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    • 91. 发明授权
    • 저온영역에서 재생 가능한 이산화티탄을 포함하는탄산알칼리 이산화탄소 고체 흡수제
    • 二氧化钛添加二氧化碳去除的碱性碳酸盐可再生溶剂
    • KR100803325B1
    • 2008-02-13
    • KR1020060108946
    • 2006-11-06
    • 한국전력공사
    • 류청걸이중범백점인김재창이수출최보윤채호진이수재정석용
    • B01J20/04B01J20/02
    • B01J20/0211B01J20/04B01J2220/4806
    • A solid sorbent for carbon dioxide removal prepared by supporting active materials such as KHCO3, K2CO3 and NaHCO3 onto TiO2 as an additive or a support is provided, and a method for preparing the same is provided, wherein the TiO2 as an additive or a support improves regeneration of the sorbent by inhibiting or preventing side reactions. In a method for preparing a TiO2 contained alkali-carbonate solid sorbent for carbon dioxide removal by preparing a TiO2 additive or support through a first step of performing a co-precipitation process or a sol-gel process, mixing the TiO2 additive or support with an alkali-carbonate component consisting of one or more of KHCO3, K2CO3, Na2CO3 and NaHCO3, and drying, firing and sieving the mixture, a method for preparing a titanium dioxide contained alkali-carbonate solid sorbent for carbon dioxide removal regenerable without performing a pre-treatment process comprises: a second step of mixing 50 to 85 wt.% of the TiO2 additive or support prepared in the first step with 15 to 50 wt.% of the alkali-carbonate component by using H2O or ethylene glycol as a binding material; a third step of firing the mixture at 200 to 650 deg.C in a nitrogen atmosphere to prepare an alkali-carbonate sorbent; and a fourth step of sorting constantly the fired material into grains having a grain size of 20 mum to 5 mm through sieving.
    • 提供了通过将活性物质如KHCO 3,K 2 CO 3和NaHCO 3负载作为添加剂或载体而制备的用于二氧化碳去除的固体吸附剂,并提供了其制备方法,其中作为添加剂或载体的TiO 2改善 通过抑制或预防副反应来再生吸附剂。 在通过在进行共沉淀法或溶胶 - 凝胶法的第一步骤中制备TiO 2添加剂或载体来制备含有二氧化碳去除二氧化碳的TiO 2的方法中,将TiO 2添加剂或载体与 由KHCO 3,K 2 CO 3,Na 2 CO 3和NaHCO 3中的一种或多种组成的碱金属 - 碳酸盐组分,并干燥,焙烧和筛分混合物,制备二氧化钛的方法包含用于二氧化碳去除的碱金属 - 碳酸盐固体吸附剂, 处理方法包括:通过使用H 2 O或乙二醇作为粘合材料,将50至85重量%的在第一步骤中制备的TiO 2添加剂或载体与15至50重量%的碱金属碳酸盐组分混合的第二步骤; 在氮气气氛中在200〜650℃下烧成混合物以制备碱碳酸盐吸附剂的第三步骤; 以及通过筛分将煅烧材料不断分选成粒径为20μm至5mm的晶粒的第四步骤。
    • 92. 发明授权
    • 연소 배기가스 중의 수은의 산화방법
    • 연소배기가스중의수은의산화방법
    • KR100635719B1
    • 2006-10-17
    • KR1020050039331
    • 2005-05-11
    • 한국전력공사
    • 박경일백점인송광철
    • B01D53/94
    • A method for oxidizing mercury in combustion exhaust gas, which is excellent in oxidation activity and economic efficiency when changing metal mercury contained in combustion exhaust gas exhausted from a large boiler into mercury chloride, is provided. A method for oxidizing mercury in combustion exhaust gas comprises mercury in the combustion exhaust gas into mercury chloride in the presence of a chromium oxide catalyst supported with a magnesium oxide-aluminum oxide prepared by coprecipitating a magnesium salt, an aluminum salt and a chromium salt at a ratio of 1:1:1 and drying the coprecipitated material at 110 deg.C. The chromium oxide supported with the magnesium oxide-aluminum oxide is prepared by adding a magnesium salt, an aluminum salt, a chromium salt and a precipitant into water to form a precipitate and calcining the precipitate to a temperature from 300 to 700 deg.C under an air atmosphere.
    • 提供一种氧化燃烧废气中的汞的方法,该方法在将从大型锅炉排出的燃烧废气中所含的金属汞变更为氯化汞时,氧化活性和经济性优异。 在氧化镁 - 氧化铝负载的氧化铬催化剂存在下,在燃烧废气中氧化汞的方法包括将燃烧废气中的汞转化为氯化汞,所述氧化镁 - 氧化铝通过将镁盐,铝盐和铬盐共沉淀在 比例为1:1:1,并在110℃下干燥共沉淀材料。 用氧化镁 - 氧化铝负载的氧化铬通过向水中加入镁盐,铝盐,铬盐和沉淀剂以形成沉淀物并将沉淀物煅烧至300-700℃的温度来制备 一个空气的气氛。
    • 94. 发明公开
    • 배가스 중 이산화탄소의 제거 방법
    • 使用二氧化碳溶液作为二氧化碳吸附溶液的水溶液除去二氧化碳的方法
    • KR1020050017649A
    • 2005-02-22
    • KR1020030054992
    • 2003-08-08
    • 한국전력공사
    • 안희수장경룡이태원천성남안영모백점인
    • B01D53/75
    • B01D53/1475B01D53/1425B01D2257/504
    • PURPOSE: To provide a method for removing carbon dioxide from exhaust gas, which uses sodium hydroxide instead of using amine-based adsorption solution to adsorb carbon dioxide from the exhaust gas and separates the carbon dioxide using an electro-dialysis stack. CONSTITUTION: The method comprises the steps of: (a) reacting exhaust gas with an aqueous solution of sodium hydroxide to adsorb carbon dioxide therefrom; (b) treating the carbon dioxide adsorbed solution obtained from the step (a) with ion-exchange membrane in an electro-dialysis stack to separate highly concentrated carbonic acid from the sodium hydroxide; and (c) reusing the concentrated sodium hydroxide at an adsorption tower, and using the concentrated carbonic acid to prepare methanol.
    • 目的:提供一种从废气中除去二氧化碳的方法,该方法使用氢氧化钠代替使用胺类吸附溶液从排气中吸附二氧化碳,并使用电渗析层分离二氧化碳。 方法:该方法包括以下步骤:(a)使废气与氢氧化钠水溶液反应以从其中吸附二氧化碳; (b)用离子交换膜在电渗析叠层中处理由步骤(a)得到的二氧化碳吸附溶液,以将高度浓缩的碳酸与氢氧化钠分离; 和(c)在吸附塔上重新使用浓氢氧化钠,并使用浓缩的碳酸制备甲醇。
    • 95. 发明公开
    • 혼합기체로부터 산기체를 분리하기 위한 흡수제 및 이를 이용한 산기체 분리방법
    • 酸气吸收和酸气吸收系统使用它
    • KR1020020003962A
    • 2002-01-16
    • KR1020000035934
    • 2000-06-28
    • 한국전력공사한국수력원자력 주식회사
    • 엄희문이재근윤지호심재구백점인
    • B01D53/14
    • Y02A50/2342Y02C10/06
    • PURPOSE: To increase absorption rate of acid gases such as SO2, CO2 from gas streams in the aqueous alkanolamine process where an absorbent mixture of MDEA, triethanolamine, dimethylethanolamine, and methyldiisopropanolamine is used, EDBEA (2,2-(ethylenedioxy)bis(ethylamine)) is added, as an absorption accelerator, to conventional ternary alkanolamine process. EDBEA has a primary amine group represented by NH2(CH2CH2O)nCH2CH2NH2 (n is an integer of 1 to 12) at both terminal ends, therefore it is possible to absorb quickly carbon dioxide across vapor-liquid interface. CONSTITUTION: An acid gas absorbent of the present invention is characterized by comprising ternary alkanolamine 20-50%, EDBEA (2,2-(ethylenedioxy)bis(ethylamine)) 0.5-5%, and the balance of water. Further, a scrubbing tower, for optimal operation with the acid gas absorbent, is preferably operated in the temperature range 40 to 60deg.C at a pressure of 1 to 2 atm.
    • 目的:为了提高使用MDEA,三乙醇胺,二甲基乙醇胺和甲基二异丙醇胺的吸收剂混合物的烷基醇胺水溶液中气流中SO2,CO2等酸性气体的吸收速率,EDBEA(2,2-(亚乙二氧基)双(乙胺) ))作为吸收促进剂加入到常规的三元链烷醇胺方法中。 EDBEA在两个末端具有由NH 2(CH 2 CH 2 O)n CH 2 CH 2 NH 2(n为1〜12的整数)表示的伯胺基,因此可以快速地吸收二氧化碳蒸气 - 液体界面。 构成:本发明的酸性气体吸收剂的特征在于含有20-50%的三元链烷醇胺,0.5-5%的EDBEA(2,2-(亚乙二氧基)双(乙胺))和余量的水。 此外,用酸性气体吸收剂最佳操作的洗涤塔优选在1至2大气压的压力下在40至60℃的温度范围内操作。