본 연구에서는 주류공장 내 고농도 CO2 제거 및 포집을 위해 L-alanine 흡수제를 적용하여 CO2 흡수, 탈리 효율을 평가 후 재생 성능을 확인하였다. 탈리공정의 효율적인 처리를 평가하기 위해 실험 실 규모에서 Hot plate, Steam 두가지 탈리 방법을 비교하였으며 Hot plate는 약 10%, Steam의 경우 약 60%의 재생효율을 확인하였다. 따라서 주류공장 내 100m3/min 실증화 규모에 Steam-Tower 탈리공정을 적용하여 최적조건을 평가한 결과 탈리 유량 4L/min 이하, Steam 온도 160℃ 이상, 탈리효율 85.5%로 확 인할 수 있었다.
CKD 추출액은 시멘트공정에서 발생한 폐기물인 CKD를 시멘트 원료로 재사용하기 위해 공정 방해물질로 작용하는 KCl을 추출한 폐수이며, 폐수처리시설 증설 등의 문제로 추출액 무방류 및 이를 재이용하고자 하였다. 이온교환법을 적용하여 KCl을 제거한 결과, 이온교환 후 추출액의 pH는 12.7 에서 pH 2 미만으로 감소하였으며 양이온교환수지의 H+가 이온교환을 거쳐 추출액에 용해되었음을 확인하였다. 이온교환의 선택성에 의해 Ca2+, K+ 순서로 제거되었으며, K+ 이온을 제거하기 위해 접촉시 간의 증가가 필요함을 판단하였다. 이온교환수지와 직접접촉시간이 약 6배 높은 접촉시간을 갖는 회분 식장치에서 연속흐름식장치 대비 4배 높은 K+ 제거 효율을, 7배 높은 Cl- 제거 효율을 확인하였다. 양이온교환수지의 H+가 음이온교환수지의 OH- 대비 1.2배 빠른 교환속도를 가짐을 추출액 pH 변화를 통해 확인하였다.
본 연구에서는 이산화탄소 흡수/재생 공정에 효율적으로 적용할 수 있는 아미노산염 흡수제의 연속재생을 통해 재생효율을 확인하였다. 재생효율은 공정적용에 있어 경제성에 큰 영향을 끼치는 인자로, 보다 경제성 있는 이산화탄소 흡수/재생 공정 확립을 위해 연속재생 실험을 진행하였다. 실험에 사용한 아미노산염은 Potassium L-lysinate와 Potassium L-alaninate이며, 각 아미노산과 Potassium hydroxide(KOH)를 1:2 몰비로 혼합하여 사용하였다. 흡수제의 재생 효율을 확인하기 위해 두 물질에 이산화탄소를 충분히 흡수시킨 후 가열을 통해 이산화탄소 탈리실험을 진행하였다. 반응초기에는 L-alanine의 반응속도가 빠르게 이루어졌으나, 시간이 지남에 따라 흡수량이 보다 큰 L-lysine이 높은 농도의 이산화탄소를 배출하였다. 두 물질의 재생효율을 비교하였을 때, L-alanine은 47.26%, L-lysine 은 62.11%로 L-lysine이 더 높은 재생효율을 나타내었다. 흡수량 및 재생효율이 좋은 L-lysine을 이용한 연속재생 실험결과, 재생횟수가 증가함에 따라 재생효율이 감소하는 것을 확인할 수 있었다.
This study investigated the interactions between starch and starch - derived materials and fluorescent materials. Many researchers have used fluorescent materials to monitor the internal structure of starch, which is an effective method. The purpose of this study was to observe the internal structure of starch by using fluorescent material and to check how much fluorescent material could be loaded inside the starch. For this, a standard curve of the fluorescent material was obtained and a linear graph corresponding to the concentration was obtained. Next, the incorporation of the fluorescent material into the starch was confirmed by CLSM in the infusion experiment. Infusion experiments were carried out to quantify the amount of fluorescent substance in starch, but the error was confirmed in this experiment. The error was caused by the action of starch and the fluorescent substances FD4 and NaFl, resulting in an increase or decrease in fluorescence intensity. To find the cause, dextrin, amylose and amylopectin, which are starch-derived substances, and α, β, γ-cyclodextrin, which can form inclusion compounds, were used. The fluorescent materials were merbromin, NaFl, and FITC. As a result, the fluorescence intensity of the fluorescent material was significantly influenced by the concentration of amylose and amylopectin. This result implies that there may be errors in the analysis of the phenomenon or observation of the starch using the fluorescent substance. We still do not know exactly the cause of this phenomenon, so further research is needed.
Proximate analysis and antioxidant activity of cultivated wild Panax ginseng (CWPG) were investigated to provide fundamental information of CWPG with different ages and to increase its industrial application. Proximate analyses of CWPG with different ages were performed. Extraction of CWPG with different ages was carried out using heatreflux extraction, and their extraction yield, crude saponin content, ginsenoside content, and antioxidant activity were analyzed. Moisture content decreased, but crude fat and crude protein were increased with aging. Extraction yield and crude saponin contents did not show a specific pattern while 5-year-old CWPG revealed the highest extraction yield and crude saponin content. All CWPGs showed typical ginsenoside profiles containing C-K and Rh2 ginsenosides, which are not found in ginseng. The 3-year-old CWPG showed the highest antioxidant activity including total phenolic content, total flavonoid content, and DPPH and ABTS radical scavenging activities. Moreover, 3-year-old CWPG also revealed the highest acidic polysaccharide content. Therefore, these results suggested that 3-year-old CWPG, which is the cheapest, can be used in industrial application due to its high antioxidant activity and acidic polysaccharide content with similar ginsenoside profile compared to 5- and 7-year-old CWPGs.
본 연구는 중·소형 선박의 배가스에 포함되어 있는 황산화물 및 질소산화물을 처리하기 위한 습식 스크러버의 처리효율에 관한 내용이다. 실험은 질소산화물 기술문서(NOX Technical Code)의 E3 모드에 준해서 진행하였다. 엔진에서 황산화물을 배출하기 위해서, 연료로 사용되는 경유에 ditertiarybutyldusulfide를 혼합하여 황 함유량을 높인 연료로 실험을 진행하였다. 배가스 내의 질소산화 물의 대부분을 차지하는 NO가스는 NO2로 산화시켜 습식 스크러버로 흡수하였으며, 황산화물인 SO2는 세정액에 잘 흡수되어 100% 처리효율을 확인하였다.
기존 연구에서는 스크러버를 이용한 NO2 를 제거하기 위해 암모니아 수용액을 적용한다. 하 지만 암모니아는 독성 및 악취가 강해 실선 적용에 어려움이 따를 수 있어, 암모니아를 대체할 수 있는 물질을 찾기 위해 이 연구를 진행하였다. 대체 물질로는 수산화나트륨(NaOH), 티오황산나트륨 (Na2S2O3), 요소(Urea)를 사용하였다. 세정액을 제외한 모든 부분은 기존 암모니아를 적용한 실험의 최 적 조건과 동일하게 진행하였다. 그 결과 실험에 사용된 세 가지 물질 중 두 물질은 암모니아 용액과 대체가 가능한 것으로 사료되었으며, 최적조건은 각각 NaOH 2.5 %, Na2S2O3 5.0 % 에서 가장 높은 효 율을 나타냈다. Urea는 효율이 일정하게 지속되지 않아 대체 물질로는 적합하지 않음을 확인 할 수 있 었다.
In this study, We evaluated the efficiency of the smart ventilation system being developed at the test-bed(KCL). Smart ventilation system improve the indoor air quality by absorbing carbon dioxide. It is reducing the infusion of outside air can be reduced to minimum energy consumption. To evaluate the energy savings and carbon dioxide removal efficiency. It was more effective when working with air conditioning and ventilation system at the same time.
The experiment was performed using the cleaning precipitator To investigate the absorption efficiency of the SOX/NOX of the aqueous ammonia solution. Concentration of the cleaning liquid is 0.1, 0.5, and 1.0% with increasing absorption efficiency has improved. However, the reaction shown only a difference in time. Absorption efficiency has improved in accordance with the gas residence time. When the direction of the same gas and the cleaning liquid is determined that there is the effect of increasing the residence time. The relative impact of SOX and NOX is this likely to react slower than SOX/NOX. The yield is determined to require
The experiment was performed for in order to remove NOx which is generated in the Ship's engine. it was performed test in order to remove NOx which is generated in the Ship's engine. It was used as the oxidizing agent sodium chlorite. Use the oxidizer is nitrogen monoxide was oxidized to nitrogen dioxide. and was tested pH adjustment to increase the efficiency of oxidizing. An aqueous solution of sodium hydroxide was used for the nitrogen dioxide absorbent. Low concentration of the solution, it showed a high efficiency. improves the absorption efficiency by add additives.
본 연구에서는 이산화탄소 고정화에 있어 이산화탄소 전환을 위해 MEA를 이용한 습식화학흡 수법의 셔틀메카니즘을 도입하였다. 또한 알칼리 무기물질을 다량 함유한 산업부산물을 습식탄산화법을 이용해 처리하고자 하였다. 즉, 산업부산물의 화학적 처리를 통해 칼슘이온을 용출하였다. 산성물질을 이용한 용출상징수를 ICP로 분석한 결과, 칼슘이온이 최대 17,900 ppm(1.79%)을 확보하였다. 또한 MEA를 이용한 습식 흡수공정을 통해 상온, 상압조건의 이산화탄소 분위기에서 94%의 전환률을 얻었 다. 슬러지의 액상탄산화를 통해 슬러지 mg 당 0.175 mg의 이산화탄소를 고정하였으며, 최종생성물의 XRD 분석결과 일반적인 탄산칼슘의 결정구조인 calcite 형상을 확인하였다.
It is important to develop the smart ventilation system in order to minimize a building energy consumption using ventilation. In this study, We evaluated the efficiency of the smart ventilation system being developed at the nursery. To evaluate the energy savings and carbon dioxide removal efficiency, two kinds of experimental conditions were compared. First, air conditioner and Smart HVAC system were operated. Second, air conditioner was operating and external air was put into the inside by rate of air circulation. It was more effective when working with air conditioning and ventilation system at the same time. If the Smart HVAC system is applied in a multi-use facility, indoor air quality will be comfortable and the social cost will be reduced.
In recent years, researchers have put a considerable effort to decrease the emission of harmful gaseous pollutants to the atmosphere. In order to remove simultaneously SO₂ and NOx from the flue gas of small and medium-sized ship, we designed minimal wet scrubber inside a compact multistage modular system. In this study we proceed experiment of elemental technology at each stage of the scrubber. The each stage is oxidation of NO which is the main component of NOx, and removal of SO₂, respectively. NaClO₂ was used to oxidize NO gas, and NaOH was used to remove SO₂gas. The maximum NO conversion efficiency and the SO₂ removal ficiency are both indicate 100%.
In this study, a liquid carbonation method was applied for producing precipitate calcium carbonate by liquid-liquid reaction. We recycled the recycling water of ready-mixed concrete, one of construction waste for use source of carbonate ion. A supernatant separated from the recycling water of ready-mixed concrete, as a result of ICP analysis of a cation, Ca²+ was contained up to 1100 ppm. We used MEA as a CO₂ absorbent for the liquid carbonation. A precipitate CaCO₃ was produced at more than MEA 20 wt%. The precipitate CaCO₃ as a final product was separated and dried. The result of XRD was confirmed the generation of CaCO₃ to calcite structure.
In this study, CO₂ adsorbent was produced for minimizing energy loss due to ventilation within the building. For improved selectivity about low concentration of CO₂ in multiple-use facilities, the ball type adsorbent was modified from a commercial zeolite, alumina, alkali metals and activated carbon with mixing LiOH, binder, and H₂O. We measured specific surface area, pore characteristic, and crystal structure of the modified adsorbent. Effects of alkalization on the absorptive properties of the adsorbents were investigated. Continuous column tests (2,000 ppm) and batch chamber tests (4m3, 5,000ppm) showed that the modified adsorbent indicated about the selectivity of CO₂ more than 9.7% (0.613 mmol/g) compared with ordinary adsorbents and CO₂ removal efficiency of 88.8% within l hour, respectively. It was estimated that the modified adsorbent was applicable to indoor environments.