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公开(公告)号：KR101487387B1
公开(公告)日：2015-01-28
申请号：KR1020130126893
申请日：2013-10-24
Applicant: 한국에너지기술연구원
CPC classification number: B01J37/02 , B01J23/883 , B01J35/1014 , B01J37/08
Abstract: 본 발명은 금속 카바이드계 메탄 리포밍 촉매 제조방법 및 그 방법에 의해 제조된 메탄 리포밍 촉매에 관한 것으로서, 보다 상세하게는 금속 카바이드계 메탄 리포밍 촉매 제조방법에 있어서, 물에, Mo전구체, Ni전구체 및 다공성 탄소물질을 혼합하여 현탁액을 제조하는 단계; 상기 현탁액의 pH를 조절하는 단계; 상기 pH조절된 현탁액를 교반하여 다공성 탄소물질에 Mo전구체 및 Ni전구체를 흡착하는 단계; 상기 다공성 탄소물질에 Mo전구체 및 Ni전구체가 흡착된 현탁액을 여과하여 촉매 전구체를 회수 및 건조하는 단계; 상기 회수 및 건조된 촉매 전구체를 소성하는 단계; 및 상기 소성된 촉매 전구체를 침탄하는 단계;를 포함하여 이루어진다.
Abstract translation: 本发明涉及一种制备金属碳化物基甲烷重整催化剂的方法和通过该方法制备的甲烷重整催化剂，更具体地涉及一种制备金属碳化物基甲烷重整催化剂的方法，包括以下步骤： 通过将Mo前体，Ni前体和多孔碳材料混合到水中来进行悬浮; 控制悬浮液的PH; 混合PH控制的悬浮液并将Mo前体和Ni前体吸附到多孔碳材料上; 将Mo前体和Ni前体的悬浮液过滤到多孔碳材料上，收集并干燥催化剂前体; 烧结收集和干燥的催化剂前体; 并将烧结的催化剂前体渗碳。
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公开(公告)号：KR101406711B1
公开(公告)日：2014-06-16
申请号：KR1020130032218
申请日：2013-03-26
Applicant: 한국에너지기술연구원
Abstract: The present invention relates to a method for separating carbon dioxide from mixed gas containing the carbon dioxide and, more particularly, to a method for using an amino silane group as a mixed solvent in a carbon dioxide separation apparatus including an absorption tower and a stripping tower. The method for separating carbon dioxide using the mixed solvent of the present invention includes: a step in which a carbon dioxide-mixed solvent is supplied to an upper portion of the absorption tower and the mixed gas containing carbon dioxide is introduced to a lower portion of the absorption tower so that the carbon dioxide contained in the mixed gas is absorbed into the mixed solvent; a step in which the mixed solvent into which the carbon dioxide is absorbed is sent to a re-evaporation tank (flash tank) and the carbon dioxide is stripped by pressure difference; and a step in which the mixed solvent which passes through the re-evaporation tank is sent to the stripping tower and is heated to strip the carbon dioxide. In the method for separating carbon dioxide, an amino silane-based mixed solvent is used as the mixed solvent. The amino silane solvent of the present invention has a higher carbon dioxide absorption performance and removal efficiency than existing commercial solvents, and thus capturing costs can be saved in process application. In addition, the low volatility results in excellent safety and economic feasibility in a process operation.
Abstract translation: 本发明涉及从包含二氧化碳的混合气体中分离二氧化碳的方法，更具体地说，涉及在包括吸收塔和汽提塔的二氧化碳分离装置中使用氨基硅烷基团作为混合溶剂的方法 。 使用本发明的混合溶剂分离二氧化碳的方法包括：向吸收塔的上部供给二氧化碳混合溶剂的步骤，将含有二氧化碳的混合气体导入到 吸收塔使得混合气体中所含的二氧化碳被吸收到混合溶剂中; 其中吸收二氧化碳的混合溶剂被送到再蒸发罐（闪蒸罐）并通过压力差汽提二氧化碳的步骤; 将通过再蒸发槽的混合溶剂送入汽提塔并被加热以除去二氧化碳的步骤。 在分离二氧化碳的方法中，使用氨基硅烷类混合溶剂作为混合溶剂。 本发明的氨基硅烷溶剂比现有的商业溶剂具有更高的二氧化碳吸收性能和去除效率，因此在工艺应用中可节省成本。 此外，低波动性在过程操作中导致出色的安全性和经济可行性。
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Patent Agency Ranking
公开(公告)号：KR1020140060930A
公开(公告)日：2014-05-21
申请号：KR1020120127899
申请日：2012-11-13
Applicant: 한국에너지기술연구원
CPC classification number: Y02A50/2342 , G01N25/005 , B01D53/1475 , C01B32/50
Abstract: The present invention relates to a method for calculating regenerative heat of a chemical absorbent for carbon dioxide. The regenerative energy of a chemical absorbent for carbon dioxide is calculated by obtaining and calculating parameters using a device in a short term instead of obtaining test values of the regenerative energy of a chemical absorbent for carbon dioxide via process operation, calculating the current heat of the absorbent from the result of measuring reaction heat and specific heat of the absorbent in the process of measuring a combustion phenomenon before and after the reaction of the absorbent for carbon dioxide, calculating the latent heat for evaporation of a solvent, and summing all the values. The method for calculating regenerative heat of an absorbent for carbon dioxide from the sum of the latent heat for evaporation, the reaction heat for absorption and the current heat comprises the steps of: calculating the latent heat for evaporation of the absorbent for carbon dioxide; measuring the reaction heat for absorption of the absorbent for carbon dioxide; and calculating the specific heat of carbon dioxide before and after reaction in the process of measuring the heat capacity before reaction of the absorbent for carbon dioxide and the heat capacity after reaction of the absorbent for carbon dioxide in a state of being completely saturated with carbon dioxide, and calculating the current heat therefrom.
Abstract translation: 本发明涉及二氧化碳化学吸收剂的再生热计算方法。 二氧化碳化学吸收剂的再生能量是通过在短期内使用装置获得和计算参数来计算的，而不是通过过程操作获得用于二氧化碳的化学吸收剂的再生能量的测试值，计算当前的热量 在测量二氧化碳吸收剂反应前后的燃烧现象的过程中测量反应热和吸收剂的比热的结果，计算用于蒸发溶剂的潜热，并将所有值相加，从而得到吸收剂。 用于计算用于二氧化碳的吸收剂的再生热的方法，用于蒸发潜热，吸收反应热和当前的热量之和包括以下步骤：计算二氧化碳吸收剂的蒸发潜热; 测量吸收二氧化碳吸收剂的反应热; 计算二氧化碳吸收剂反应前的热容量和反应二氧化碳吸收剂在二氧化碳完全饱和后的反应后的热容量的反应前后的二氧化碳的比热 ，并计算当前的热量。
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公开(公告)号：KR1020130126359A
公开(公告)日：2013-11-20
申请号：KR1020120050430
申请日：2012-05-11
Applicant: 한국에너지기술연구원
IPC: B01D53/14 , B01D53/62 , B01D19/00 , C07D233/58
CPC classification number: Y02C10/04 , Y02C10/06 , Y02P20/152 , B01D53/14 , B01D19/00 , B01D53/62 , C07D233/58
Abstract: Disclosed are an ether-functionalized immidazolium-based ionic liquid and a separating method of carbon dioxide using the same. The ether-functionalized imidazolium-based ionic liquid has excellent carbon dioxide absorbing ability. The absorbed carbon dioxide is easily attached and detached by heating, so the ether-functionalized imidazolium-based ionic liquid has user convenience, selectivity, thermal stability, and long lifetime, thereby being useful for collecting CO2.
Abstract translation: 公开了醚官能化的基于咪唑鎓的离子液体和使用其的二氧化碳的分离方法。 醚官能化的咪唑鎓离子液体具有优异的二氧化碳吸收能力。 吸收的二氧化碳通过加热容易地附着和分离，因此醚官能化的咪唑鎓离子液体具有用户便利性，选择性，热稳定性和长寿命，因此可用于收集二氧化碳。
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公开(公告)号：KR101316543B1
公开(公告)日：2013-10-15
申请号：KR1020110062228
申请日：2011-06-27
Applicant: 한국에너지기술연구원
CPC classification number: Y02A50/2342 , Y02C10/04 , Y02C10/06
Abstract: 본 발명은 이산화탄소 흡수 방법에 관한 것으로서, 이산화탄소 흡수공정에서 염의 생성을 최소화하고, 발생된 염을 효과적으로 제거함으로써 재생에너지를 최소화할 수 있는 이산화탄소 흡수 공정에 관한 것이다. 본 발명의 이산화탄소 흡수 공정은 알칼리탄산염에 입체장애 시클릭 아민이 첨가된 이산화탄소 흡수제에 이산화탄소가 포함된 기체를 접촉시키는 기체 접촉단계; 상기 기체로부터 이산화탄소를 흡수하는 이산화탄소 흡수단계; 상기 이산화탄소가 흡수된 흡수제에서 염을 분리하는 공정; 상기 염이 분리된 흡수제를 재생하는 단계를 포함한다.
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公开(公告)号：KR101288530B1
公开(公告)日：2013-07-26
申请号：KR1020110089922
申请日：2011-09-06
Applicant: 한국에너지기술연구원
CPC classification number: B01D71/024 , C01B13/0255
Abstract: 본원은 La
1-x Sr
x Ti
1-y Fe
y O
3-δ 로 코팅된 Ba
1-x Sr
x Co
1-y Fe
y O
3-δ 의 조성을 갖는 이온전도성 산소분리용 분리막 및 이의 제조방법을 제공한다. La
1-x Sr
x Ti
1-y Fe
y O
3-δ 로
보호 코팅된 본원의 Ba
1-x Sr
x Co
1-y Fe
y O
3-δ 분리막은 코팅되지 않은 분리막과 비교하여 현저히 향상된 산소투과도 및 열적 안정성을 가져 이산화탄소를 함유하는 공기로부터 산소 분리 등에 유용하게 사용될 수 있다.-
97.发明公开
公开(公告)号：KR1020130019161A
公开(公告)日：2013-02-26
申请号：KR1020110081149
申请日：2011-08-16
Applicant: 한국에너지기술연구원
IPC: C07D233/60 , C07D233/58 , C07C309/04 , B01J20/22
Abstract: PURPOSE: A method for synthesizing sulfonate-based ionic liquid for separating carbon dioxide is provided to prepare 1-(2-methoxyethyl)-3-methylimidazolnium methanesulfonate and to ensure a stable physical property. CONSTITUTION: A method for synthesizing 1-(2-methoxyethyl)-3-methylimidazolnium methansulfonate ionic liquid comprises: a step of adding 2-methoxyethy methanesulfonate and 1-methylimidazole in a beaker, injecting dichloromethane as a solvent, and stirring at 50-70 deg. C. and 200-250 rpm for 25-35 hours; a step of removing unreacted materials and the solvent and collecting a synthesized solution; and a step of purifying the synthesized solution. The collection step comprises a step of removing the solvent by decompression; a step of repetitively washing the solvent-removed solution using ethyl acetate; and a step of removing the washing solution and collecting the synthesized solution. [Reference numerals] (AA) Step of stirring 2-methoxyethy methanesulfonate and 1-methylimidazole by injecting a solvent; (BB) Step of collecting a synthesized solution by removing the solvent and unreacted materials; (CC) Step of purifying the synthesized solution by filtering with a filter; (DD) Step of drying by removing residual moisture
Abstract translation: 目的：提供一种合成磺酸盐离子液体分离二氧化碳的方法，以制备甲磺酸1-（2-甲氧基乙基）-3-甲基咪唑并确保物理性质稳定。 构成：合成1-（2-甲氧基乙基）-3-甲基咪唑鎓甲磺酸盐离子液体的方法包括：在烧杯中加入2-甲氧基乙基甲磺酸酯和1-甲基咪唑的步骤，注入二氯甲烷作为溶剂，并在50-70℃下搅拌 度。 C和200-250rpm 25-35小时; 除去未反应物和溶剂并收集合成溶液的步骤; 和纯化合成溶液的步骤。 收集步骤包括通过减压除去溶剂的步骤; 使用乙酸乙酯重复洗涤除去溶剂的溶液的步骤; 以及除去洗涤溶液并收集合成溶液的步骤。 （AA）通过注入溶剂来搅拌甲磺酸2-甲氧基乙酯和1-甲基咪唑的工序; （BB）通过除去溶剂和未反应物质来收集合成溶液的步骤; （CC）用过滤器过滤净化合成溶液的步骤; （DD）通过去除残留水分干燥步骤
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