KR20020050991A - Method for wet scrubbing of nitrogen oxides from flue gas - Google Patents
Method for wet scrubbing of nitrogen oxides from flue gas Download PDFInfo
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- KR20020050991A KR20020050991A KR1020000080308A KR20000080308A KR20020050991A KR 20020050991 A KR20020050991 A KR 20020050991A KR 1020000080308 A KR1020000080308 A KR 1020000080308A KR 20000080308 A KR20000080308 A KR 20000080308A KR 20020050991 A KR20020050991 A KR 20020050991A
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/54—Nitrogen compounds
- B01D53/56—Nitrogen oxides
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
- B01D53/1493—Selection of liquid materials for use as absorbents
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/77—Liquid phase processes
- B01D53/78—Liquid phase processes with gas-liquid contact
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Abstract
Description
[산업상 이용 분야][Industrial use]
본 발명은 배기가스 중에 함유된 질소산화물(NOx)의 습식제거방법에 관한 것으로, 특히 질소산화물의 습식 세정공정에서 흡수제로 NaClO2, Na2SO3, 및 NaOH를 혼합한 용액을 사용하여 질소산화물을 제거하는 제거방법에 관한 것이다.The present invention relates to a method for the wet removal of nitrogen oxides (NO x ) contained in the exhaust gas, in particular using a solution of NaClO 2 , Na 2 SO 3 , and NaOH as a absorbent in the wet cleaning process of nitrogen oxides. It relates to a removal method for removing an oxide.
[종래 기술][Prior art]
소각 또는 연소 공정에서 생성된 질소산화물(NOx)은 대기 중에 포함되어 산성비 및 이로 인한 환경파괴 원인으로 알려져 있다. 따라서 질소산화물이 대기중으로 배출되기 전에 배기가스로부터 질소산화물을 제거하는 것이 중요하다.Nitrogen oxides (NO x ) produced during incineration or combustion processes are known to be the cause of acid rain and environmental degradation. Therefore, it is important to remove nitrogen oxides from the exhaust gas before it is released into the atmosphere.
일반적으로 배기가스에 함유된 질소산화물을 제거하는 방법은 건식공정과 습식공정으로 크게 나누어진다. 이중 습식공정은 질산 제조설비나 금속의 산세공정 등에서 발생하는 배기가스 중의 질소산화물을 제거하는데 많이 사용되고 있는데, 이들 공정에서 발생하는 질소산화물은 물에 잘 녹아 쉽게 제거되는 NO2를 많이 포함하고 있기 때문이다.In general, the method of removing the nitrogen oxide contained in the exhaust gas is largely divided into a dry process and a wet process. Double wet process is used to remove nitrogen oxides in exhaust gas from nitric acid manufacturing facilities and metal pickling processes, because the nitrogen oxides generated in these processes contain a lot of NO 2 which is easily dissolved in water and easily removed. to be.
이와같은 습식 세정공정에서는 주로 NaOH나 Na2S 등과 같은 알카리 용액을 사용하여 배기가스 중의 질소산화물을 제거한다. 이때 반응은 하기의 반응식 1과 같다.In such a wet cleaning process, an alkali solution such as NaOH or Na 2 S is mainly used to remove nitrogen oxides in the exhaust gas. In this case, the reaction is shown in Scheme 1 below.
[반응식 1]Scheme 1
그러나 질소산화물 중의 많은 부분을 차지하는 일산화질소(NO)의 경우 물에 대한 용해도가 낮아 물에 잘 용해되지 않고, 산소와의 산화반응에 의해 NO2로 산화되는 정도가 매우 낮기 때문에 질소산화물 중에 NO의 함량이 높을 경우 제거효율이 떨어지게 된다.However, nitrogen monoxide (NO), which occupies a large portion of nitrogen oxides, has low solubility in water, so that it is not soluble in water, and oxidation of NO 2 is very low due to oxidation with oxygen. If the content is high, the removal efficiency is reduced.
따라서 이러한 습식 세정공정의 문제점을 해결하기 위한 방법들이 고안되어 왔다. 그 예로는 공지문헌 "Industrial & Engineering Chemistry : Process Design and Development, Col.22, No.2, pp.323∼329, 1983"은 산화제인 KMnO4를 NaOH 용액에 같이 사용하여 NO를 물에 용해가 잘 되는 NO2나 NO3로 산화시킴으로서 질소산화물(NOx) 제거효율을 높일 수 있음을 나타내고 있다. 그러나 이 방법에서는반응과정에서 고형의 MnO2가 생성되어 세정탑이 막히는 문제점이 있다.Therefore, methods have been devised to solve the problems of the wet cleaning process. For example, the publication "Industrial & Engineering Chemistry: Process Design and Development, Col. 22, No. 2, pp.323-329, 1983" uses KMnO 4 as an oxidant in NaOH solution to dissolve NO in water. By oxidizing to NO 2 or NO 3 which is good, it shows that nitrogen oxide (NO x ) removal efficiency can be improved. However, this method has a problem in that solid MnO 2 is generated during the reaction and the washing tower is blocked.
이외에 산화제인 NaClO2를 사용하여 NO 제거효율을 높이는 방법이 알려져 있는데, 공지문헌 "Chem.Eng.Comm., col.174, pp.21∼51, 1999"에서는 NaClO2와 NaOH를 혼합한 흡수액을 이용하여 NO를 제거하는 방법에 대해 개시되어 있다. 이 방법의 경우에는 NO를 효과적으로 제거할 수 있지만, 일부분의 NO가 NO2로 산화되어 흡수액에서 제거되지 않고 배출된다는 문제점이 있다.In addition, a method of improving NO removal efficiency by using an oxidizing agent, NaClO 2 , is known. In the well-known document "Chem.Eng.Comm., Col.174, pp.21-51, 1999", an absorbent liquid in which NaClO 2 and NaOH are mixed is used. Discloses a method for removing NO. In this method, NO can be effectively removed, but there is a problem that a part of NO is oxidized to NO 2 and is discharged without being removed from the absorbent liquid.
본 발명은 상기 종래 기술의 문제점을 고려하여, 배기가스 중에 함유된 질소산화물의 제거효율이 높은 흡수제를 제공하는 것을 목적으로 한다.The present invention has been made in view of the problems of the prior art, and an object thereof is to provide an absorbent having a high removal efficiency of nitrogen oxide contained in exhaust gas.
본 발명의 다른 목적은 상기 흡수제를 사용하여 배기가스 중에 함유된 질소산화물을 제거하는 습식제거방법을 제공하는 것이다.Another object of the present invention is to provide a wet removal method for removing nitrogen oxides contained in exhaust gas using the absorbent.
[과제를 해결하기 위한 수단][Means for solving the problem]
본 발명은 상기 목적을 달성하기 위하여, 배기가스에 함유된 질소산화물(NOx)의 제거효율이 높은 흡수제를 제공한다.In order to achieve the above object, the present invention provides an absorbent having high removal efficiency of nitrogen oxide (NO x ) contained in exhaust gas.
또한 본 발명은 배기가스에 함유된 질소산화물의 습식 세정공정에 있어서,In addition, the present invention in the wet cleaning process of the nitrogen oxide contained in the exhaust gas,
a) NaClO2, Na2SO3, 및 NaOH를 혼합하여 흡수제를 제공하는 단계; 및a) mixing NaClO 2 , Na 2 SO 3 , and NaOH to provide an absorbent; And
b) 상기 흡수제에 질소산화물이 함유된 배기가스를 접촉시키는 단계b) contacting the absorbent exhaust gas containing nitrogen oxides
를 포함하는 질소산화물의 습식제거방법을 제공한다.It provides a wet removal method of nitrogen oxide comprising a.
이하 본 발명을 상세히 설명한다.Hereinafter, the present invention will be described in detail.
[작용][Action]
본 발명은 배기가스 중에 함유된 질소산화물(NOx)을 제거하기 위하여 습식 세정공정에서 흡수제로 NaClO2, Na2SO3, 및 NaOH를 혼합한 용액을 사용하여 질소산화물이 함유된 배기가스를 접촉시킴으로써 배기가스 중에 함유된 질소산화물을 효과적으로 제거할 수 있다.In the present invention, in order to remove nitrogen oxides (NO x ) contained in the exhaust gas, the exhaust gas containing nitrogen oxides is contacted using a solution containing NaClO 2 , Na 2 SO 3 , and NaOH as an absorbent in a wet cleaning process. In this way, the nitrogen oxide contained in the exhaust gas can be effectively removed.
본 발명에서는 종래의 NaClO2와 NaOH를 혼합한 흡수액을 사용하여 배기가스 중에 함유된 질소산화물을 제거하는 방법에 있어서, NO의 산화에 의해 발생된 NO2가 제거되지 않고 배출되는 단점을 개선하기 위하여, NaClO2, Na2SO3, 및 NaOH를 혼합한 용액을 흡수제로 사용한다.In the present invention, in the conventional method for removing nitrogen oxides contained in the exhaust gas by using an absorption liquid mixed with NaClO 2 and NaOH, to improve the disadvantage that the NO 2 generated by the oxidation of NO is not removed. , A solution of NaClO 2 , Na 2 SO 3 , and NaOH is used as an absorbent.
본 발명의 질소산화물 가스제거용 흡수제는 제거하고자 하는 NO와 NO2의 양, 및 비율에 따라 당량비보다 많은 양으로 포함하는 것이 바람직하다. 또한 실제 사용시에도 질소산화물과의 반응에 의해 가스제거용 흡구제가 소모되는 정도만큼 계속해서 보충하면서 사용한다. 따라서 가스제거용 흡수제의 사용비도 NO, 및 NO2의 비율에 따라 조절하는 것이 바람직하다.Absorbent for removing nitrogen oxide gas of the present invention NO and NO to be removed2It includes in an amount greater than the equivalence ratio according to the quantity, and ratio It is preferable. In addition, in actual use, it is used while continuing to replenish as much as the amount of the gas removal absorbing agent by the reaction with nitrogen oxides. Therefore, the use ratio of absorbent for degassing is NO, and NO2It is preferable to adjust according to the ratio of.
본 발명과 같은 세정방법에서 NaClO2는 강산화제로 NO와 반응하여 질산을 생성하거나, NO를 NO2로 산화시킨다. 이는 하기의 반응식 2와 같이 반응한다.In the cleaning method of the present invention, NaClO 2 reacts with NO as a strong oxidant to produce nitric acid, or oxidize NO to NO 2 . It reacts as in Scheme 2 below.
[반응식 2]Scheme 2
본 발명의 질소산화물을 제거하기 위한 산화제 중 Na2SO3는 하기의 반응식 3과 같은 반응에 의해 NO2를 제거하는 역할을 한다.Na 2 SO 3 in the oxidizing agent for removing the nitrogen oxide of the present invention serves to remove NO 2 by the reaction shown in Scheme 3 below.
[반응식 3]Scheme 3
본 발명에서 흡수액에 사용되는 NaOH는 흡수액의 pH를 유지하기 위해 사용되고, 이는 질소산화물이 흡수액에 흡수되어 제거되면서 생성되는 질산에 의해 pH가 떨어지면 NaClO2등이 분해되어 효율이 떨어지는 것을 막아준다.NaOH used in the absorbent liquid in the present invention is used to maintain the pH of the absorbent liquid, which prevents NaClO 2 from being degraded when the pH is lowered by nitric acid produced while being absorbed and removed by the nitrogen oxide.
이하의 실시예를 통하여 본 발명을 더욱 상세하게 설명한다. 단 실시예는 본 발명을 예시하기 위한 것이지 이들만으로 한정하는 것은 아니다.The present invention will be described in more detail with reference to the following examples. However, the examples are not intended to limit the present invention to illustrate the invention.
[실시예]EXAMPLE
실시예 1Example 1
질소산화물의 제거효과를 측정하기 위하여 공기에 NO가 1600 ppm 혼합된 혼합가스를 2 L/min의 유량으로 흡수액이 1 L 들어있는 컬럼에 버플링(bubbling)하면서 통과시켜 제거효율을 측정하였다. 흡수액으로 사용된 NaClO2와 Na2SO3, 및 NaOH의 농도는 각각 5 중량%였다. 반응개시 1 시간 후, 흡수컬럼 출구에서의 NO, NO2의 각각 농도를 하기 표 1에 나타내었다.In order to measure the removal effect of nitrogen oxides, the removal efficiency was measured by passing a mixed gas mixed with 1600 ppm of NO in air at a flow rate of 2 L / min while bubbling a column containing 1 L of absorbent liquid. The concentrations of NaClO 2 , Na 2 SO 3 , and NaOH used as the absorbent liquid were 5% by weight, respectively. One hour after the start of the reaction, the concentrations of NO and NO 2 at the outlet of the absorption column are shown in Table 1 below.
비교예 1Comparative Example 1
질소산화물의 제거효과를 측정하기 위하여 공기에 NO가 1600 ppm 혼합된 혼합가스를 2 L/min의 유량으로 흡수액이 1 L 들어있는 컬럼에 버플링(bubbling)하면서 통과시켜 제거효율을 측정하였다. 흡수액으로 NaClO2와 NaOH만을 사용하고 각각의 농도는 5 중량%로 하였다. 반응개시 1 시간 후, 흡수컬럼 출구에서의 NO, NO2의 각각 농도를 하기 표 1에 나타내었다.In order to measure the removal effect of nitrogen oxides, the removal efficiency was measured by passing a mixed gas mixed with 1600 ppm of NO in air at a flow rate of 2 L / min while bubbling a column containing 1 L of absorbent liquid. Only NaClO 2 and NaOH were used as the absorbing liquid, and each concentration was 5% by weight. One hour after the start of the reaction, the concentrations of NO and NO 2 at the outlet of the absorption column are shown in Table 1 below.
상기 표 1에 따르면, NaClO2와 NaOH만 사용한 경우는 NO2가 많이 배출되었으나, NaClO2와 Na2SO3, 및 NaOH을 사용한 흡수제는 NO2배출량이 크게 줄어들어 질소산화물 제거율이 높음을 알 수 있었다.According to Table 1, when only NaClO 2 and NaOH was used, a lot of NO 2 was discharged. However, the absorbents using NaClO 2 , Na 2 SO 3 , and NaOH showed a large reduction in NO 2 emissions, resulting in high NOx removal rates. .
상기에서 살펴본 바와 같이, 본 발명의 방법은 NaClO2와 Na2SO3, 및 NaOH을혼합한 용액을 흡수제로 사용하여 배기가스 중의 질소산화물을 효과적으로 제거할 수 있다.As described above, the method of the present invention can effectively remove nitrogen oxides in the exhaust gas by using a mixture of NaClO 2 , Na 2 SO 3 , and NaOH as an absorbent.
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Cited By (2)
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KR100945520B1 (en) * | 2008-03-12 | 2010-03-09 | 엔텍이앤씨 주식회사 | Method for eliminating odorous gas |
KR102031210B1 (en) | 2018-05-02 | 2019-10-11 | 한국에너지기술연구원 | Apparatus and Method for Reduction of Hazardous Emission of Marine Engine |
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JPS56126431A (en) * | 1980-03-08 | 1981-10-03 | Nippon Soda Co Ltd | Wet type denitration method |
JPS57171424A (en) * | 1981-04-14 | 1982-10-22 | Fuji Kikai Kk | Removal of nitrogen oxides in gas |
US4839147A (en) * | 1985-04-05 | 1989-06-13 | Waagner-Biro Aktiengesellschaft | Method of purifying combustion product gases contaminated with dust and noxious gases |
KR19980071998A (en) * | 1998-07-10 | 1998-10-26 | 홍종두 | Nitrogen oxide removal method using oxidant and its removal device |
KR20000042033A (en) * | 1998-12-24 | 2000-07-15 | 이구택 | Improved wet removing method of nitrogen oxide contained in exhaust gas |
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US4086327A (en) * | 1975-10-17 | 1978-04-25 | Agency Of Industrial Science & Technology | Process for removing nitrogen oxides from gaseous mixtures |
JPS56126431A (en) * | 1980-03-08 | 1981-10-03 | Nippon Soda Co Ltd | Wet type denitration method |
JPS57171424A (en) * | 1981-04-14 | 1982-10-22 | Fuji Kikai Kk | Removal of nitrogen oxides in gas |
US4839147A (en) * | 1985-04-05 | 1989-06-13 | Waagner-Biro Aktiengesellschaft | Method of purifying combustion product gases contaminated with dust and noxious gases |
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Publication number | Priority date | Publication date | Assignee | Title |
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KR100945520B1 (en) * | 2008-03-12 | 2010-03-09 | 엔텍이앤씨 주식회사 | Method for eliminating odorous gas |
KR102031210B1 (en) | 2018-05-02 | 2019-10-11 | 한국에너지기술연구원 | Apparatus and Method for Reduction of Hazardous Emission of Marine Engine |
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