• Bulletin of the Korean Chemical Society
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• 제31권10호
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• pp.2989-2991
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• 2010

• 플랜트 저널
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• 제13권2호
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• pp.34-38
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• 2017

상업규모의 온실가스 저감 기술 중 대표적인 기술 중 하나인 연소 후 습식아민 $CO_2$포집 기술에서 기술의 개발에 중점을 두고 있는 부분이 운영비의 개선 부분이다. 습식아민 $CO_2$ 포집기술에서 사용되는 아민은 대체로 고가의 아민을 사용한다. 고가의 아민을 사용하기 때문에 설비 운영 중 발생하는 흡수제의 손실이 운영비에 영향을 미칠 수 있고 설비의 용량이 커질 수록 운영비는 더욱 커지게 된다. 본 연구에서는 150MW급 석탄화력발전소 배기가스에 아민흡수법 CCS기술을 적용 할 경우 흡수제의 손실이 설비 운영비에 미치는 영향과 물 세정 타워의 설계가 흡수제 손실 절감에 어떠한 영향을 미치는지 살펴 보았다.

• 약학회지
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• 제24권3_4호
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• pp.159-165
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• 1980

Tetrathiocyanatocobaltate[II] forms complexes with tertiary amine salts or quarternary ammonium salts which were extractable from aqueous solution by organic solvent. In order to study composition of the complex, the colored crystalline complexes produced were evaluated with elemental analysis, infrared and mass spectra. And also a novel spectrophotometric method for the determination of tertiary amine salt or quarternary ammonium salt with tetrathiocyanatocobaltate[II] was established by organic solvent extraction within coefficient of variation of 1.06-1.35%.

• 공업화학
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• 제7권1호
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• pp.186-193
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• 1996

몇 가지 키토산 비드들을 W/O 에멀젼법과 capillary extrusion법에 의해 제조하여, SEM 사진을 통해 표면 구조와 표면적의 차이를 관찰하였고, BET법으로 표면적을 측정하였으며, 피크린산 적정에 의해 유효 아민함량을 측정하여 상기 결과들과의 상관관계를 알아 보았다. W/O 에멀젼법에 의해 제조한 비드의 경우 capillary extrusion법에 의해 제조된 비드들보다 입자의 크기가 작았으며, 반대로 표면적, 유효 아민함량은 높게 나타났다. 또한 비드의 표면적, 유효 아민함량, 겉보기 밀도(apparent density) 및 기계적 강도(hardness)는 제조시 건조방법에 따라 매우 큰 편차를 나타내었다. Hardness 측정결과 solvent dehydration법에 의해 건조된 비드들이 동결건조법에 의해 건조된 비드들에 비해 높은 강도를 나타내었다. 또한 겉보기 밀도에 있어서도 solvent dehydration한 비드들이 동결건조한 비드들에 비해 높은 겉보기 밀도를 보였다. SEM 사진 분석결과 solvent dehydration법에 의한 비드들은 매우 작은 pore들이 비드의 표면에 무수히 존재한 반면 동결건조한 비드에서는 벌집모양의 pore들이 존재하고 있음을 알 수 있었다. 피크린산 적정결과 solvent dehydration한 비드의 경우 동결건조한 비드보다 약 10배의 높은 유효 아민함량을 나타내었으며 비드의 표면적이 클수록 유효 아민함랑은 높게 나타났다. 또한 fluorescamine을 반응시킨 후 형광현미경으로 관찰하여 비드의 표면과 내부의 pore 주위에 노출된 1차 아민의 존재를 정성적으로 확인할 수 있었다.

• 한국환경과학회지
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• 제32권6호
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• pp.477-482
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• 2023

Halloysite nanotube (HNT) has a nanotube structure with the chemical formula of Al₂Si₂O₅(OH)₄ · nH₂O and is a natural sediment of aluminosilicate. A lot of research has been conducted to improve the mechanical properties of epoxy composites by generating interactions between HNTs and polymers through surface treatment of HNTs, such as exchange of amine group as a terminal functional group. However, most of the surface modification methods are performed under wet conditions, which require a relatively large amount of time, manpower and solvent. In order to save time and simplify complicated procedures, a dry coating machine was designed and used for amine group exchange. Comparing the XPS results, it was found that the results of NH₂-HNT prepared using a dry coating machine and the substitution through the wet method were not significantly different, and it has been confirmed that the amount of solvent used and the time savings can be made.

• 에너지공학
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• 제28권4호
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• pp.8-12
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• 2019

Thermal amine scrubbing is the most advanced CO₂ capture technique but its largescale application is hindered due to the large heat requirement during solvent regeneration step. The addition of a solid metal oxide catalysts can optimize the CO₂ desorption rate and thus minimize the energy consumption. Herein, we evaluate the solvent regeneration performance of Monoethanolamine (MEA) and Diethanolamine (DEA) solvents without and with two metal oxide catalysts (TiO₂ and V₂O₅) within a temperature range of 40-86℃. The solvent regeneration performance was evaluated in terms of CO₂ desorption rate and overall amount of CO₂ desorbed during the experiments. Both catalysts improved the solvent regeneration performance by desorbing greater amounts of CO₂ with higher CO₂ desorption rates at low temperature. Improvements of 86% and 50% in the CO₂ desorption rate were made by the catalysts for MEA and DEA solvents, respectively. The total amount of the desorbed CO₂ also improved by 17% and 13% from MEA and DEA solvents, respectively. The metal oxide catalyst-aided regeneration of amine solutions can be a new approach to minimize the heat requirement during solvent regeneration and thus can remove a primary shortfall of this technology.

• 한국산업융합학회 논문집
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• 제27권2_2호
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• pp.357-361
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• 2024

Halloysite nanotube (HNT) has a nanotube structure with the chemical formula of Al₂Si₂O₅(OH)₄·nH₂O and is a natural sediment of aluminosilicate. HNT has been used as additive to improve the mechanical properties of epoxy composites with exchange of amine group as a terminal functional group using huge amount of organic solvents. In order to save time and simplify complicated procedures, a dry coating machine was designed and used for amine group exchange in previous research. For better applications, it was conducted with different parameters and with scale up settings. Best condition was found to reduce usage of solvent, time and man power.

• 한국물환경학회지
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• 제36권1호
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• pp.48-54
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• 2020

This paper presents a screening protocol for the selection of solvents available for the solvent extraction desalination process. The desalination solvents hypothetically and theoretically require the capability of (1) Forming hydrogen bonds with water, (2) Absorbing some water molecules into its non-polar solvent layer, (3) Changing solubility for water-solvent separation, and (4) Rejecting salt ions during absorption. Similar to carboxylic acids, amine solvents are solvent chemicals applicable for desalination. The key parameter for selecting the potential solvent was the octanol-water partitioning coefficient (Kow) of which preferable value for desalination was in the range of 1-3. Six of the 30 amine solvents can absorb water and have a variable, i.e., temperature swing solubility with water molecule for water-solvent separation. Also, the hydrogen bonding interaction between solvent and water must be stronger than the ion-dipole interaction between water and salt, which means that the salt ions must be broken from the water and only water molecules absorbed for the desalination. In the final step, three solvents were selected as desalination solvents to remove salt ions and recover water. The water recovery of these three solvents were 15.4 %, 2.8 %, 10.5 %, and salt rejection were 76 %, 98 %, 95 %, respectively. This study suggests a new screening protocol comprising the theoretical and experimental approaches for the selection of solvents for the desalination method which is a new and challenges the desalination process in the future.

• Biotechnology and Bioprocess Engineering:BBE
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• 제6권6호
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• pp.386-394
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• 2001

Carboxylic acids are examples of compounds with wide industrial applications and high potential, This article presents the principles of reactive extraction along with the character-istics of tertiary amine extractants, while is given on considering the effect of the amine class and chain length, As such a brief overview the current research on reactive extraction, including the recovery of citric acid, selective amine-based extraction , and extractive fermentation is given. When discussing extractive fermentation strategies for reducing solvent toxicity are also suggested based on specific examples. Finally, solvent regeneration and stripping of extracted acid explained.

• 대한화학회지
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• 제16권6호
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• pp.361-368
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• 1972

5%트리옥틸아민과 5%옥틸알콜이 든 헥산유기용매 1l는 62g의 $WO_3$를 추출할 수 있었는데 반하여 아민만을 사용했을 경우는 37g의 $WO_3$밖에 추출할 수 없었다. 유기용매 추출과정에서 이러한 알콜의 아민-텅스텐 화합물의 용해도의 상승작용 및 아민과 텅스텐산간의 상호작용을 핵자기 공명분광학을 이용하여 연구하였다. 텅스텐은 고분자형의 텅스텐산 이온상태로 유기층으로 추출되어 다중텅스텐산 트리옥틸 암모니움염을 형성함을 알 수 있었으며 이 염은 텅스텐산이온과 알콜간에 수소결합을 형성함으로써 탄화수소 용매에서 더욱 안정화됨을 알 수 있었다.