, and the total amount of nitrogen eluted in the washing water after washing was measured. The cleaning liquid was water and a sodium sulfite aqueous solution (concentration 5%). The washing time was 1 hour, 2.5 hours, and 4 hours.

試験結果を図2に示す。全窒素溶出量は従来の再生方法(水洗浄、4時間)を100として、それぞれの再生方法による全窒素溶出量を比較した。亜硫酸ナトリウム水溶液(濃度5%)による再生方法は、洗浄時間を従来の4分の1以上とすることによって、従来方法と同等以上の洗浄効果を得た。従って、亜硫酸ナトリウム水溶液による再生方法で再生時間を短縮できる。なお、本試験を20回繰り返したところ、従来方法ではサンプルが僅かに割れ・欠けが起こったが、亜硫酸ナトリウム水溶液での再生ではサンプルの割れ・欠けが起こらず、再生による吸収除去剤の強度低下を抑制することを確認した。   The test results are shown in FIG. The total nitrogen elution amount was set to 100 as the conventional regeneration method (water washing, 4 hours), and the total nitrogen elution amount by each regeneration method was compared. The regeneration method using a sodium sulfite aqueous solution (concentration 5%) obtained a cleaning effect equivalent to or higher than that of the conventional method by setting the cleaning time to a quarter or more of the conventional method. Therefore, the regeneration time can be shortened by the regeneration method using an aqueous sodium sulfite solution. In addition, when this test was repeated 20 times, the sample was slightly cracked or chipped by the conventional method, but the sample was not cracked or chipped by regeneration with an aqueous sodium sulfite solution, and the strength of the absorbent remover was reduced by regeneration. It was confirmed that

(実施例2)
実施例1と同様の試験を、洗浄時間1時間として洗浄水を亜硫酸ナトリウム水溶液濃度を0.2%、1.0%、5.0%の3パターンで実施した。
(Example 2)
The same test as in Example 1 was carried out with a washing time of 1 hour and the washing water in three patterns with a sodium sulfite aqueous solution concentration of 0.2%, 1.0% and 5.0%.

試験結果を図3に示す。亜硫酸ナトリウム水溶液濃度を0.2%〜5.0%として酸性ガス吸収除去剤を1時間洗浄することによって、従来方法と同等の洗浄効果を得た。なお、亜硫酸ナトリウム水溶液の濃度を0.2%未満とした場合、洗浄効果がより小さくなるため、洗浄時間を1時間とする場合は亜硫酸ナトリウム水溶液濃度を0.2%以上とすることが好ましい。一方、亜硫酸ナトリウム水溶液濃度が5.0%を超える場合、1回の洗浄工程で使用する亜硫酸ナトリウムの投入量が多くなり過ぎるため洗浄コストが増加してしまう。   The test results are shown in FIG. A cleaning effect equivalent to that of the conventional method was obtained by cleaning the acidic gas absorbing / removing agent for 1 hour with an aqueous sodium sulfite concentration of 0.2% to 5.0%. When the concentration of the sodium sulfite aqueous solution is less than 0.2%, the cleaning effect is further reduced. Therefore, when the cleaning time is 1 hour, the concentration of the sodium sulfite aqueous solution is preferably 0.2% or more. On the other hand, when the concentration of the sodium sulfite aqueous solution exceeds 5.0%, the amount of sodium sulfite used in one cleaning step is excessively increased, resulting in an increase in cleaning cost.

また、本試験を20回繰り返したところ、従来方法ではサンプルが僅かに割れ・欠けが起こったが、亜硫酸ナトリウム水溶液での再生ではサンプルの割れ・欠けが起こらず、再生による吸収除去剤の強度低下を抑制することを確認した。従って、本実施例により、洗浄水に使用する亜硫酸ナトリウム水溶液の濃度を0.2%〜5.0%とすることによって、酸性ガス吸収除去剤の強度低下を抑えつつ再生時間の短縮化を図ることができる。   In addition, when this test was repeated 20 times, the sample was slightly cracked or chipped by the conventional method, but the sample was not cracked or chipped by regeneration with an aqueous sodium sulfite solution, and the strength of the absorbent removal agent decreased due to regeneration. It was confirmed that Therefore, according to the present embodiment, the concentration of the sodium sulfite aqueous solution used for the washing water is set to 0.2% to 5.0%, thereby reducing the regeneration time while suppressing the decrease in the strength of the acid gas absorption and removal agent. be able to.

本発明は、自動車トンネル排ガスまたは道路道路沿道に設置する酸性ガス吸収処理装置に使用する酸性ガス吸収除去剤の再生方法として適している。   INDUSTRIAL APPLICABILITY The present invention is suitable as a method for regenerating an acid gas absorption / removal agent used in automobile tunnel exhaust gas or an acid gas absorption treatment apparatus installed along a road.

本発明の一実施例による再生方法フロー図Reproduction method flow chart according to one embodiment of the present invention 本発明の実施例1による試験結果を示すグラフThe graph which shows the test result by Example 1 of this invention 本発明の実施例2による試験結果を示すグラフThe graph which shows the test result by Example 2 of this invention 本発明の第1の実施の形態を示す酸性ガス吸収処理装置システム系統図Acid gas absorption processing system diagram showing the first embodiment of the present invention 従来の酸性ガス吸収除去剤の断面図Cross section of conventional acid gas absorption and removal agent

符号の説明Explanation of symbols

1 硫酸カルシウム
2 水酸化カルシウム
3 活性炭
4 不定形炭素
5 ナトリウムまたはカリウムの水酸化物または炭酸塩
6 酸性ガス吸収除去剤
7 気体流路
8 酸性ガス吸収処理装置
DESCRIPTION OF SYMBOLS 1 Calcium sulfate 2 Calcium hydroxide 3 Activated carbon 4 Amorphous carbon 5 Sodium or potassium hydroxide or carbonate 6 Acid gas absorption removal agent 7 Gas flow path 8 Acid gas absorption treatment device

Claims (9)

硫酸カルシウムと水酸化カルシウムと活性炭の主成分にセルロースエーテルを少量混合した混練成型硬化物を、ナトリウムまたはカリウムの水酸化物または炭酸塩の水溶液に浸漬して得た酸性ガス吸収除去剤において、長期間使用後、該吸収除去剤を亜硫酸塩水溶液で洗浄することにより、該吸収除去剤の活性を回復させる浄化性能再生方法。 In the acid gas absorption and removal agent obtained by immersing a kneaded molded cured product in which a small amount of cellulose ether is mixed with the main components of calcium sulfate, calcium hydroxide and activated carbon in an aqueous solution of sodium or potassium hydroxide or carbonate. A purification performance regeneration method for recovering the activity of the absorption removing agent by washing the absorption removing agent with a sulfite aqueous solution after a period of use. 亜硫酸塩は、亜硫酸ナトリウムとした請求項1記載の吸収除去剤浄化性能再生方法。 The absorption removal agent purification performance regeneration method according to claim 1, wherein the sulfite is sodium sulfite. 亜硫酸ナトリウム水溶液の濃度を0.2〜5重量%とした請求項2記載の吸収除去剤浄化性能再生方法。 The method according to claim 2, wherein the concentration of the aqueous sodium sulfite solution is 0.2 to 5% by weight. 亜硫酸塩水溶液で洗浄し、乾燥後、水酸化ナトリウム水溶液に浸漬することにより、該吸収除去剤の活性を回復させる請求項1〜3いずれかに記載の酸性ガス吸収除去剤浄化性能再生方法。 4. The method for regenerating purification performance of an acid gas absorption / removal agent according to any one of claims 1 to 3, wherein the activity of the absorption / removal agent is recovered by washing with a sulfite aqueous solution, drying, and immersing in an aqueous sodium hydroxide solution. 亜硫酸塩水溶液で洗浄し、乾燥後、水酸化カリウム水溶液に浸漬することにより、該吸収除去剤の活性を回復させる請求項1〜3いずれかに記載の酸性ガス吸収除去剤浄化性能再生方法。 4. The method for regenerating purification performance of an acid gas absorption / removal agent according to any one of claims 1 to 3, wherein the activity of the absorption / removal agent is recovered by washing with a sulfite aqueous solution, drying, and immersing in an aqueous potassium hydroxide solution. 亜硫酸塩水溶液で洗浄し、乾燥後、炭酸ナトリウム水溶液に浸漬することにより、該吸収除去剤の活性を回復させる請求項1〜3いずれかに記載の酸性ガス吸収除去剤浄化性能再生方法。 4. The method for regenerating purification performance of an acid gas absorbing / removing agent according to any one of claims 1 to 3, wherein the activity of the absorbing / removing agent is recovered by washing with an aqueous sulfite solution, drying, and immersing in an aqueous sodium carbonate solution. 亜硫酸塩水溶液で洗浄し、乾燥後、炭酸カリウム水溶液に浸漬することにより、該吸収除去剤の活性を回復させる請求項1〜3いずれかに記載の酸性ガス吸収除去剤浄化性能再生方法。 4. The method for regenerating purification performance of an acid gas absorption / removal agent according to any one of claims 1 to 3, wherein the activity of the absorption / removal agent is recovered by washing with a sulfite aqueous solution, drying, and immersing in an aqueous potassium carbonate solution. 該酸性ガス吸収除去剤をニ酸化窒素もしくは二酸化イオウを含有する気体が流れる気体流路に配置した処理装置であり、前記酸性ガス吸収除去剤は、−20〜120℃の雰囲気温度で接触させることにより気体中の前記酸性ガスを除去する酸性ガス吸収処理装置であって、長期間使用後該吸収除去剤の活性が低下しても請求項1〜7のいずれか1項に記載の再生方法により繰り返し該吸収除去剤を利用可能な酸性ガス吸収処理装置。 The acid gas absorption / removal agent is a treatment apparatus arranged in a gas flow path through which a gas containing nitrogen dioxide or sulfur dioxide flows, and the acid gas absorption / removal agent is brought into contact at an atmospheric temperature of -20 to 120 ° C. An acidic gas absorption treatment apparatus that removes the acidic gas in the gas by using the regeneration method according to any one of claims 1 to 7, even if the activity of the absorbent removal agent decreases after long-term use. An acidic gas absorption treatment apparatus capable of repeatedly using the absorption and removal agent. 該酸性ガス吸収除去剤を自動車トンネルまたは自動車道路沿道に設置することにより、自動車トンネル排ガスまたは自動車道路沿道大気を浄化する請求項8記載の酸性ガス吸収処理装置。 The acid gas absorption treatment apparatus according to claim 8, wherein the acid gas absorption / removal agent is installed along an automobile tunnel or an automobile road to purify the exhaust gas from the automobile tunnel or the atmosphere along the automobile road.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012510887A (en) * 2008-12-08 2012-05-17 キャンソルヴ テクノロジーズ インコーポレーテッド Regeneration method of ion exchange resin using sulfurous acid

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012510887A (en) * 2008-12-08 2012-05-17 キャンソルヴ テクノロジーズ インコーポレーテッド Regeneration method of ion exchange resin using sulfurous acid

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