KR100891231B1 - Reduction Reagent Solution For Restricting Production of Nitrous Oxide - Google Patents
Reduction Reagent Solution For Restricting Production of Nitrous Oxide Download PDFInfo
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- KR100891231B1 KR100891231B1 KR1020070008109A KR20070008109A KR100891231B1 KR 100891231 B1 KR100891231 B1 KR 100891231B1 KR 1020070008109 A KR1020070008109 A KR 1020070008109A KR 20070008109 A KR20070008109 A KR 20070008109A KR 100891231 B1 KR100891231 B1 KR 100891231B1
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- nitrous oxide
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- GQPLMRYTRLFLPF-UHFFFAOYSA-N Nitrous Oxide Chemical compound [O-][N+]#N GQPLMRYTRLFLPF-UHFFFAOYSA-N 0.000 title claims abstract description 36
- 239000001272 nitrous oxide Substances 0.000 title claims abstract description 12
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 11
- 239000003153 chemical reaction reagent Substances 0.000 title 1
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims abstract description 24
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims abstract description 14
- 239000004202 carbamide Substances 0.000 claims abstract description 14
- 239000000284 extract Substances 0.000 claims abstract description 11
- 239000010871 livestock manure Substances 0.000 claims abstract description 11
- 210000003608 fece Anatomy 0.000 claims abstract description 9
- 238000000034 method Methods 0.000 claims description 18
- 238000010531 catalytic reduction reaction Methods 0.000 claims description 3
- 230000002401 inhibitory effect Effects 0.000 claims description 2
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 abstract description 47
- 239000000463 material Substances 0.000 abstract description 11
- 239000007789 gas Substances 0.000 abstract description 6
- 238000002485 combustion reaction Methods 0.000 abstract description 4
- 239000003054 catalyst Substances 0.000 description 11
- 235000012054 meals Nutrition 0.000 description 7
- 238000002360 preparation method Methods 0.000 description 7
- 239000002699 waste material Substances 0.000 description 7
- 238000006243 chemical reaction Methods 0.000 description 5
- 150000002736 metal compounds Chemical class 0.000 description 5
- 229910021645 metal ion Inorganic materials 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 4
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 3
- 239000003638 chemical reducing agent Substances 0.000 description 3
- 238000006722 reduction reaction Methods 0.000 description 3
- 229910052708 sodium Inorganic materials 0.000 description 3
- 239000011734 sodium Substances 0.000 description 3
- 239000010457 zeolite Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 229910021536 Zeolite Inorganic materials 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- 239000003546 flue gas Substances 0.000 description 2
- ZFSLODLOARCGLH-UHFFFAOYSA-N isocyanuric acid Chemical compound OC1=NC(O)=NC(O)=N1 ZFSLODLOARCGLH-UHFFFAOYSA-N 0.000 description 2
- 229910052744 lithium Inorganic materials 0.000 description 2
- 244000144972 livestock Species 0.000 description 2
- 229910052700 potassium Inorganic materials 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- MGWGWNFMUOTEHG-UHFFFAOYSA-N 4-(3,5-dimethylphenyl)-1,3-thiazol-2-amine Chemical compound CC1=CC(C)=CC(C=2N=C(N)SC=2)=C1 MGWGWNFMUOTEHG-UHFFFAOYSA-N 0.000 description 1
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- BVCZEBOGSOYJJT-UHFFFAOYSA-N ammonium carbamate Chemical compound [NH4+].NC([O-])=O BVCZEBOGSOYJJT-UHFFFAOYSA-N 0.000 description 1
- 235000011114 ammonium hydroxide Nutrition 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- KXDHJXZQYSOELW-UHFFFAOYSA-N carbonic acid monoamide Natural products NC(O)=O KXDHJXZQYSOELW-UHFFFAOYSA-N 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- GDVKFRBCXAPAQJ-UHFFFAOYSA-A dialuminum;hexamagnesium;carbonate;hexadecahydroxide Chemical compound [OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[Mg+2].[Mg+2].[Mg+2].[Mg+2].[Mg+2].[Mg+2].[Al+3].[Al+3].[O-]C([O-])=O GDVKFRBCXAPAQJ-UHFFFAOYSA-A 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 229910001657 ferrierite group Inorganic materials 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 229910001701 hydrotalcite Inorganic materials 0.000 description 1
- 229960001545 hydrotalcite Drugs 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000005070 sampling Methods 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 238000003900 soil pollution Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 230000001629 suppression Effects 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 238000007669 thermal treatment Methods 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
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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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
- B01D47/06—Spray cleaning
-
- 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
- B01D53/79—Injecting reactants
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/20—Reductants
- B01D2251/206—Ammonium compounds
- B01D2251/2067—Urea
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/30—Alkali metal compounds
- B01D2251/304—Alkali metal compounds of sodium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/60—Inorganic bases or salts
- B01D2251/604—Hydroxides
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
- Y02C20/00—Capture or disposal of greenhouse gases
- Y02C20/10—Capture or disposal of greenhouse gases of nitrous oxide (N2O)
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
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- Biomedical Technology (AREA)
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- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Treating Waste Gases (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Abstract
본 발명은 연소로에서 배출되는 아산화질소(N2O)의 생성을 억제하기 위하여 사용되는 환원용액제재로서, 더욱 상세하게는 분뇨 추출액에 소량의 요소와 NaOH를 첨가, 혼합한 환원용액제재에 관한 것으로서 연소로에서 배출되는 배기 가스중의 질소산화물을 저감시키고, 아산화질소의 생성을 억제하는데 매우 효과적이다. The present invention relates to a reducing solution material used to suppress the production of nitrous oxide (N 2 O) discharged from a combustion furnace, and more particularly, to a reducing solution material in which a small amount of urea and NaOH are added and mixed with a manure extract. It is very effective in reducing nitrogen oxides in the exhaust gas discharged from the combustion furnace and suppressing the production of nitrous oxide.
아산화질소, 분뇨 추출액, 요소, NaOHNitrous oxide, manure extract, urea, NaOH
Description
도 1은 요소 용액만을 분무하였을때 반응온도 변화에 따라 N2O 생성양을 도시한 그래프이다.
도 2는 요소용액에 NaOH를 첨가하였을 때 반응온도 변화에 따라 N2O 생성양을 도시한 그래프이다. 1 is a graph showing the amount of N 2 O produced according to the change of reaction temperature when spraying only urea solution.
2 is a graph showing the amount of N 2 O produced according to the change in reaction temperature when NaOH was added to the urea solution.
본 발명은 선택적 무촉매 환원 공정에 사용되는 환원용액제재에 관한 것으로서, 더욱 상세하게는 분뇨 폐기물에 요소와 금속 이온을 첨가하여 제조한 선택적 무촉매 환원용액제재에 관한 것이다. The present invention relates to a reducing solution preparation used in a selective non-catalytic reduction process, and more particularly, to a selective non-catalyst reducing solution preparation prepared by adding urea and metal ions to a manure waste.
배기가스에 함유된 질소산화물(NOx)은 90% 이상의 일산화질소와 이산화질소 및 아산화질소로 구성되며, 지구온난화와 대기오염을 유발하는 대표적인 환경오염물질이다. 아산화질소의 경우 다양한 발생원을 갖고 있으나 그 중 화석연료의 연소로 발생되는 양이 증가하고 있는 추세이다. 아산화질소의 제거는 일반적으로 질소산화물 제거 기술로 혼용되어 사용되며 연소 후처리 기술인 촉매를 이용한 방법이 가장 많이 사용되어 왔다. Nitrogen oxide (NOx) contained in exhaust gas is composed of more than 90% nitrogen monoxide, nitrogen dioxide and nitrous oxide, and is a representative environmental pollutant that causes global warming and air pollution. Nitrous oxide has various sources, but the amount of nitrous oxide produced by the burning of fossil fuels is increasing. Nitrous oxide removal is generally used interchangeably as a technique for removing nitrogen oxides, and a method using a catalyst that is a combustion post-treatment technique has been most frequently used.
촉매를 이용하는 기술로는 하이드로탈사이트로부터 제조된 금속산화물 촉매에서 일산화탄소를 이용하는 기술 [등록특허 10-0654885], 다단촉매층으로 NO, NO2, N2O를 동시에 제거하는 방법 [공개특허 10-2005-0088774], 제올라이트를 촉매로 사용하는 방법 [공개특허 10-2004-0010605], 철담지 제올라이트를 이용하는 방법 [공개특허 10-2004-0015066], 페리어라이트에 칼륨과 나트륨을 담지한 촉매를 사용하는 방법 [미국특허 제6,682,710 B1], 철담지 제올라이트에 탄화수소를 이용하여 N2O를 제거하는 방법 [미국특허 제 6,872,372 B1]등이 있다. 촉매를 이용하는 기술은 일반적으로 효율은 높지만 설비 후단에 별도의 시설을 설치하여야 하고 고가의 촉매를 지속적으로 교체하여야 한다는 단점이 있다. 또한 N2O 생성과 동시에 배출되는 NO, NO2의 제거를 위하여 또 다른 NOx 제어기술을 사용하여야 한다는 단점을 갖는다. 따라서 질소산화물 제거기술중에 촉매를 사용하지 않으며 N2O 생성을 억제할 수 있으면 보다 우수한 저감기술이 될 수 있다.As a technique using a catalyst, a technique using carbon monoxide in a metal oxide catalyst prepared from hydrotalcite [patent 10-0654885], and a method of simultaneously removing NO, NO 2 and N 2 O with a multistage catalyst layer. -0088774], a method using zeolite as a catalyst [public patent 10-2004-0010605], a method using an iron-supported zeolite [public patent 10-2004-0015066], using a catalyst supporting potassium and sodium in ferrierite US Pat. No. 6,682,710 B1, US Pat. No. 6,872,372 B1, and the like to remove N 2 O using hydrocarbons in iron-supported zeolites. The technology using the catalyst is generally high efficiency, but has the disadvantage of having to install a separate facility at the rear of the facility and to continuously replace the expensive catalyst. In addition, there is a disadvantage that another NOx control technique should be used to remove NO and NO 2 discharged simultaneously with N 2 O generation. Therefore, if the catalyst is not used in the nitrogen oxide removal technology and the N 2 O production can be suppressed, it can be a better reduction technology.
촉매를 사용하지 않으며 질소산화물을 저감할 수 있는 기술로는 선택적 무촉매 환원공정이 있으며, 이 공정은 요소용액이나 암모니아수 또는 시아누릭산을 고온에 분무함으로써 질소산화물의 저감을 얻을 수 있다. 그러나 NOx 환원제로 사용되는 요소, 암모니아, 시아누릭산 모두 NOx 제거에는 효율적인 부분이 있으나 투입되는 환원제의 질소성분으로 인하여 N2O의 생성이 유도된다는 단점을 갖는다.A technique that can reduce nitrogen oxides without using a catalyst is a selective non-catalytic reduction process, which can reduce nitrogen oxides by spraying urea solution, ammonia water or cyanuric acid at high temperature. However, although urea, ammonia and cyanuric acid used as NOx reducing agents all have an efficient part for removing NOx, N 2 O is generated due to the nitrogen component of the reducing agent introduced.
이러한 문제를 해결하기 위하여 N2O를 저감하는 기술로 수화제(hydrolysis agent)를 이용하는 기술 [미국특허 제 5,543,123], 암모늄카바메이트를 이용하는 기술 [미국특허 제 4,997,631]이 있고, 아산화질소가 고온에서 분해되는 특성을 이용한 것으로 순환유동층 연소로에서 배출되는 가스내의 아산화질소를 920oC 이상으로 재가열 하는 열적처리 방법 [미국특허 제5,048,432]이 있다. 그러나 이러한 기술은 N2O의 저감은 가능하지만 반응이 일어나는 온도창이 좁거나, 가격이 고가이거나, NOx 제거효율이 낮아지거나, 또는 NH3 배출농도가 증가하거나 하는 문제점을 나타내게 되었다.In order to solve this problem, there is a technique using a hydrolysis agent (US Patent No. 5,543,123), a technique using an ammonium carbamate [US Patent No. 4,997,631] as a technology for reducing N 2 O, nitrous oxide is decomposed at high temperature There is a thermal treatment method [US Pat. No. 5,048,432] which reheats nitrous oxide in gas discharged from a circulating fluidized bed combustion furnace to 920 ° C. or more. However, this technique can reduce the N 2 O but presents problems such as narrow temperature window, high price, low NOx removal efficiency, or increased NH 3 emission concentration.
이에, 본 발명자들은 상기한 문제점들을 해결하고자, 폭넓은 온도범위에서 높은 NOx 저감율을 유지하며 동시에 N2O의 생성 억제가 가능한 새로운 N2O 생성 억제용 환원용액제재를 개발하였다. 즉, 본 발명자들은 폐기물로 처리되는 축산 분뇨로부터 추출한 용액에 소량의 금속 이온과 요소를 추가하여 700℃~1,100℃ 고온 영역에서 N2O의 생성 억제 효과가 우수한 환원용액제재를 완성하였다. 본 발명에 따르면, 배기가스중의 N2O와 환원용액제재내의 금속 이온이 반응하여 N2O가 N2로 전환됨으로써 N2O의 생성을 억제시킨다. 즉, 본 발명은 폐기물 처리나 폐수 처리 문제를 유발하는 축산 분뇨에 소량의 Na, Li, K 등의 금속 이온을 첨가하여 배기가스 내의 질소산화물 제거 효율이 높은 환원용액제재를 완성하였다.
본 발명은 폐기물 처리나 폐수 처리 문제를 유발하는 분뇨를 이용하여 넓은 온도 영역에서 N2O 생성을 억제할 수 있고, 가격이 저렴한 환원용액제재를 제공하는 것을 목적으로 한다. Thus, the present inventors to solve the above problems, the width has been developed a wide temperature range, new N 2 O produced a reducing solution for reducing material can maintain a high NOx reduction ratio, and at the same time suppressing generation of N 2 O in. That is, the present inventors added a small amount of metal ions and urea to the solution extracted from the livestock manure to be treated as waste to complete a reducing solution having excellent effect of suppressing the production of N 2 O in the high temperature region of 700 ° C to 1,100 ° C. According to the invention, thereby inhibiting the generation of N 2 O N 2 O by being converted to metal ions in the solution reduced materials and N 2 O in the exhaust gas is the reaction with N 2. That is, the present invention added a small amount of metal ions, such as Na, Li, K, to the livestock waste causing the waste treatment and wastewater treatment problems, thereby completing a reducing solution material having high efficiency of removing nitrogen oxides in the exhaust gas.
An object of the present invention is to provide a reducing solution material that can suppress the production of N 2 O in a wide temperature range by using manure that causes waste treatment or waste water treatment problems.
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본 발명의 환원용액제재는 축산 분뇨를 이용하여 추출한 용액을 주성분으로 하고, 이 추출액에 소량의 금속 화합물(예를 들어, NaOH)과 요소[(NH2)2CO]를 첨가, 혼합하여 이루어진다. 이때, 환원용액제재 전체 중량중 계분, 돈분, 축분과 같은 분뇨 추출액 함량이 1 ~ 95중량%이고, 상기 금속 화합물의 함량은 0.1 ~ 5중량%이며, 요소[(NH2)2CO]는 5 ∼ 50중량%인 것이 바람직하다.
먼저, 상기 분뇨 추출액은 계분(또는 돈분, 축분) 1 ∼ 50 중량%에 물을 혼합하여 상온에서 24시간 동안 교반기를 이용하여 교반한 후, 교반이 종결된 슬러리를 감압 필터링을 하여 부유물이 없는 추출액 상태로 얻는다.
또한, 상기 금속 화합물은 Na, Li, Fe, Zn, Ba, K 및 Mg 등의 금속 이온을 포함하는 금속 화합물이 바람직한데, 이러한 금속 화합물의 예로서는 NaOH를 들 수 있다. The reducing solution preparation of the present invention comprises a solution extracted using livestock manure as a main component, and a small amount of a metal compound (for example, NaOH) and urea [(NH 2 ) 2 CO] are added and mixed with the extract. At this time, the manure extract content of the total weight of the reducing solution, such as pig meal, pig meal, shaft meal is 1 to 95% by weight, the content of the metal compound is 0.1 to 5% by weight, urea [(NH 2 ) 2 CO] is 5 It is preferable that it is-50 weight%.
First, the manure extract is stirred with a stirrer for 24 hours at room temperature by mixing water to 1 to 50% by weight (or pig meal, shaft meal) using a stirrer, filtered under reduced pressure to extract the suspension without floating Get in the state.
In addition, the metal compound is preferably a metal compound containing metal ions such as Na, Li, Fe, Zn, Ba, K and Mg. Examples of such metal compounds include NaOH.
이와 같은 구성의 본 발명에 따른 환원용액제재를 제조하는 과정을 상세하게 설명하면 다음과 같다. Referring to the process for producing a reducing solution preparation according to the invention of such a configuration in detail as follows.
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먼저, 분뇨 추출액을 제조하기 위하여 계분(또는 돈분, 축분)을 1 ∼ 50 중량%로 물과 혼합하여 상온에서 24시간 교반기를 이용하여 교반한다. 교반이 종결된 슬러리를 감압 필터링하여 부유물이 없는 추출액을 얻는다. 이 추출액 1 ~ 95중량%에 물 10 ∼ 90중량%, 요소 5 ∼ 50중량% 및 NaOH 0.1 ∼ 5중량%를 첨가하여 최종 환원용액제재를 완성하였다.First, in order to prepare the manure extract, the system powder (or pig meal, shaft meal) is mixed with water at 1 to 50% by weight and stirred using a stirrer at room temperature for 24 hours. The stirred slurry is filtered under reduced pressure to obtain an extract free of suspended solids. 10 to 90% by weight of water, 5 to 50% by weight of urea and 0.1 to 5% by weight of NaOH were added to 1 to 95% by weight of the extract to complete the final reducing solution preparation.
본 발명에 따른 질소산화물 저감용 환원용액제재는 온도구간 700℃~1,100℃ 에서 질소산화물의 저감과 아산화질소의 생성 억제를 가능하게할 뿐만 아니라 분뇨 폐기물에 의한 토양 오염이나 수질 오염과 같은 이차 오염을 줄일수 있어 환경오염 방지에 매우 효과적이다. The reducing solution preparation for reducing nitrogen oxides according to the present invention not only enables the reduction of nitrogen oxides and the suppression of nitrous oxide production in the temperature range of 700 ° C. to 1,100 ° C., but also reduces secondary pollution such as soil pollution or water pollution by manure waste. It is very effective in preventing environmental pollution.
이하, 본 발명을 실시예에 근거하여 더욱 상세하게 설명하겠는바, 본 발명이 이러한 실시예에 의해 한정되는 것은 아니다.Hereinafter, the present invention will be described in more detail with reference to Examples, but the present invention is not limited to these Examples.
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[실시예 1] Example 1
계분과 물의 비율을 1:1로 조절한 후 상온에서 24시간 동안 공기와 접촉하지 않도록 밀폐를 유지하며 교반하였다. 교반 과정이 종결된 용액을 300㎛의 메쉬(mesh)로 여과하고, 그 여과액을 다시 원심분리기로 1,800rpm으로 20분간 작동시킨 후, 상등액을 취하여 계분 추출 원액을 제조하였다. 이 계분 추출 원액, 요소[(NH2)2CO], NaOH를 질량비로 각각 94:5:1로 혼합하여 최종적인 질소산화물 환원용액제재를 제조하였다.
[비교예 1]
물 95g과 요소 5g을 이용하여 환원용액제재를 제조하였다.
[실험 방법]
직경 0.2m, 길이 6m의 고온 내화재(Castable)와 SS304 도관으로 제작되고, LPG버너를 사용하여 내부 온도를 조절할 수 있는 반응기를 준비하였다. 이 반응기 내부에 배연 가스와 500 ppm 정도의 질소산화물을 공급하고, 반응기 측면에 설치된 노즐을 통해 상기 실시예 1 및 비교예 1에 의해 제조된 환원용액제재를 분무하였다.
이때, 반응기의 내부 온도는 750℃ ∼1,050℃로 조절되었다. 반응이 종결된 후, 반응기 내부의 배연 가스를 시료 채취관을 통하여 흡입하고, 가스분석기를 이용하여 N2O 농도 변화를 측정하여 도 1 및 도 2에 나타내었다.
도 1 및 도 2로부터 알 수 있는 바와 같이, 반응 온도 750℃ ∼1,050℃에서 비교예 1에 비해 실시예 1의 환원용액제재가 N2O 농도를 보다 효과적으로 저감시키고 있음을 확인할 수 있다. After adjusting the ratio of the system to water at 1: 1, the mixture was stirred while keeping it in contact with air at room temperature for 24 hours. After the stirring was terminated, the solution was filtered through a 300 μm mesh, and the filtrate was again operated by 1,800 rpm for 20 minutes using a centrifugal separator. The powdered extract extract, urea [(NH 2 ) 2 CO], and NaOH were mixed in a mass ratio of 94: 5: 1, respectively, to prepare a final nitrogen oxide reducing solution material.
Comparative Example 1
A reducing solution was prepared using 95 g of water and 5 g of urea.
[Experimental method]
A reactor made of a high temperature refractory (Castable) and SS304 conduit of 0.2m in diameter and 6m in length and using an LPG burner was prepared. Flue gas and about 500 ppm of nitrogen oxide were supplied into the reactor, and the reducing solution material prepared in Example 1 and Comparative Example 1 was sprayed through a nozzle installed at the side of the reactor.
At this time, the internal temperature of the reactor was adjusted to 750 ℃ to 1,050 ℃. After the reaction was completed, the flue gas inside the reactor was sucked through the sampling tube, and the change in N 2 O concentration was measured using a gas analyzer, and the results are shown in FIGS. 1 and 2.
As can be seen from FIGS. 1 and 2, it can be seen that the reducing solution preparation of Example 1 more effectively reduces the N 2 O concentration at the reaction temperature of 750 ° C to 1,050 ° C.
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본 발명에 따른 환원용액제재는 700℃~1,100℃에서 NOx 제거효율이 우수하고, N2O의 생성을 억제하는 효과를 얻을 수 있다. 또한, 본 발명의 환원용액제재는 축산 폐기물을 이용하여 제조되기 때문에 경제적일 뿐만 아니라 환경오염을 방지한다는 부가적인 이점을 가진다. 따라서, 본 발명의 환원용액제재는 각종 산업시설의 N2O 생성을 억제함과 동시에 NOx 정화용 환원제로 널리 활용될 수 있다.Reducing solution material according to the present invention is excellent in the NOx removal efficiency at 700 ℃ ~ 1,100 ℃, it is possible to obtain the effect of suppressing the production of N 2 O. In addition, the reducing solution material of the present invention has the additional advantage of being economical and preventing environmental pollution because it is manufactured using livestock waste. Therefore, the reducing solution material of the present invention can be widely used as a reducing agent for NOx purification while suppressing the production of N 2 O in various industrial facilities.
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