WO2011025209A2 - Composition for removing carbon dioxide generated during combustion - Google Patents

Composition for removing carbon dioxide generated during combustion Download PDF

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WO2011025209A2
WO2011025209A2 PCT/KR2010/005618 KR2010005618W WO2011025209A2 WO 2011025209 A2 WO2011025209 A2 WO 2011025209A2 KR 2010005618 W KR2010005618 W KR 2010005618W WO 2011025209 A2 WO2011025209 A2 WO 2011025209A2
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carbon dioxide
composition
fuel
generated during
oil
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French (fr)
Korean (ko)
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WO2011025209A3 (en
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정충의
정훈
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극동환경화학 주식회사
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation 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
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/46Removing components of defined structure
    • B01D53/62Carbon oxides
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B13/00Oxygen; Ozone; Oxides or hydroxides in general
    • C01B13/14Methods for preparing oxides or hydroxides in general
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation 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
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/77Liquid phase processes
    • B01D53/78Liquid phase processes with gas-liquid contact
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01FCOMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
    • C01F11/00Compounds of calcium, strontium, or barium
    • C01F11/18Carbonates
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2251/00Reactants
    • B01D2251/30Alkali metal compounds
    • B01D2251/304Alkali metal compounds of sodium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2251/00Reactants
    • B01D2251/40Alkaline earth metal or magnesium compounds
    • B01D2251/402Alkaline earth metal or magnesium compounds of magnesium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2251/00Reactants
    • B01D2251/40Alkaline earth metal or magnesium compounds
    • B01D2251/404Alkaline earth metal or magnesium compounds of calcium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2251/00Reactants
    • B01D2251/60Inorganic bases or salts
    • B01D2251/602Oxides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2251/00Reactants
    • B01D2251/60Inorganic bases or salts
    • B01D2251/604Hydroxides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/50Carbon oxides
    • B01D2257/504Carbon dioxide
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2258/00Sources of waste gases
    • B01D2258/02Other waste gases
    • B01D2258/0283Flue gases
    • 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

Definitions

  • the present invention relates to fuels used for the operation of heaters (boilers, warmers, etc.) and other devices (incinerators, generators, etc.), that is, oils (light oil, kerosene, LPG, bunker seed oil, etc.) and solid fuels (brown coal, lump coal, shell coal, Coal briquettes, wood, solidified fuel, palm fuel, etc.) relates to a composition for removing carbon dioxide generated during combustion to remove the carbon dioxide gas in the waste gas discharged to the flue and to prevent air pollution.
  • oils light oil, kerosene, LPG, bunker seed oil, etc.
  • solid fuels brown coal, lump coal, shell coal, Coal briquettes, wood, solidified fuel, palm fuel, etc.
  • a composition for removing carbon dioxide generated during combustion to remove the carbon dioxide gas in the waste gas discharged to the flue and to prevent air pollution.
  • NO X nitrogen oxides
  • SO X sulfur oxides
  • the gas causing the climate change has various emission paths, and the CO 2 gas emitted through the combustion of fossil fuels contains about 90wt% of carbon based on the liquid fuel although the carbon content in each fuel is different. Therefore, CO 2 gas generated in the combustion process of fossil fuel is discharged in an amount corresponding to 3.3 times ⁇ (44/12) ⁇ 0.9 ⁇ of the used fuel, considering the stoichiometric ratio of the combustion reaction. As shown, it accounts for 58% of the total climate change-causing gas.
  • the countermeasure against climate change-inducing gas is centered on the reduction of CO 2 gas emitted through the combustion of fossil fuel.
  • CO 2 gas emission suppression is applicable to alternative energy technologies, CO 2 gas treatment technology Is divided into separate recovery practical technology and practical resource recycling technology.
  • An active way to curb CO 2 emissions is to develop alternative energy sources without burning fossil fuels using solar, tidal, hydro, geothermal, biomass, nuclear fission and fusion technologies. To improve technology, increase power generation efficiency, and develop technology to separate, recover and convert CO 2 gas.
  • the technique of immobilization in the inside is likely to cause a second environmental destruction, and the technique of artificially immobilizing the emitted CO 2 gas by using a chemical catalyst, a biological immobilization, an electrochemical immobilization, a photochemical immobilization, and a photocatalyst is a perfect technique. The implementation is not established.
  • the method of immobilizing and treating CO 2 gas is also known, and the immobilization technology is largely proceeded by biological treatment and chemical treatment.
  • Electrolysis of CO 2 gas or the use of catalysts to produce methane, methanol, etc. requires additional separation and recovery processes to maintain the purity of CO 2 when treating flue gas. Therefore, there is a problem that it is not suitable for use in the actual process.
  • the process of biologically treating CO 2 gas has the problem that the reaction rate is very slow and there is a high possibility of causing another environmental problem such as the temperature rise of sea water.
  • these methods are still laboratory-scale processes in large buildings or industrial facilities. There is a problem in that it is not suitable for treating CO 2 gas emitted from a large process such as a boiler, a large incineration plant.
  • the present invention is to solve the above problems
  • the greenhouse effect is further reduced by more effectively removing or reducing CO2 gas contained in flue gas from large buildings, industrial boilers, or incineration facilities that use fossil fuel as the main fuel.
  • the purpose is to contribute to the prevention of warming.
  • the above object is characterized by comprising "adding and mixing 0.25% of sodium hydroxide as a reaction agent and 2.25% of magnesium oxide as a reaction delay agent in 97.50% of calcium hydroxide aqueous solution prepared by dissolving water in quicklime of calcium oxide.” It can be achieved.
  • Application of the present invention improves the quality of life because the problem of air pollution due to the exhaust gas generated during combustion is significantly improved, improve the public's awareness of the environment according to the development of clean technology, the use of oil Can fundamentally change the negative perception of boiler or incinerator installations,
  • the present invention removes carbon dioxide generated during combustion, comprising 97.50% of calcium hydroxide aqueous solution prepared by dissolving water in quicklime, which is calcium oxide, by adding 0.25% of sodium hydroxide as a reaction accelerator and 2.25% of magnesium oxide as a reaction retardant.
  • compositions for the following are disclosed.
  • composition for removing the carbon dioxide generated during the combustion of the present invention will be described in detail with respect to the composition for removing the carbon dioxide generated during the combustion of the present invention.
  • composition of the composition for removing the carbon dioxide generated during combustion of the present invention is added to 97.50% of calcium hydroxide aqueous solution prepared by dissolving water in calcium oxide quicklime, 0.25% of sodium hydroxide as a reaction agent and 2.25% of magnesium oxide as a reaction retardant. It is made by mixing.
  • the present invention relates to fuels used for the operation of heaters (boilers, warmers, etc.) and other devices (incinerators, generators, etc.), that is, oils (light oil, kerosene, LPG) and solid fuels (brown coal, coal coal, coal briquettes, wood)
  • oils light oil, kerosene, LPG
  • solid fuels brown coal, coal coal, coal briquettes, wood
  • the calcium hydroxide aqueous solution reacts rapidly with carbon dioxide and removes carbon dioxide while controlling the reaction rate by adding magnesium oxide, a reaction retardant, to solve the economic inefficiency caused by the rapid progress of the sodium hydroxide transient reaction.
  • magnesium oxide a reaction retardant
  • Chemical reaction with carbon dioxide is performed by the calcium hydroxide and sodium hydroxide to generate insoluble calcium carbonate particles, thereby removing carbon dioxide.
  • the chemical reaction is as follows.
  • Kyungin Environment Co., Ltd. the principal company and the consignment agency, introduced the present invention into a device installed at the Songdo Cheongna Incinerator, respectively, and published test data on the amount of carbon dioxide generated from March 19 to March 22, 2010 in Table 2 below. Same as
  • Table 2 shows the data measured by the applicant.
  • Table 3 shows data measured by Kyungin Environment Co., Ltd., a consignment agency.
  • the measurement of the amount of carbon dioxide generated at the measurement point of the front end and the measurement point at the rear end was measured twice at the Kyungin Environment Co., Ltd. three times, respectively. It is 8.33% and the average carbon dioxide concentration measured at the next stage is 6.70% and the total CO2 removal efficiency is 19.60%, which is very effective compared to the existing CO2 removal rate.
  • the measured results in Kyungin Environment Co., Ltd. were 2.06% of the average carbon dioxide concentration measured at the front end measurement point and 0.00% of the average concentration of the carbon dioxide at the downstream end measured point.
  • test report according to Table 4 is represented by the image in FIG.
  • it may contain 20PPM of red dye.
  • red indicator phenolphthalein when reacted with carbon dioxide in the state of adding red indicator phenolphthalein to alkaline calcined pH 11 The slaked lime is changed to neutral pH of about 8 and the phenolphthalein is colorless so that it is possible to grasp the extent of carbon dioxide removal by the color change of the indicator, which is a known technique.
  • composition for removing carbon dioxide generated by combustion of the present invention when the composition for removing carbon dioxide generated by combustion of the present invention is combined with carbon dioxide contained in the waste gas, carbon dioxide is removed or reduced, thereby solving problems such as environmental pollution and greenhouse effect.
  • the present invention relates to fuels used for the operation of heaters (boilers, warmers, etc.) and other devices (incinerators, generators, etc.), that is, oils (light oil, kerosene, LPG, bunker seed oil, etc.) and solid fuels (brown coal, lump coal, shell coal, Coal briquettes, wood, solidified fuel, palm fuel, etc.) are burned and a composition for removing carbon dioxide generated during combustion to remove the carbon dioxide gas in the waste gas discharged to the flue to prevent air pollution,
  • oils light oil, kerosene, LPG, bunker seed oil, etc.
  • solid fuels brown coal, lump coal, shell coal, Coal briquettes, wood, solidified fuel, palm fuel, etc.
  • the quality of life is greatly improved due to the significant improvement of the air pollution caused by the generated exhaust gas, and the development of clean technology raises the public's awareness of the environment, and the negative perception of installing oil-fired boilers or incinerators.

Abstract

The present invention relates to a composition for removing carbon dioxide generated during combustion, which removes carbon dioxide from the waste gas generated when fuel used for operating a heater (boiler, fan heater, etc.) and other apparatuses (incinerator, generator, etc.), that is, oil (light oil, lamp oil, LPG, bunker C oil, etc.) and solid fuel (brown coal, lump coal, briquettes, molded charcoal, lumber, solidified fuel, palm kernel shell fuel, etc.) are burnt, and discharged through a flue, so as to prevent atmospheric contamination. The composition of the present invention is prepared by adding and mixing 0.25% of sodium hydroxide serving as a reaction persisting agent and 2.25% of magnesium oxide serving as a reaction retardant with 97.50% of calcium hydroxide solution prepared by dissolving burned lime, which is calcium oxide, into water. The composition of the present invention removes carbon dioxide generated during combustion to increase the quantity of heat, and reduces the amount of carbon dioxide emitted to the atmosphere to prevent global warming caused by the greenhouse effect.

Description

연소시 발생되는 이산화탄소를 제거하기 위한 조성물Composition for removing carbon dioxide generated during combustion
본 발명은 난방기(보일러, 온풍기 등) 및 기타 장치(소각로, 발전기 등)의 가동을 위하여 사용되는 연료 즉 유류(경유, 등유, LPG, 벙커씨유 등) 및 고체연료(갈탄, 괴탄, 조개탄, 성형탄, 목재, 고형화 연료, 팜연료 등)가 연소되고 연도로 배출되는 폐가스중에 있는 이산화탄소가스를 제거하여 대기오염을 방지할 수 있도록 한 연소시 발생되는 이산화탄소를 제거하기 위한 조성물에 관한 것이다.The present invention relates to fuels used for the operation of heaters (boilers, warmers, etc.) and other devices (incinerators, generators, etc.), that is, oils (light oil, kerosene, LPG, bunker seed oil, etc.) and solid fuels (brown coal, lump coal, shell coal, Coal briquettes, wood, solidified fuel, palm fuel, etc.) relates to a composition for removing carbon dioxide generated during combustion to remove the carbon dioxide gas in the waste gas discharged to the flue and to prevent air pollution.
최근, 폭발적인 인구의 증가, 자동차산업을 포함한 각종 산업의 발달 및 화석연료를 주연료로 사용하는 제반 인간활동에 의하여 대기중으로 방출되는 CO2가스의 양이 급증하고 있으며, 이와 같이 대기중으로 배출된 CO2가스는 수증기 및 기타 인간활동에 의하여 배출되는 CH4, N2O, 할로겐화 탄소 등과 함께 대기권 상층부에 정체되면서 온실효과를 유발시키고, 이와 같은 온실효과는 해수의 온도를 상승시켜 예측 불가능한 기후변화를 초래하게 된다.In recent years, the amount of CO 2 gas released into the atmosphere is rapidly increasing due to the explosive increase in population, the development of various industries including the automobile industry, and human activities using fossil fuel as the main fuel. 2 The gases, together with CH 4 , N 2 O and carbon halides, released by water vapor and other human activities, stagnate in the upper atmosphere, causing a greenhouse effect, which increases the temperature of the seawater and thus creates unpredictable climate change. Will result.
또한, 석탄, 석유와 같은 화석연료의 연소과정에서 온실효과를 유발시키는 CO2가스 이외에 상당량의 질소산화물(NOX) 및 황산화물(SOX)가 발생되는 데, 이들은 산성비 및 오존과 같은 광화학 스모그 문제를 유발하여 인간 및 자연생태계에 악영향을 초래하고 있다.In addition, in the combustion of fossil fuels such as coal and petroleum, a significant amount of nitrogen oxides (NO X ) and sulfur oxides (SO X ) are generated in addition to the CO 2 gas that causes the greenhouse effect. These are photochemical smog such as acid rain and ozone. It causes problems and adversely affects human and natural ecosystems.
이와 같이 기후변화를 유발시키는 가스는 배출경로가 다양한 데, 이중 화석연료의 연소를 통해 배출되는 CO2가스는 각 연료중의 탄소함량이 다르긴 하나 액체연료를 기준으로 약 90wt%의 탄소성분을 포함하고 있으므로 화석연료의 연소과정에서 발생되는 CO2가스는 연소반응 양론비를 고려할 때, 사용연료의 3.3배{(44/12)×0.9}에 해당하는 양으로 배출되며, 이 양은 다음 표 1에서 나타난 바와 같이 전체 기후변화 유발 가스량의 58%를 차지한다.As such, the gas causing the climate change has various emission paths, and the CO 2 gas emitted through the combustion of fossil fuels contains about 90wt% of carbon based on the liquid fuel although the carbon content in each fuel is different. Therefore, CO 2 gas generated in the combustion process of fossil fuel is discharged in an amount corresponding to 3.3 times {(44/12) × 0.9} of the used fuel, considering the stoichiometric ratio of the combustion reaction. As shown, it accounts for 58% of the total climate change-causing gas.
표 1 배출원별 온실가스 배출기여도
배출원 기여도
화석연료(석탄,석유,천연가스 등) 58%
산업(시멘트 등) 4%
농업(신진대사, 농경지, 목축 등) 18%
임업(벌채, 토지이용 변화 등) 17%
폐기물(쓰레기, 하수, 매립지 등) 3%
합 계 100%
Table 1 GHG Emissions by Source
Source Contribution
Fossil fuels (coal, oil, natural gas, etc.) 58%
Industry (cement, etc.) 4%
Agriculture (metabolism, farmland, livestock, etc.) 18%
Forestry (logging, land use change, etc.) 17%
Waste (garbage, sewage, landfill, etc.) 3%
Sum 100%
(자료: 그린피스, 'Fossil Fuels and Climate Protection : Carbon Logic'(1997)(Source: Greenpeace, 'Fossil Fuels and Climate Protection: Carbon Logic' (1997)
이에 따라서, 기후변화 유발 가스 대책은 화석연료의 연소를 통하여 배출되는 CO2가스의 저감방안이 중심을 이룬다.Accordingly, the countermeasure against climate change-inducing gas is centered on the reduction of CO 2 gas emitted through the combustion of fossil fuel.
상기한 CO2를 비롯한 각종 배기가스에 의하여 초래되는 기후의 이상변화가 지구상의 환경문제 중 인류에 미치는 영향범위가 가장 클 것으로 예견되고 있는 주요 사안으로 대두됨에 따라, 최근 기후변화와 관련하여 국제적 인 대처방안이 마련되고 있다.As climate change caused by various kinds of exhaust gas such as CO 2 is raised as a major issue that is expected to have the greatest impact on humankind among the global environmental problems, the recent international Countermeasures are being prepared.
이와 같은 국제적인 대처방안의 일환으로서, 1992년 6월 리우 UN환경개발회의에서 기후변화협약이 채택된 이래 1997년 12월 교토 제 3차 당사국 회의에서는 2008∼2012년 온실가스배출량을 1990년 대비 유럽연합(EU)8%, 미국 7%, 일본 6% 씩 감축하는 것을 비롯하여 총 38개국이 평균 5.2%를 줄이고, 1백 30여 개발도상국은 자발적으로 감축에 참여할 것을 촉구하는 「교토의정서」를 채택하였으며, 국가간의 배출권 거래 등을 허용하는 유연성 체제가 확립되었다.As part of this international response, the third meeting of the governing bodies in Kyoto in December 1997, compared with the EU in 2008-2012, was adopted at the third meeting of the Kyoto Parties in December 1997, since the climate change convention was adopted at the Rio UN Environmental Development Conference in June 1992. A total of 38 countries reduced 5.2%, including an 8% reduction in the United States, 7% in the United States, and 6% in Japan, and more than 130 developing countries adopted the Kyoto Protocol, which calls for voluntary reductions. In other words, a flexible regime has been established that allows trade in emissions rights between countries.
한편, 철강, 석유화학 등 에너지 다소비형 산업구조인 우리나라의 경우, 최근 10년간 CO2가스의 배출량 증가율이 연간 10%로 세계 1위를 보이고 있으며 큰 변화가 없다면 2010년 CO2가스의 배출량은 1990년 대비 3.3배가 될 것으로 전망되고 있다.On the other hand, if the country somewhat-free industrial structure, steel, petrochemical, energy, emissions growth rate of the past 10 years CO 2 gas is showing the world first place with 10% per year, and there is no significant change in emissions of CO 2 gas 2010 1990 It is expected to be 3.3 times that of the year.
특히, 경제기반이 취약한 동유럽국가들이 의무감축 대상인 점을 감안하면, 비록 1998년 11월 부에노스아이레스의 4차 총회에서 협약가입이 성시되지 않았다고하여도 OECD회원국인 우리나라에서는 곧 국제사회의 압력을 수용하지 않을 수 없는 절박한 상황이다.In particular, considering that European countries with weak economic bases are subject to mandatory reductions, the OECD, even though the signing of the Convention at the Fourth General Assembly in Buenos Aires in November 1998, did not accept the pressure of the international community. It's a desperate situation.
이와 같은 국제사회의 압력에 의하여 협약에 가입하는 경우에, 1990년 배출수준으로 CO2가스배출 감출목표가 설정된다면, 2010년 기준 CO2가스 배출량의 약 70% 감축이 이루어져야 하므로 장기적인 적절한 대응책이 준비되지 못할 경우IMF체제 이상으로 심각한 경제위기에 직면하게 될 것으로 전망된다.In the case of such acceded to the Convention by the pressure of the international community, if the 1990 emissions level in CO 2 emissions conceal goal setting, of 2010, the CO 2 must be made 70% reduction of gas emissions, so be prepared a long-term adequate countermeasures Failure to do so is likely to face a serious economic crisis beyond the IMF system.
한편, CO2가스의 배출을 저감시킬 수 있는 기술은 크게 CO2가스 배출억제기술과 CO2가스 처리기술로 구분되는 데, CO2가스 배출억제는 에너지 대체기술에 해당되며, CO2가스 처리기술은 분리회수 실용화기술과실용자원화 기술로 세분화된다.On the other hand, to which can reduce the emission of CO 2 gas technique is largely separated by a CO 2 gas emission suppression techniques and CO 2 gas treatment technology, CO 2 gas emission suppression is applicable to alternative energy technologies, CO 2 gas treatment technology Is divided into separate recovery practical technology and practical resource recycling technology.
CO2가스의 배출을 억제하는 적극적인 방법은 태양에너지, 조력, 수력, 지열, 바이오매스, 핵분열 및 핵융합기술을 이용하여 화석연료를 연소시키지 않고도 대체 에너지원을 개발하는 것이며, 소극적인 방법은 에너지 효율을 개선하고, 발전효율을 증대시키며, CO2가스를 분리·회수·변환하는 기술을 개발하는 것이다.An active way to curb CO 2 emissions is to develop alternative energy sources without burning fossil fuels using solar, tidal, hydro, geothermal, biomass, nuclear fission and fusion technologies. To improve technology, increase power generation efficiency, and develop technology to separate, recover and convert CO 2 gas.
한편, 배출된 CO2가스를 흡착, 흡수, 막분리하는 기술은 현재의 기술 수준으로 보아 규모와 경제적인 측면에서 부정적인 견해가 많으며, 배출된 CO2가스를 임야 및 해양플랑크톤, 심해흡수 등과 같이 자연계 내에서 고정화 시키는 기술은 제 2의 환경파괴를 초래할 우려가 높고, 화학적 촉매, 생물학적 고정화, 전기화학적 고정화, 광화학적 고정화, 광촉매 등을 이용하여 배출된 CO2가스를 인공적으로 고정화시키는 기술은 완벽한 기술 구현이 확립되지 않고 있는 실정이다.On the other hand, the adsorption, separation absorbed, just a discharged CO 2 gas technology, natural world, such as seen with the current technological level of scale and often have a negative opinion on the economic side, the exhaust CO 2 gas forest and marine plankton, deep absorption The technique of immobilization in the inside is likely to cause a second environmental destruction, and the technique of artificially immobilizing the emitted CO 2 gas by using a chemical catalyst, a biological immobilization, an electrochemical immobilization, a photochemical immobilization, and a photocatalyst is a perfect technique. The implementation is not established.
디모토 토시타케(Dmoto Toshitake)에 따르면, CO2가스의 회수 및 심해 저장기술, 회수 및 화학적 유효 이용기술, 회수 및 생물학적 유효이용기술, 대규모 녹화기술은 세계적인 중심기술로 평가되고 있다.According to de moto Toshio frondosa (Dmoto Toshitake), collected and stored deep-sea technology, chemical recovery and utilization technology, biological recovery and effective utilization technique, a large-scale recording technique of CO 2 gas is being evaluated as a global center technology.
우리나라의 경우, 배출된 CO2가스를 분리시키기 위하여 흡수법, 흡착법, 막분리기술 등이 연구되고 있고, 촉매환원법, 화학적 전환기술들을 중심으로 기초연구가 수행되고 있으며, 광촉매를 이용하여 처리하는 기술은 최근에 점진적으로 연구되고 있으나, 아직 전자빔을 이용하는 방식은 개발되어 있지 않은 실정이다.In Korea, absorption method, adsorption method, and membrane separation technology have been studied to separate the discharged CO 2 gas, and basic research has been carried out based on catalytic reduction method and chemical conversion technology. Recently, although gradually researched, a method using an electron beam has not been developed yet.
CO2가스를 고정화시켜 처리하는 방식도 알려져 있는 바, 고정화 기술은 크게 생물학적 처리와 화학적인 처리방법으로 진행되고 있다.The method of immobilizing and treating CO 2 gas is also known, and the immobilization technology is largely proceeded by biological treatment and chemical treatment.
CO2가스를 전기분해하거나 촉매를 이용하여 메탄, 메탄올 등을 만드는 방식은 실제 배가스를 처리할 때 CO2의 순도를 유지하기 위하여 부가적인 분리, 회수공정이 필요하다. 따라서 실제공정에 사용하기에는 부적합하다는 문제가 있다.Electrolysis of CO 2 gas or the use of catalysts to produce methane, methanol, etc. requires additional separation and recovery processes to maintain the purity of CO 2 when treating flue gas. Therefore, there is a problem that it is not suitable for use in the actual process.
또한, CO2가스를 생물학적으로 처리하는 공정은 반응속도가 매우 느리고 해수의 온도상승 등 또 다른 환경문제를 일으킬 가능성이 크다는 문제가 있으며, 게다가 이러한 방식들은 아직 실험실 규모의 공정으로서 대형 빌딩이나 산업시설의 보일러, 대규모의 소각설비 등과 같은 대단위 공정에서 배출되는 CO2가스를 처리하기에는 부적합하다는 문제가 있다.In addition, the process of biologically treating CO 2 gas has the problem that the reaction rate is very slow and there is a high possibility of causing another environmental problem such as the temperature rise of sea water. Furthermore, these methods are still laboratory-scale processes in large buildings or industrial facilities. There is a problem in that it is not suitable for treating CO 2 gas emitted from a large process such as a boiler, a large incineration plant.
본 발명은 상기의 문제점을 해결하기 위한 것으로서,The present invention is to solve the above problems,
화석연료를 주연료로 사용하는 대형 빌딩이나 산업시설의 보일러 또는 대규모 소각시설로부터 발생되는 배연가스중에 포함된 CO2가스를 대기로 배출되기 전단계에서 보다 효과적으로 제거 또는 감소시킴으로서 더욱 나아가서는 온실효과에 의한 지구온난화 예방에 기여하고자 하는데 그 목적이 있는 것이다.In addition, the greenhouse effect is further reduced by more effectively removing or reducing CO2 gas contained in flue gas from large buildings, industrial boilers, or incineration facilities that use fossil fuel as the main fuel. The purpose is to contribute to the prevention of warming.
상기와 같은 목적을 달성하기 위한 구체적인 해결적 수단은,Specific solution means for achieving the above object,
"산화칼슘인 생석회에 물을 용해시켜서 제조된 수산화칼슘 수용액 97.50%에 반응지속제인 수산화나트륨 0.25%와 반응지연제인 산화마그네슘 2.25%을 첨가혼합하여 이루어진 것"을 그 구성적 특징으로 함으로서 상기의 목적을 달성할 수 있는 것이다.The above object is characterized by comprising "adding and mixing 0.25% of sodium hydroxide as a reaction agent and 2.25% of magnesium oxide as a reaction delay agent in 97.50% of calcium hydroxide aqueous solution prepared by dissolving water in quicklime of calcium oxide." It can be achieved.
본 발명을 적용하면, 연소시 발생되는 배기가스로 인한 대기오염문제가 현저하게 개선되기 때문에 삶의 질이 향상되며, 청정기술의 개발에 따라 환경에 대한 일반 대중의 인식도를 앙양시키게 되고, 유류사용 보일러나 소각로 설치에 대한 부정적인 인식을 근본적으로 변화시킬 수 있으며,Application of the present invention improves the quality of life because the problem of air pollution due to the exhaust gas generated during combustion is significantly improved, improve the public's awareness of the environment according to the development of clean technology, the use of oil Can fundamentally change the negative perception of boiler or incinerator installations,
특히, 대기중에 방출되는 이산화탄소량을 저감함으로써 온실효과에 의한 지구온난화 예방에 기여하는 효과가 있다.In particular, by reducing the amount of carbon dioxide emitted into the atmosphere there is an effect that contributes to the prevention of global warming due to the greenhouse effect.
도 1은 이산화탄소 제거를 위한 흐름도1 is a flow chart for carbon dioxide removal
도 2는 본 발명에 의한 이산화탄소 제거 효율성을 증명하기 위한 시험성적서2 is a test report for demonstrating the carbon dioxide removal efficiency according to the present invention
본 발명은 산화칼슘인 생석회에 물을 용해시켜서 제조된 수산화칼슘 수용액 97.50%에 반응지속제인 수산화나트륨 0.25%와 반응지연제인 산화마그네슘 2.25%을 첨가혼합하여 이루어진 것을 특징으로 하는 연소시 발생되는 이산화탄소를 제거하기 위한 조성물을 개시한다.The present invention removes carbon dioxide generated during combustion, comprising 97.50% of calcium hydroxide aqueous solution prepared by dissolving water in quicklime, which is calcium oxide, by adding 0.25% of sodium hydroxide as a reaction accelerator and 2.25% of magnesium oxide as a reaction retardant. Disclosed are compositions for the following.
이하 본 발명인 연소시 발생되는 이산화탄소를 제거하기 위한 조성물에 대하여 구체적으로 설명하고자 한다.Hereinafter will be described in detail with respect to the composition for removing the carbon dioxide generated during the combustion of the present invention.
본 발명인 연소시 발생되는 이산화탄소를 제거하기 위한 조성물의 구체적인 구성은, 산화칼슘인 생석회에 물을 용해시켜서 제조된 수산화칼슘 수용액 97.50%에 반응지속제인 수산화나트륨 0.25%와 반응지연제인 산화마그네슘 2.25%을 첨가혼합하여 이루어진 것이다.Specific composition of the composition for removing the carbon dioxide generated during combustion of the present invention is added to 97.50% of calcium hydroxide aqueous solution prepared by dissolving water in calcium oxide quicklime, 0.25% of sodium hydroxide as a reaction agent and 2.25% of magnesium oxide as a reaction retardant. It is made by mixing.
이하 구체적으로 설명하면,In more detail below,
본 발명은 난방기(보일러, 온풍기 등) 및 기타 장치(소각로, 발전기 등)의 가동을 위하여 사용되는 연료 즉 유류(경유, 등유, LPG) 및 고체연료(갈탄, 괴탄, 조개탄, 성형탄, 목재)가 연소되고 연도로 배출되는 폐가스중에 함유되어 있는 이산화탄소를 효과적으로 제거하기 위한 조성물을 제공하기 위한 것으로, 여러가지 시험을 거쳐서 이산화탄소를 제거하기 위해서 수산화칼슘 수용액 97.50%에 반응지속제인 수산화나트륨 0.25%와 반응이 너무 빨리 발생됨에 따른 문제점을 해소하기 위해서 반응지연제인 산화마그네슘 2.25%를 포함시킨다.The present invention relates to fuels used for the operation of heaters (boilers, warmers, etc.) and other devices (incinerators, generators, etc.), that is, oils (light oil, kerosene, LPG) and solid fuels (brown coal, coal coal, coal briquettes, wood) To provide a composition for effectively removing the carbon dioxide contained in the waste gas which is combusted and discharged to the flue, the reaction is too fast with 0.25% sodium hydroxide solution 97.50% to remove carbon dioxide through various tests. In order to solve the problem caused by the occurrence of the reaction delaying agent, magnesium oxide 2.25% is included.
즉, 수산화칼슘 수용액은 이산화탄소와 신속하게 반응을 하고, 수산화나트륨 과도 반응을 급격하게 진행됨에 따른 경제적인 비효율성을 해소하기 위해 반응지연제인 산화마그네슘을 추가 함유하여 반응의 속도를 조절하면서 이산화탄소를 제거함으로서 정제효과를 향상시킬 수 있는 장점이 있다.In other words, the calcium hydroxide aqueous solution reacts rapidly with carbon dioxide and removes carbon dioxide while controlling the reaction rate by adding magnesium oxide, a reaction retardant, to solve the economic inefficiency caused by the rapid progress of the sodium hydroxide transient reaction. There is an advantage that can improve the purification effect.
상기 수산화칼슘과 수산화나트륨에 의해서 이산화탄소와 화학반응을 하여 불용성의 탄산칼슘입자를 생성하게 되며, 이를 제거함으로서 이산화탄소를 제거할 수 있다. 그 화학반응은 하기식과 같다.Chemical reaction with carbon dioxide is performed by the calcium hydroxide and sodium hydroxide to generate insoluble calcium carbonate particles, thereby removing carbon dioxide. The chemical reaction is as follows.
Ca(OH)2 + CO2 →CaCO3 + H2OCa (OH) 2 + CO 2 → CaCO 3 + H 2 O
즉, 칼슘이온이 이산화탄소와 반응하여 불용성 탄산칼슘이 생성되며, 반응 지속제인 수산화나트륨(NaOH)에 의해 반응지속현상과 반응지연제인 산화마그네슘(MgO)에 의해 반응지연현상을 동시에 발생함으로서 일정속도를 유지하면서 반응토록 하는 것이다.In other words, calcium ions react with carbon dioxide to form insoluble calcium carbonate, and the reaction delay phenomenon is caused simultaneously by the sodium hydroxide (NaOH) as the reaction continuity and the reaction delay phenomenon by the magnesium oxide (MgO) as the reaction delayer. It keeps reacting.
이에 대하여 본원인과 위탁기관인 주식회사 경인환경이 각각 송도청라소각장에 설치된 장치에 본 발명을 투입하여 2010년 3월 19일부터 3월 22일까지 이산화탄소의 발생량에 대한 시험데이터를 표 2 에 게재하면 다음과 같다.With respect to this, Kyungin Environment Co., Ltd., the principal company and the consignment agency, introduced the present invention into a device installed at the Songdo Cheongna Incinerator, respectively, and published test data on the amount of carbon dioxide generated from March 19 to March 22, 2010 in Table 2 below. Same as
표 2는 본원인에 의해 자체 측정한 데이터이다.Table 2 shows the data measured by the applicant.
표 2
번호 O2 CO T(℃) CO2(전단) CO2(후단) 제거효율 비고
1 5.60 % 14 ppm 207 8.70 %
2 6.30 % 11 ppm 207 8.20 %
3 6.50 % 10 ppm 206 8.10 %
4 8.80 % 10 ppm 165 6.90 %
5 9.10 % 10 ppm 157 6.60 %
6 9.30 % 10 ppm 153 6.60 %
CO2평균농도 8.33 % 6.70 %
CO2제거효율 19.60 %
TABLE 2
number O 2 CO T (℃) CO 2 (shear) CO 2 (back) Removal efficiency Remarks
One 5.60% 14 ppm 207 8.70%
2 6.30% 11 ppm 207 8.20%
3 6.50% 10 ppm 206 8.10%
4 8.80% 10 ppm 165 6.90%
5 9.10% 10 ppm 157 6.60%
6 9.30% 10 ppm 153 6.60%
CO 2 average concentration 8.33% 6.70%
CO 2 removal efficiency 19.60%
표 3은 위탁기관인 주식회사 경인환경에 의해 측정된 데이터이다.Table 3 shows data measured by Kyungin Environment Co., Ltd., a consignment agency.
표 3
번호 O2 CO T(℃) CO2(전단) CO2(후단) 제거효율 비고
1 6.90 % 3 ppm 45.7 2.25 %
2 7.40 % 7 ppm 47.0 1.87 %
3 10.50 % 10 ppm 37.1 0.00 %
4 9.80 % 10 ppm 37.8 0.00 %
CO2평균농도 2.06 % 0.00 %
CO2제거효율 100 %
TABLE 3
number O 2 CO T (℃) CO 2 (shear) CO 2 (back) Removal efficiency Remarks
One 6.90% 3 ppm 45.7 2.25%
2 7.40% 7 ppm 47.0 1.87%
3 10.50% 10 ppm 37.1 0.00%
4 9.80% 10 ppm 37.8 0.00%
CO 2 average concentration 2.06% 0.00%
CO 2 removal efficiency 100%
상기 표 2 와 표 3에서 보는 바와 같이, 전단의 측정점과 후단의 측정점에서 이산화탄소의 발생량을 본원인은 각각 3회 주식회사 경인환경은 2회 측정한 결과 본원인의 전단 측정점에서의 이산화탄소 평균농도 측정치는 8.33%이고 후단 측정점에서의 이산화탄소 평균농도 측정치는 6.70%로서 전체 이산화탄소 제거효율은 19.60%로서 기존의 이산화탄소 제거율에 비해 매우 효과적으로 나타나고 있으며,As shown in Table 2 and Table 3, the measurement of the amount of carbon dioxide generated at the measurement point of the front end and the measurement point at the rear end was measured twice at the Kyungin Environment Co., Ltd. three times, respectively. It is 8.33% and the average carbon dioxide concentration measured at the next stage is 6.70% and the total CO2 removal efficiency is 19.60%, which is very effective compared to the existing CO2 removal rate.
특히, 주식회사 경인환경에서 측정한 결과는 전단 측정점에서의 이산화탄소 평균농도 측정치는 2.06%이고 후단 측정점에서의 이산화탄소 평균농도 측정치는 0.00%로서 전체 이산화탄소 제거효율은 100%의 획기적인 시험 결과가 도출되었다.In particular, the measured results in Kyungin Environment Co., Ltd. were 2.06% of the average carbon dioxide concentration measured at the front end measurement point and 0.00% of the average concentration of the carbon dioxide at the downstream end measured point.
이와 같은 결과에 대한 주식회사 경인환경의 시험 성적서의 시험항목과 그 결과치를 표 4에 게재하면 다음과 같다.The test items of the test report of Kyungin Environment Co., Ltd. and the results of these results are shown in Table 4.
표 4
시험항목 전 단 후 단
CO2(%) 2.06 0.00
비 고 ;
Table 4
Test Items Previous After
CO 2 (%) 2.06 0.00
NOTE;
업 소 명 ; 송도청라소각장 (태영플랜트 의뢰)Business name; Songdo Cheongna Incineration Plant (Taeyoung Plant)
채취일자 ; 2010년 03월 19일Collection date; March 19, 2010
시 설 명 ; 소각시설Description; Incineration Facility
시험항목 ; CO2 이다.Test Items ; CO 2 .
표 4에 의한 시험 성적서는 도 2 에 이미지로 표현된다.The test report according to Table 4 is represented by the image in FIG.
바람직하게는 본 발명의 색상을 발휘하기 위해 붉은색의 염료를 20PPM 함유할 수도 있는 것으로서 공지된 기술로 알카리성인 pH 11의 소석회에 붉은색의 지시약 페놀프탈레인(phenolphthalein)을 투입한 상태에서 이산화탄소와 반응하면 소석회가 pH 8 정도의 중성으로 변화되고 상기 페놀프탈레인은 무색을 띠는 것으로서 이와 같이 지시약의 색 변화로 이산화탄소의 제거정도를 파악할 수 있도록 한 것이며 이는 이미 공지된 기술인 것이다.Preferably, in order to exhibit the color of the present invention, it may contain 20PPM of red dye. As a known technique, when reacted with carbon dioxide in the state of adding red indicator phenolphthalein to alkaline calcined pH 11 The slaked lime is changed to neutral pH of about 8 and the phenolphthalein is colorless so that it is possible to grasp the extent of carbon dioxide removal by the color change of the indicator, which is a known technique.
상기와 같이 본 발명인 연소시 발생되는 이산화탄소를 제거하기 위한 조성물을 폐가스에 함유된 이산화탄소와 결합되면 이산화탄소가 제거 또는 저감됨으로서 결국 환경오염 및 온실효과 등등의 문제점을 해결할 수 있는 것이다.As described above, when the composition for removing carbon dioxide generated by combustion of the present invention is combined with carbon dioxide contained in the waste gas, carbon dioxide is removed or reduced, thereby solving problems such as environmental pollution and greenhouse effect.
본 발명은 난방기(보일러, 온풍기 등) 및 기타 장치(소각로, 발전기 등)의 가동을 위하여 사용되는 연료 즉 유류(경유, 등유, LPG, 벙커씨유 등) 및 고체연료(갈탄, 괴탄, 조개탄, 성형탄, 목재, 고형화 연료, 팜연료 등)가 연소되고 연도로 배출되는 폐가스중에 있는 이산화탄소가스를 제거하여 대기오염을 방지할 수 있도록 한 연소시 발생되는 이산화탄소를 제거하기 위한 조성물을 제공하여, 연소시 발생되는 배기가스로 인한 대기오염문제가 현저하게 개선되기 때문에 삶의 질이 향상되며, 청정기술의 개발에 따라 환경에 대한 일반 대중의 인식도를 앙양시키게 되고, 유류사용 보일러나 소각로 설치에 대한 부정적인 인식을 근본적으로 변화시킬 수 있으며, 특히 대기중에 방출되는 이산화탄소량을 저감함으로써 온실효과에 의한 지구온난화 예방에 기여하는 산업상 이용 가능성을 기대할 수 있다.The present invention relates to fuels used for the operation of heaters (boilers, warmers, etc.) and other devices (incinerators, generators, etc.), that is, oils (light oil, kerosene, LPG, bunker seed oil, etc.) and solid fuels (brown coal, lump coal, shell coal, Coal briquettes, wood, solidified fuel, palm fuel, etc.) are burned and a composition for removing carbon dioxide generated during combustion to remove the carbon dioxide gas in the waste gas discharged to the flue to prevent air pollution, The quality of life is greatly improved due to the significant improvement of the air pollution caused by the generated exhaust gas, and the development of clean technology raises the public's awareness of the environment, and the negative perception of installing oil-fired boilers or incinerators. Can be fundamentally changed and, in particular, by reducing the amount of carbon dioxide released into the atmosphere, it is possible to prevent global warming due to the greenhouse effect. The industry can expect to availability.
이상에서는 본 발명을 특정의 바람직한 실시예를 예를들어 설명하였으나, 본 발명은 상기한 실시예에 한정되지 아니하며 본 발명의 정신을 벗어나지 않는 범위내에서 당해 발명이 속하는 기술분야에서 통상의 지식을 가진자에 의해 다양한 변경과 수정이 가능할 것이다.In the above, the present invention has been described with reference to specific preferred embodiments, but the present invention is not limited to the above-described embodiments, and the present invention is not limited to the above-described embodiments. Various changes and modifications may be made by the user.

Claims (1)

  1. 산화칼슘인 생석회에 물을 용해시켜서 제조된 수산화칼슘 수용액 97.50%에 반응지속제인 수산화나트륨 0.25%와 반응지연제인 산화마그네슘 2.25%을 첨가혼합하여 이루어진 것을 특징으로 하는 연소시 발생되는 이산화탄소를 제거하기 위한 조성물.A composition for removing carbon dioxide generated during combustion, characterized by mixing and mixing 0.25% of sodium hydroxide as a reaction agent and 2.25% of magnesium oxide as a reaction delay agent to 97.50% of an aqueous solution of calcium hydroxide prepared by dissolving water in quicklime of calcium oxide. .
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KR101469617B1 (en) * 2011-11-08 2014-12-08 주식회사 에스디알앤디 Bio gas upgrading equipment
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